JP2004119084A - Fuel cell - Google Patents

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Publication number
JP2004119084A
JP2004119084A JP2002278171A JP2002278171A JP2004119084A JP 2004119084 A JP2004119084 A JP 2004119084A JP 2002278171 A JP2002278171 A JP 2002278171A JP 2002278171 A JP2002278171 A JP 2002278171A JP 2004119084 A JP2004119084 A JP 2004119084A
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Prior art keywords
air
water
flow path
separator
fuel cell
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JP2002278171A
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JP4221985B2 (en
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Munehisa Horiguchi
堀口 宗久
Hidemi Kato
加藤 英美
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Equos Research Co Ltd
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Equos Research Co Ltd
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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

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Abstract

<P>PROBLEM TO BE SOLVED: To prevent closure of air passage due to invasion of liquid water into the air passage in a fuel cell separator. <P>SOLUTION: The fuel cell comprises a separator 10B between the mutually adjoining unit cells 10A. The separator comprises the air passage S1 at least on the surface side contacting with the air pole 12 of the fuel cell and a cooling space S2 as a cooling means, on the rear side, where the air and water are supplied, and the cooling space is communicated with the air passage through a communicating hole 143 formed in the separator, and the end part on the entrance side of the air passage is closed to the supply of the air and water by a lid 145 formed in one body at the end part of the separator. Thereby, the invasion of water in liquid state into the air passage is prevented without installing any special member. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、燃料電池に関し、特にその単位セル間に介挿されるセパレータを利用した燃料電池の冷却技術に関する。
【0002】
【従来の技術】
燃料電池の一形式としてのPEM型燃料電池の単位セルは、燃料極(一般に燃料として水素ガスが用いられることから、水素極ともいう)と酸化剤極(同様に酸化剤として酸素を含むガスである空気が用いられることから、以下これを空気極という)との間に高分子固体電解質膜が挟持された構成とされる。燃料極と空気極は、共に触媒物質を含む触媒層と、触媒層を支持するとともに反応ガスを透過される機能を有する電極基材からなる。燃料極と空気極の更に外側には、反応ガスとしての水素と空気をセル外部から電極面に均一に供給するとともに、反応ガスの余剰分をセル外部に排出するためのガス流路(一般に電極面側が開いた溝で構成される)を設けたセパレータ(コネクタ板)が積層される。このセパレータは、ガスの透過を防止するとともに、発生した電流を外部へ取り出すための集電を行う。上記のような単位セルとセパレータとで1ユニットの単電池が構成される。
【0003】
実際の燃料電池では、かかる単電池の多数個が直列に積層されてスタックが構成される。このような、燃料電池では、十分な発電効率を維持するために、単位セル中の高分子固体電解質膜を十分に湿潤状態に保つ必要があり、一般に、電解反応により生成する水のみでは水分が不足することから、各単位セルに加湿水を供給する手段を必要とする。また、電解反応により発生電力にほぼ相当する熱量の熱が発生するため、燃料電池本体が過度にヒートアップすることを防止する冷却手段が講じられる。
【0004】
燃料電池の冷却手段としては、従来より種々の方式のものが提案されている。それらのうちの一方式として、空気極に酸化剤としての空気を送り込むための空気マニホールド内に、水を噴射するノズルを設ける構成を採り、ガス流路に送り込む空気に水を噴射して予め混入させ、ガス流路中で水が加熱により蒸発する際の潜熱を利用して冷却するものがある。この方式のものは、本来、単位セルを湿潤状態に保つ必要があることからセルへの供給を必須とする水を、同じく空気極側への供給を必要とする空気の流れに乗せて供給し、この水を冷却にも利用するのが合理的であるとする着想に基づいている。
【0005】
上記のような方式を採る燃料電池システムにおいて、出願人は、先の出願に係る特願2002−54839において、空気マニホールド内で水を噴射混入させた空気を、セパレータに形成した冷却空間から連通孔を経て空気流路に供給する方式のものを提案している。この方式では、冷却空間に伝わる単位セルの熱により蒸発する水の潜熱により単位セルが冷却され、蒸気化した水が空気と共に空気流路に供給される。これによりセパレータを介して単位セルを冷却しながら、空気流路への液体水又は霧状の水の侵入による流路の閉塞が防止される。すなわち、上記のような仕組みの燃料電池装置の場合、冷却空間に供給された空気と水は、燃料電池の発電時に発生する発熱を潜熱冷却するのに使われる。そして、液体の状態で供給された水の一部は冷却空間内で蒸発し、空気と一緒に水蒸気として連通孔から空気流路へ供給され、空気は燃料電池の反応に使われ、水蒸気は加湿に使われる。
【0006】
上記のような供給方式を採る場合、空気流路に冷却空間と同様に空気と水を供給すると、液体の状態で供給された水により空気流路が閉塞する可能性があるため、空気と水の供給を専ら冷却空間に限って行ない、空気流路への空気と水の供給は、冷却空間を介する供給として、水を水蒸気の状態で空気と共に空気流路に供給されるようにするのが望ましい。
【0007】
【発明が解決しようとする課題】
ところで、セパレータ内の空気流路と冷却空間は、互いに隣接させて交互に配置されることから、空気と水を供給する空気マニホールドに対して、空気流路の入口側も冷却空間の入口部を挟んで切れ切れに位置するため、これら空気流路の入口側を空気と水の供給に対して閉鎖しようとしても、これを一つの部材で被蓋することは事実上不可能である。そこで、個々の空気流路の入口部に何らかの詰め物をして閉鎖する方法も考えられないではないが、こうした方法は、燃料電池セパレータの製造工数を著しく増加させる要因となり、実用性に乏しいものである。
【0008】
そこで本発明は、上記のような課題を解決すべく、セパレータにおける空気流路の入口側を製造工数の増加を伴わない方法で閉鎖し、それにより燃料電池セルへの空気と水の供給に対して、冷却空間を介する空気流路への空気と水蒸気の供給を可能とした燃料電池を提供することを目的とする。
【0009】
【課題を解決するための手段】
前記の目的は、互いに隣接する単位セルの間にセパレータが配置される燃料電池において、前記セパレータは、単位セルの少なくとも空気極に接する表面側に設けられた空気流路と、背面側に設けられて空気と水とを供給される冷却空間とからなり、該冷却空間に伝わる単位セルの熱により蒸発する水の潜熱により単位セルを冷却する冷却手段を備え、前記冷却空間は、セパレータに形成した連通孔を介して空気流路に連通され、該空気流路の入口側端部は、セパレータの端部に一体形成した蓋部により空気と水の供給に対して閉鎖されていることを特徴とする構成により達成される。
【0010】
この構成における、前記セパレータは、冷却空間を画成する空間画成部材を備え、前記蓋部は、空間画成部材の端部に形成された構成とするのが有効である。具体的には、前記セパレータの空間画成部材は、導電性金属板材料のプレス成形品からなる一対の板状部材を板面方向に互いに当接させてなり、両板状部材の間に冷却空間を画成するとともに、一方の板状部材の端部の屈曲により蓋部を構成するものとされる。この場合、前記セパレータの空間画成部材は、一方の板状部材の他端部の屈曲により形成された流路狭窄部を有する構成とするのが有効である。より具体的には、前記一方の板状部材は、その板面を隆起させる屈曲により形成されて板状部材を縦断して延びる波状屈曲部と、縦方向の端部で波状屈曲部の山部間に挟まれる谷部を山部方向に傾斜させる屈曲により形成されて先端を山部と面一(同一平面)にされた傾斜部を有し、他方の板状部材と協働して波状屈曲部の内側に冷却空間を画成するとともに、傾斜部を蓋部として空気流路の入口側端部を閉鎖する構成とされる。
【0011】
【作用】
本発明の各請求項に記載の構成では、燃料電池セルの空気極へ導くべく供給される空気と水が、空気流路については、その入口側端部を被蓋する蓋部により直接の侵入を遮られ、専ら冷却空間に供給される。そして、冷却空間に供給された水はセルからセパレータに伝わる熱で加熱されて水蒸気状態になり、空気流に乗ってセパレータの連通孔を通って空気流路に供給され、空気極の湿潤と冷却に利用される。そして、空気流路に入った余剰の空気と蒸気は、セパレータと空気極の空気流路の下部開口から排出される。この間、冷却空間内で加熱により水が蒸発することでセパレータから熱を奪う潜熱冷却作用が生じる。
【0012】
また、空気流路に入らなかった空気と水は、セパレータの冷却空間の端部開口から排出されるが、流路狭窄部を有するものでは、液体水状態の水が流路狭窄部に至って滞留することで流路を塞ぐ現象が生じ、この水が冷却空間からの空気の直接の排出を妨げる作用をする。したがって、流路狭窄部を有するものでは、冷却空間に供給された空気は、実質上全て空気流路に送り込まれてから、空気流路を経て排出されるようになる。また、この場合の空気に対する閉栓機能を果たす液体水は、流路狭窄部に滞留する最下部の水が上部の水に押され、水滴となって落下することで順次排水される。
【0013】
【発明の実施の形態】
以下、図面を参照して、本発明の実施形態を説明する。先ず、図1は、この発明の適用に係る車両用燃料電池システムの構成例を示す。このシステムは、燃料電池スタック1と、燃料電池スタック1に燃料としての水素を供給する燃料供給系(図に2点鎖線で示す)2と、同じく燃料電池スタック1に酸化ガスとしての空気を供給する空気供給系(図に1点鎖線で示す)3と、燃料電池スタック1を含むシステムの所要箇所に主として冷却のために水を供給する水供給系(図に実線で示す)4と、発電負荷としての電気負荷系(図に破線で示す)5から構成されている。
【0014】
燃料電池スタック1は、板状の単電池を板厚方向に多数積層集合させて構成されている。図2に横断面、図3に縦断面を示すように、単電池10は、単位セル10Aとセパレータ10Bとで構成されている。なお、説明の都合上、図2には隣接する単位セルも併せて示し、図3では単位セルの図示は省略されている。単位セル10Aは、固体高分子電解質膜11を空気極12と燃料極13とで挟持したものとされており、セパレータ10Bは、その詳細な構造については後に詳記するが、2枚合わせの薄板金属板14,15の四囲を絶縁体枠16,17で囲った構成とされている。セパレータ10Bには、燃料供給系2の水素供給路20に連通する水素流路L1,L2と、空気供給系3の空気マニホールド34に冷却空間S2を介して連通する空気流路S1が形成されており、燃料電池スタック1は、水素流路L1,L2を水平方向、空気流路S1を垂直方向に向けた姿勢で、空気マニホールド34に接続された収容筐体内に配置されている。
【0015】
図1に戻って、燃料供給系2は、水素吸蔵合金を燃料としての水素の貯蔵部21として構成され、該貯蔵部21と燃料電池スタック1をつなぐ水素供給路20の途中に、燃料電池スタック1への供給圧を調節する水素調圧弁23と、供給遮断を制御する水素供給電磁弁24が直列に介挿されている。燃料供給系2に関連して、燃料電池スタック1にはそれから必要に応じて水素を抜くための水素排気路27が設けられ、その途中に、排気路開閉のための水素排気電磁弁29と、外気の吸込みを防ぐ水素排気逆止弁28とが介挿されている。なお、水素供給路20には、水素調圧弁23による調圧前後のガス圧を計測する水素1次圧センサ22及び2次圧センサ25が設けられている。
【0016】
空気供給系3は、外気をフィルタ及びヒータを経て空気マニホールド34に送り込む空気供給ファン31を配置したダクトと、燃料電池スタック1と水素吸蔵合金の貯蔵部21とをつなぐダクトと、貯蔵部21と水凝縮器46とをつなぐダクトと、水凝縮器46からフィルタを経て使用済みの空気を外気に放出する排出路とで構成されている。この空気供給系3には、更に、燃料電池スタック1に供給される空気の温度を必要に応じたヒータ作動のために空気供給ファンの上流側で監視する吸気温度センサ32と、燃料電池スタック1下流のダクトに付設して燃料電池スタック1から排出される空気の温度を監視する排気温度センサ37も設けられている。
【0017】
水供給系4は、水タンク40を中心として、該水タンク40から水噴射ポンプ41により送り出される水を、空気マニホールド34に水噴射ノズル45により供給し、かつ、貯蔵部21の水素吸蔵合金に吸蔵ノズル46により供給し、燃料電池スタック1で回収及び生成された水と、水凝縮器46での凝縮により生じた水を直接水タンク40に戻す循環路で構成されている。循環路の供給側を構成する水噴射ポンプ41から水噴射ノズル45に至る水路の途中には、噴射量を調節する直噴水電磁弁43が介挿され、水噴射ポンプ41の吸込み側にはノズル45の詰りを防止するためのフィルタ42が介挿されている。水噴射ポンプ41から吸蔵ノズル46に至る水路の途中にも同様に噴射量を調節する吸蔵電磁弁47が介挿されている。循環路の回収側は、燃料電池スタック1から水タンク40に戻る水路と、水凝縮器46からポンプ44を経て水タンク40に戻る水路とで構成されている。この水タンク40には、水温センサ47と水位センサ48が設けられ、タンクの水温と水位の監視が可能とされている。
【0018】
燃料電池の電気負荷系5は、燃料電池スタック1からリレー53を経てモータ52制御のためのインバータ51につながる導線で構成されている。このシステムでは、燃料電池装置の空気供給ファン31、水凝縮器46のファン、水噴射ポンプ41、水タンク40の凍結対策ヒータ、各種電磁弁等の付帯設備の駆動電源として、蓄電池からなる2次電池54が設けられており、2次電池54は燃料電池に対して並列に接続されている。この2次電池54は、モータ52の回生電流を蓄積し、また、燃料電池の出力が不足している場合には、出力を補う用途にも用いられる。
【0019】
こうした構成からなる燃料電池システムでは、水素供給電磁弁24を閉じ、図示しない充填路からの水素ガスの供給で水素吸蔵合金への水素の吸蔵が行われる。また、水供給系4への水の供給は、給水電磁弁48を開いて、水タンク40へ水を供給することにより行われる。そして、発電状態では、水素供給電磁弁24を開いて、水素調圧弁23による調圧下で水素吸蔵合金に吸蔵させた水素を燃料電池スタック1に供給する一方、空気供給ファン31を起動させて、空気マニホールド34経由で燃料電池スタック1に空気を送り込む操作が行われる。この発電状態で、必要に応じて連続又は間歇的に水供給系4の水直噴ポンプ41を運転しながら直噴水電磁弁43を開いて水噴射ノズル45から空気マニホールド34内に水を噴射させることで、燃料電池スタック1への供給空気に霧状に水を混入させる操作が行われる。この水は、空気と共に燃料電池スタック1の各セパレータの図2及び図3に示す冷却空間S2の上部開口から冷却空間S2に入り、蒸気化されて空気流路S1を経て各単電池の空気極12側に供給されるものを除き冷却空間S2の排出部を構成する下部開口から筐体下部に排出され、水タンク40に回収される。
【0020】
上記のようにして燃料電池スタック1に送り込まれ、燃料電池スタック1で加熱された空気と水蒸気状態の水は、筐体の下部からダクトを経て水素吸蔵合金の貯蔵部21に入り、水素吸蔵合金を加熱した後、ダクトを経て水凝縮器46に導かれ、乾燥状態の空気と凝縮水とに分けられ、乾燥状態の空気はフィルタ経由で外気に放出され、凝縮水はポンプ44を経て水タンク40に戻る。また、液状のまま燃料電池スタック1を抜けた水は、直接水タンク40に戻る。
【0021】
このシステムの特徴は、燃料電池スタック1における空気流路S1と冷却空間S2とを一本化した流通経路に配置でき、同時に空気と水を流通させることができるので、冷却のための装置を別に設ける必要がない点にある。
【0022】
次に、燃料電池スタック1の各単電池10の単位セル10A間に介挿されるセパレータ10Bの詳細な構成を説明する。図4に構成部材を分解して示すように、セパレータ10Bは、単位セル10Aの空気極12と燃料極13(図2参照)に接触して電流を外部に取り出すための対を成す集電部材14,15と、それらに重ね合わされて単位セル10Aを支持する枠体16,17とを備えている。集電部材14,15は、この形態では、薄板金属板、例えば板厚が0.1mm程度のもので構成されている。この構成金属は、導電性と耐食性を備えた金属で、例えば、ステンレス、ニッケル合金、チタン合金等に耐蝕導電処理を施したもの等が挙げられる。
【0023】
一方の集電部材14は、冷却空間S2を画成する空間画成部材の一方を構成すべく、横長の矩形の板材からなり、板面を所定の範囲で部分的に隆起させるプレス加工によって、複数の凸部141が押出し形成されている。これら凸部141は、連続する直線状で、板材の縦辺(図示の形態における短辺)に平行かつ等間隔で、板面を完全に縦断する配置とされ、それにより全体として波状屈曲部140を構成している。そして、集電部材14の縦方向の上端部には、波状屈曲部140の山部すなわち凸部141間に挟まる谷部を山部方向に傾斜させる屈曲により、先端部を山部と面一にされた、本発明の主題に係る蓋部として機能する傾斜部145が形成されている。更に、各凸部141は、それらの下部が板厚方向に押し潰されて偏平化されている。これら傾斜部145と凸部141の偏平化部分141’を除く部分の断面形状は、図2では、便宜上大まかに矩形波状断面で示されているが、プレス加工の型抜きの関係から、根元側が若干裾広がりの形状とするのがより実際的である。
【0024】
図2を参照して、凸部141の間に画定され、単位セル10Aの空気極12に面する側が開いた溝状の空間S1は、後に詳記するように、空気極12側に空気を流通させる空気流路として使用される。各凸部141の頂部142の平面は、空気極12が接触する当接部となっている。また、凸部141の裏側に画定される溝状の空間S2は、同じく後に詳記する冷却空間(本形態では流路)として使用される。そして、これら空気流路S1と冷却空間S2を部分的に連通させるべく、集電部材14を貫通する多数の通孔143が形成されている。これら通孔143の開設位置は任意であるが、凸部141の両側面が常識的である。更に、集電部材14の横辺(図示の形態における長辺)方向の両端部近傍には、縦方向に長い長円孔144が形成されている。この長円孔144は、集電部材14を集電部材15と枠体16,17とに重ねてセパレータ10Bを積層した場合に、これら各部材を整合して貫通する水素流路L1,L2を構成する。
【0025】
図4に戻って、他方の集電部材15は、冷却空間S2を画成する空間画成部材の他方を構成すべく、集電部材14と合致する矩形の板材からなり、プレス加工によって、複数の凸部151が押出し形成されている。凸部151は、頂部152(図2参照)が平坦で、断面形状も、先の凸部141の場合と同様に実質上矩形波状とされているが、この形態の場合の凸部151は、縦方向に間欠的に設けられている。すなわち、凸部151は、横方向(長辺方向)の配設ピッチを集電部材14の凸部141の配設ピッチに合わせ、縦方向(短辺方向)の配設ピッチを適宜の間隔とした円形又は矩形の突起とされている。図2における左半分の断面は、これら凸部151の配列部分での截断面を表し、右半分の断面は、配列部分間での截断面を表す。これら凸部151の間に形成される縦横の空間S3は、単位セル10の燃料極13に面する側が開いた面状の空間を構成し、燃料である水素が流通する水素流路とされる。これら凸部151の頂部152の平面は、燃料極13が接触する当接部となっている。また、凸部151の裏側は、集電部材14に面する側が開いた短筒状の空間S4となっていて、集電部材14の空間S2に合わさっており、結果的に冷却空間S2を介して、両端が板材の長辺部に開口する開口部を備える構成となる。この集電部材15にも、集電部材14と同様に長辺方向の両端部近傍に、短辺方向に長い長円孔153が形成され、集電部材14と枠体15,16とに重ねてセパレータ10Bを積層した場合に、これら各部材を整合して貫通する水素流路L1,L2を構成する。この形態において、凸部151を燃料極13に対して小面積で間欠的に当接する短柱状としているのは、これにより柱状の凸部151の間をぬう水素流路S3が縦横に形成され、水素ガスの流れの滞留やよどみを抑制できることを狙ったものである。また、こうすることで、燃料極13に対する水素ガスの接触面積が大きくなるので、発電効率の向上も期待できる。
【0026】
上記の構成からなる集電部材14,15は、各凸部141,151が共に外側となるように重ね合わされて固定される。このとき、凸部141,151を形成していない板面部分、すなわち水素流路S3の裏側面と空気流路S1の裏側面が当接した状態となり、相互に通電可能な状態となる。また、集電部材14,15を重ね合わせることによって、それらの間に、空間S2と空間S4が合わさった冷却空間が形成される。また、単位セル10Aが集電部材14に合わさることで、空間S1の開放面側が閉鎖され、管状の空気流路が構成され、この流路を囲む壁の一部が空気極12で構成されることになる。そしてこの空気流路S1から、単位セル10Aの空気極12に空気と水が供給される。同様に、単位セル10Aが集電部材15に合わさることで、空間S3の開放面側が閉鎖され、面状の水素流路が構成され、この流路を囲む壁の一部が燃料極13で構成されることになる。そしてこの燃料流路S3から、単位セル10Aの燃料極13に水素が供給される。
【0027】
前記の構成からなる集電部材14,15には、枠体16,17がそれぞれ重ねられる。図3及び図4に示すように、集電部材14に重ねられる枠体16は、集電部材14と実質上同じ外形形状とされ、両側の縦枠部161を上下の横枠部162,163で連結した構造とされ、下方の横枠部163は、両側の縦枠部161の下辺及び集電部材14,15の下辺と面一にならないように、これらの下辺より横枠部163の下辺が上方に位置するように全体を若干上方にずらした位置に配置されている。これらの枠で囲まれる中央には、集電部材14の凸部141を収納する窓164が画定されている。また、この枠体16にも、その両端部近傍に、集電部材14の長円孔144に合致する位置及び形状の長円孔165が形成されている。枠体16の横枠部162,163と、これらが連結される部分の縦枠部161は、縦枠部161全体の厚さより薄肉とされ、これらの肉厚の関係から、集電部材14が重ねられる側の面の横枠部162,163は、集電部材14の凸部形成範囲に対応する位置で、短辺方向全体に渡って集電部材14との当接面より後退した面を形成している。したがって、枠体16が集電部材14に重ねられた状態では、集電部材14の凸部141は、窓164内では単位セル10Aの空気極12に接触し、横枠部162,163に対峙する部分では、それらに当接する関係となる。かくして、集電部材14と枠体16との間には、上部で集電部材14の凸部141と横枠部162の内側面、窓164部で集電部材14の凸部141と単位セル10Aの空気極12面、下部で集電部材14の凸部141と横枠部163の内側面で囲われた多数の管状空間として、上端が蓋部145の先端の横枠部162内面への当接により塞がれ、下端が横枠部163と集電部材14との間に開放された縦方向に延びる空気流路S1が画定される。
【0028】
集電部材15に重ねられる枠体17は、枠体16より縦方向寸法の短い枠状に構成され、この場合、本体部分170には、窓171より横方向に大きな開口が形成されている。この開口の高さは、窓171の高さを画定するが、開口の幅は、集電部材15の両端の長円孔153の外端間の幅に合致する幅とされている。そして、この開口の幅方向両端の近傍に、一対の縦枠部172が設けられている。この両縦枠部172に挟まれる幅が窓171の横幅を画定し、両縦枠部172と本体部分170の開口の幅とで画定される幅が、集電部材15の両端の長円孔153の横幅に合致する寸法とされ、実質的に長円孔153の位置と形状に合致する長孔173が構成されている。縦枠部172は、本体部分170より薄肉とされ、これらの肉厚の関係から、集電部材15が重ねられる側の面の縦枠部172が設けられた位置で、集電部材15の凸部151の高さに相当する分だけ、当接面より後退した面を形成している。したがって、枠体17が集電部材15に重ねられた状態では、集電部材15の凸部151は、縦枠部172では縦枠部172に当接し、窓171内では単位セル10Aの燃料極13に接触する当接関係となる。このようにして長孔173に挟まれる部分には、凸部151をぬうように一様に形成された面状の水素流路S3が構成される。
【0029】
更に図面上には表れていない細部構成について説明すると、望ましくは、冷却空間S2を構成する流路の断面積を上辺側から下辺側に向かうにしたがって順次小さくなる設定とする。こうした構成を採ることで、冷却空間S1から空気流路S2に流れる空気の圧力損失を低減することができる。こうした流路構成は、集電部材14の凸部141の高さあるいは幅又はそれら両方を適宜設定することで実現できる。
【0030】
また、空気流路S1及び冷却空間S2の内壁面には、必要に応じて親水性処理が施される。この処理は、具体的には、内壁表面と水の接触角が40°以下、好ましくは30°以下となるような表面処理とされる。処理方法としては、親水処理剤を、表面に塗布する方法が採られる。塗布される処理剤としては、ポリアクリルアミド、ポリウレタン系樹脂、酸化チタン(TiO2)等が挙げられる。この他の親水性処理としては、金属表面の粗さを粗化する処理が挙げられる。例えば、プラズマ処理などがその例である。親水性処理は、最も温度が高くなる部位に施すことが好ましく、例えば、単位セル10Aに接触している凸部141の頂部142の裏側の冷却空間内壁表面F1、凸部141表側の空気流路側壁表面F2と裏側の冷却空間側壁表面F3、空気流路底面F4の順で、優先的に処理されていることが望ましい。さらに、冷却空間S2の一部を構成する凸部151の内壁表面F5にも親水性処理を施してもよい。親水性処理を施すことにより、内壁面の濡れが促進され、水の潜熱冷却による効果が向上する。
【0031】
以上のように構成された枠体16,17によって集電部材14,15を保持してセパレータ10Bが構成され、セパレータ10Bと単位セル10Aを交互に積層して、燃料電池スタック1が構成される。こうして積層された燃料電池スタック1の上面には、図5に示すように、多数の冷却空間S2の開口が間隔を置いて横方向に並び、枠体17と枠体16の横枠部162の厚さを合わせた分の間隔を置いて、同配列の開口が積層方向に並んだ空気と水の取入れ部が構成される。また、燃料電池スタック1の下面には、図6に示すように、長方形の空気流路の排出部の中に冷却空間S2の流路狭窄部S2’下端の開口が間隔を置いて横方向に並び、枠体17と枠体16の横枠部163の厚さを合わせた分の間隔を置いて、同配列の開口が積層方向に並んだ水の排出部が構成される。
【0032】
以上の構成からなる燃料電池の各単電池における本発明の主題に係る構成を纏めると、図3に示すセパレータの縦断面及び図5に示すセパレータの上面を参照して、空気流路S1の入口側端部は、セパレータ10Bにより空気と水の供給に対して閉鎖されている。セパレータ10Bは、冷却空間S2を画成する空間画成部材として集電部材14,15を備えることから、空気流路S1の入口側端部は、集電部材14により閉鎖されている。セパレータ10Bの集電部材14,15は、導電性金属板材料のプレス成形品からなる一対の板状部材を板面方向に互いに当接させてなり、両板状部材の間に冷却空間S2を画成するとともに、一方の板状部材すなわち集電部材14の端部の屈曲により空気流路S1の入口側端部を閉鎖している。集電部材14は、その板面を隆起させる屈曲により形成されて板状部材を縦断して延びる波状屈曲部140と、縦方向の端部で波状屈曲部140の山部間に挟まれる谷部を山部方向に傾斜させる屈曲により形成されて先端を山部と面一にされた傾斜部145を有し、他方の板状部材15と協働して波状屈曲部140の内側に冷却空間S2を画成するとともに、傾斜部145により空気流路S1の入口側端部を閉鎖している。
【0033】
こうした構成からなる燃料電池スタックは、その各単電池に空気と水及び水素を供給することで、図7に模式化して示すように作動する。この形態の場合、空気と水は、スタックの上面から一様に供給されることから、空気流路S1には直接水が入らないように、空気流路S1の開口部は、集電部材14上部の傾斜部145で閉鎖されている。図示のように、冷却空間S2に供給される空気と水は、空気流中に水滴が霧状に混入した状態(以下この状態を混合流という)で冷却空間の上部に入る。燃料電池の定常運転状態では、単位セル10Aが反応により発熱しているため、冷却空間S2内の混合流が加熱される。混合流中の水滴は、親水性処理により冷却空間S2壁面に付着し、加熱により蒸発して壁面から熱を奪う潜熱冷却作用が生じる。こうして蒸気となった水は、図に網掛けの矢印で示すように、通孔143から図に白抜き矢印で流れを示す空気と共に空気流路S1に入り、単位セル10Aの空気極12側に付着し、空気極12を湿潤させる。そして、空気流路S1に入った余剰の空気と蒸気は、燃料電池スタックの下方の空気流路S1の下部開口から排出される。
【0034】
これに対して、空気流路S1に入らなかった空気と水は、そのままでは燃料電池スタックの下方の冷却空間S2の下部開口から排出されることになるが、流路狭窄部S2’の作用で、壁を伝って流下する液体水状態の水が流路狭窄部S2’に至って滞留することで毛細管現象により流路を塞ぐ現象が生じ、この水が冷却空間S2からの空気の直接の排出を妨げる作用をする。したがって、冷却空間S2に供給された空気は、実質上全て空気流路S1に送り込まれてから、空気流路S1を経て燃料電池スタックから排出されるようになる。また、空気に対する閉栓機能を果たす液体水は、流路狭窄部S2’に滞留する最下部の水が上部の水に押され、水滴となって落下することで順次排水される。
【0035】
一方、燃料流路S3への水素の供給は、各単電池10の両側をそれらの積層方向に貫く水素流路L1,L2(図2参照)の一方から、縦枠部172と凸部151の間の空間を通して、それにつながる燃料流路S3から行なわれる。これにより単位セル10Aの燃料極13への水素の供給が行なわれる。この燃料極13側では、燃料流路S3に入った余剰の水素は、反対側の水素流路に排出され、この水素流路につながるシステムの配管により排出又は回収される。
【0036】
以上詳述したように、この形態によると、空気流路S1の入口側端部の閉鎖がセパレータ10Bの端部に一体形成した蓋部145によりなされるため、各空気流路S1毎の入口側端部に詰め物をするような製造工数の増加や、切れ切れの空気流路S1の入口側端部を塞ぐ複雑な蓋部材をセパレータ10Bに付加する等の構造の複雑化や部品点数の増加を招くことなく、簡単な構成で空気流路S1の入口側端部を閉鎖することができる。そして、これにより冷却空間S2を介する空気流路S1への空気と水蒸気の供給を実現し、空気流路S1へ空気と水を直接供給する場合のような、水による空気流路S1の閉塞の懸念をなくすことができる。
【0037】
また、冷却空間S2を画成する空間画成部材14の端部を蓋部145とすることで、セパレータ10Bを構成する枠体16,17等の他の部材に影響を与えることなく、空気流路S1の入口側端部の閉鎖が可能である。更に、蓋部145を板状部材14の屈曲による構成しているため、セパレータ10Bを構成する金属材料製の空間画成部材14に冷却空間S2を形成させる加工と同時に加工が可能であり、加工工数の増加も防ぐことができる。また、空間画成部材を構成する板状部材14の両端部に屈曲により形成される蓋部145と流路狭窄部S2’を有することになるため、空間画成部材のプレス加工の際に板材にかかる応力を両端部についてバランスさせることができ、それにより板材の板面内の反り、すなわち板材の一方の辺が縮んで扇状に変形する現象を防ぐことができ、プレス加工精度が向上する。また、蓋部145が傾斜部とされることで、冷却空間S2と空気流路S1を画成する波状屈曲部140に対して滑らかにつながる形状となるため、板状部材をプレス加工性に優れた形状とすることができる。
【0038】
以上、本発明の理解のために実施形態を例示したが、本発明は例示の実施形態に限定されるものではなく、特許請求の範囲に記載の事項の範囲内で、種々に具体的構成を変更して実施可能なものである。
【0039】
【発明の効果】
本発明の請求項1に記載の構成によれば、空気流路の入口側端部の閉鎖がセパレータの端部に一体形成した蓋部によりなされるため、各空気流路毎の入口側端部に詰め物をするような製造工数の増加や、切れ切れの空気流路の入口側端部を塞ぐ複雑な蓋部材をセパレータに付加する等の構造の複雑化や部品点数の増加を招くことなく、簡単な構成で空気流路の入口側端部を閉鎖することができる。そして、これにより冷却空間を介する空気流路への空気と水蒸気の供給を実現し、空気流路へ空気と水の直接供給する場合のような、水による空気流路の閉塞の懸念をなくすことができる。
【0040】
また、請求項2に記載の発明によれば、冷却空間を画成する空間画成部材の端部を空気流路の入口側端部の蓋部とすることで、セパレータを構成する他の部材に影響を与えることなく、空気流路の入口側端部の閉鎖が可能である。
【0041】
更に、請求項3に記載の発明によれば、空気流路の入口側端部の蓋部を板状部材の屈曲による構成しているため、セパレータを構成する金属材料製の空間画成部材に冷却空間を形成させる加工と同時に加工が可能であり、加工工数の増加も防ぐことができる。
【0042】
また、請求項4に記載の構成によれば、空間画成部材を構成する板状部材の両端部に屈曲により形成される蓋部と流路狭窄部を有することになるため、空間画成部材のプレス加工の際に板材にかかる応力を両端部についてバランスさせることができる。この結果、板材の板面内の反り、すなわち板材の一方の辺が縮んで扇状に変形する現象を防ぐことができ、プレス加工精度が向上する。
【0043】
また、請求項5に記載の構成によれば、板状部材の蓋部が傾斜部とされることで、冷却空間と空気流路を画成する波状屈曲部に対して滑らかにつながる形状となるため、板状部材をプレス加工性に優れた形状とすることができる。
【図面の簡単な説明】
【図1】本発明の適用に係る燃料電池システムの構成図である。
【図2】本発明の実施形態に係る単電池の部分横断面図である。
【図3】実施形態の単電池の部分縦断面図である。
【図4】実施形態の単電池を構成するセパレータの分解斜視図である。
【図5】実施形態に係る単電池の部分上面図である。
【図6】実施形態に係る単電池の部分底面図である。
【図7】実施形態のセパレータによる冷却と排水のメカニズムを示す模式図である。
【符号の説明】
10A 単位セル
10B セパレータ
12 空気極
14,15 導電部材(空間画成部材、板状部材)
140 波状屈曲部
143 連通孔
145 傾斜部(蓋部)
S1 空気流路
S2 冷却空間(冷却手段)
S2’ 流路狭窄部
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a fuel cell, and more particularly to a fuel cell cooling technique using a separator interposed between unit cells of the fuel cell.
[0002]
[Prior art]
A unit cell of a PEM fuel cell as one type of fuel cell includes a fuel electrode (generally referred to as a hydrogen electrode because hydrogen gas is used as fuel) and an oxidant electrode (also a gas containing oxygen as an oxidant). Since a certain air is used, this is hereinafter referred to as an air electrode) and a solid polymer electrolyte membrane is sandwiched between the two. Each of the fuel electrode and the air electrode includes a catalyst layer containing a catalyst substance, and an electrode base material that supports the catalyst layer and has a function of transmitting a reaction gas. Further outside the fuel electrode and the air electrode, a gas flow path (generally, an electrode) for supplying hydrogen and air as reactant gas uniformly from the outside of the cell to the electrode surface and discharging an excess of the reactant gas outside the cell. Separator (connector plate) provided with a groove having an open surface side) is laminated. This separator prevents gas permeation and performs current collection for taking out the generated current to the outside. The unit cell and the separator as described above constitute one unit cell.
[0003]
In an actual fuel cell, a large number of such unit cells are stacked in series to form a stack. In such a fuel cell, in order to maintain sufficient power generation efficiency, it is necessary to keep the polymer solid electrolyte membrane in the unit cell in a sufficiently wet state. Generally, only water generated by the electrolytic reaction causes moisture to be generated. Because of the shortage, means for supplying humidified water to each unit cell is required. In addition, since the amount of heat substantially corresponding to the generated electric power is generated by the electrolytic reaction, a cooling means for preventing the fuel cell body from excessively heating up is provided.
[0004]
Various types of fuel cell cooling means have been conventionally proposed. As one of these methods, a configuration is adopted in which a nozzle for jetting water is provided in an air manifold for sending air as an oxidant to the air electrode, and water is jetted into the air sent to the gas flow path and mixed in advance. In some cases, cooling is performed using latent heat generated when water evaporates by heating in a gas flow path. In this method, water, which must be supplied to the cell because it is necessary to keep the unit cell wet, is supplied along with the flow of air that also needs to be supplied to the air electrode side. It is based on the idea that it is reasonable to use this water for cooling.
[0005]
In the fuel cell system adopting the above-described method, the applicant has disclosed in Japanese Patent Application No. 2002-54839 according to the earlier application that the air in which water is injected and mixed in the air manifold is connected to the communication space from the cooling space formed in the separator. To supply air to the air flow path. In this method, the unit cells are cooled by the latent heat of water evaporating by the heat of the unit cells transmitted to the cooling space, and the vaporized water is supplied to the air flow path together with the air. Thereby, while cooling the unit cell via the separator, the blockage of the flow path due to the intrusion of liquid water or mist-like water into the air flow path is prevented. That is, in the case of the fuel cell device having the above-described structure, the air and water supplied to the cooling space are used for latent heat cooling of the heat generated during power generation of the fuel cell. Then, a part of the water supplied in a liquid state evaporates in the cooling space and is supplied together with the air as water vapor from the communication hole to the air flow path, the air is used for the reaction of the fuel cell, and the water vapor is humidified. Used for
[0006]
In the case of employing the above-described supply method, if air and water are supplied to the air flow path in the same manner as the cooling space, the air flow path may be blocked by the water supplied in a liquid state. The supply of air and water to the air flow path is limited to the cooling space only, and the supply of air and water to the air flow path is to be supplied to the air flow path together with the air in the form of water vapor as the supply through the cooling space. desirable.
[0007]
[Problems to be solved by the invention]
By the way, since the air flow path and the cooling space in the separator are alternately arranged adjacent to each other, the inlet side of the air flow path also has an inlet portion of the cooling space with respect to the air manifold that supplies air and water. Since they are positioned so as to be cut and sandwiched, it is practically impossible to cover the inlet side of these air flow paths with a single member even if the air flow is to be closed against the supply of air and water. Therefore, it is not surprising that a method of closing the inlet of each air flow path with some kind of padding is conceivable, but such a method significantly increases the man-hours for manufacturing the fuel cell separator, and is not practical. is there.
[0008]
In order to solve the above-described problems, the present invention closes the inlet side of the air flow path in the separator in a method without increasing the number of manufacturing steps, thereby reducing the supply of air and water to the fuel cell. Accordingly, it is an object of the present invention to provide a fuel cell capable of supplying air and water vapor to an air flow path through a cooling space.
[0009]
[Means for Solving the Problems]
The object is to provide a fuel cell in which a separator is arranged between unit cells adjacent to each other, wherein the separator is provided on an air flow path provided on at least a surface side in contact with an air electrode of the unit cell, and provided on a back side. And cooling means for cooling the unit cells by latent heat of water evaporating by the heat of the unit cells transmitted to the cooling space, wherein the cooling space is formed in a separator. It is communicated with the air flow path through the communication hole, and the inlet end of the air flow path is closed to the supply of air and water by a lid integrally formed at the end of the separator. This is achieved by a configuration that
[0010]
In this configuration, it is effective that the separator includes a space defining member that defines a cooling space, and the lid is formed at an end of the space defining member. Specifically, the space defining member of the separator is formed by bringing a pair of plate members made of a press-formed product of a conductive metal plate material into contact with each other in a plate surface direction, and cooling between the two plate members. A space is defined, and a lid is formed by bending an end of one of the plate-like members. In this case, it is effective that the space defining member of the separator has a configuration in which a channel narrowing portion is formed by bending the other end of one plate-like member. More specifically, the one plate-shaped member has a wavy bent portion formed by bending to protrude the plate surface and extending by traversing the plate-shaped member, and a crest of a wavy bent portion at a longitudinal end. A valley portion sandwiched between the valley portions is formed by bending so as to be inclined in the direction of the hill portion, and has an inclined portion whose tip is flush with the hill portion (same plane), and is corrugated in cooperation with the other plate-shaped member. A cooling space is defined inside the portion, and the inlet side end of the air flow path is closed with the inclined portion as a lid.
[0011]
[Action]
In the configuration described in each claim of the present invention, air and water supplied to guide the air electrode of the fuel cell directly enter the air flow path by the lid covering the inlet end. And is supplied exclusively to the cooling space. Then, the water supplied to the cooling space is heated by the heat transmitted from the cell to the separator to be in a water vapor state, and is supplied to the air flow path through the communication hole of the separator riding on the air flow to wet and cool the air electrode. Used for Excess air and steam entering the air flow path are discharged from the lower opening of the air flow path of the separator and the air electrode. During this time, the latent heat cooling action of removing heat from the separator is caused by the evaporation of water by heating in the cooling space.
[0012]
In addition, air and water that have not entered the air flow path are discharged from the opening at the end of the cooling space of the separator. However, in the case of the flow path having the flow path narrowing portion, water in a liquid water state stays at the flow path narrowing portion. This causes a phenomenon of blocking the flow path, and this water acts to prevent direct discharge of air from the cooling space. Therefore, in the one having the flow path constricted portion, substantially all the air supplied to the cooling space is sent to the air flow path and then discharged through the air flow path. In this case, the liquid water that fulfills the function of closing the air is sequentially drained by the lower water remaining in the narrow channel portion being pushed by the upper water and dropping as water droplets.
[0013]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings. First, FIG. 1 shows a configuration example of a vehicle fuel cell system according to an application of the present invention. This system includes a fuel cell stack 1, a fuel supply system (shown by a two-dot chain line) 2 for supplying hydrogen as fuel to the fuel cell stack 1, and air for supplying oxidizing gas to the fuel cell stack 1. An air supply system (shown by a dashed-dotted line in the figure) 3, a water supply system (shown by a solid line in the figure) 4 for supplying water mainly for cooling to required parts of the system including the fuel cell stack 1, and power generation. It comprises an electric load system (shown by a broken line in the figure) 5 as a load.
[0014]
The fuel cell stack 1 is configured by stacking a large number of plate-shaped unit cells in the plate thickness direction. As shown in a horizontal cross section in FIG. 2 and a vertical cross section in FIG. 3, the unit cell 10 includes a unit cell 10A and a separator 10B. For convenience of description, FIG. 2 also shows adjacent unit cells, and FIG. 3 does not show the unit cells. The unit cell 10A has a solid polymer electrolyte membrane 11 sandwiched between an air electrode 12 and a fuel electrode 13, and the separator 10B has a two-piece thin plate, although a detailed structure thereof will be described later. The four metal plates 14 and 15 are surrounded by insulator frames 16 and 17. The separator 10B is formed with hydrogen passages L1 and L2 communicating with the hydrogen supply passage 20 of the fuel supply system 2 and an air passage S1 communicating with the air manifold 34 of the air supply system 3 via the cooling space S2. The fuel cell stack 1 is disposed in a housing connected to the air manifold 34 with the hydrogen flow paths L1 and L2 oriented horizontally and the air flow path S1 oriented vertically.
[0015]
Returning to FIG. 1, the fuel supply system 2 is configured as a storage unit 21 for hydrogen using a hydrogen storage alloy as a fuel, and is provided in a hydrogen supply path 20 connecting the storage unit 21 and the fuel cell stack 1. A hydrogen pressure regulating valve 23 for adjusting the supply pressure to 1 and a hydrogen supply solenoid valve 24 for controlling the supply cutoff are inserted in series. In connection with the fuel supply system 2, the fuel cell stack 1 is provided with a hydrogen exhaust path 27 for extracting hydrogen therefrom as needed, and in the middle thereof, a hydrogen exhaust solenoid valve 29 for opening and closing the exhaust path, A hydrogen exhaust check valve 28 for preventing the intake of outside air is interposed. The hydrogen supply path 20 is provided with a hydrogen primary pressure sensor 22 and a secondary pressure sensor 25 for measuring gas pressures before and after pressure regulation by a hydrogen pressure regulating valve 23.
[0016]
The air supply system 3 includes a duct in which an air supply fan 31 that sends outside air to the air manifold 34 via a filter and a heater is arranged, a duct that connects the fuel cell stack 1 to the storage unit 21 of the hydrogen storage alloy, and a storage unit 21. It is composed of a duct connecting the water condenser 46 and a discharge path for discharging used air from the water condenser 46 through a filter to the outside air. The air supply system 3 further includes an intake air temperature sensor 32 that monitors the temperature of air supplied to the fuel cell stack 1 upstream of an air supply fan for operating a heater as needed, An exhaust temperature sensor 37 attached to the downstream duct and monitoring the temperature of the air exhausted from the fuel cell stack 1 is also provided.
[0017]
The water supply system 4 supplies the water sent from the water tank 40 by the water injection pump 41 to the air manifold 34 by the water injection nozzle 45 around the water tank 40, and supplies the water to the hydrogen storage alloy in the storage unit 21. The circulation path is configured to directly return to the water tank 40 water supplied by the storage nozzle 46 and collected and generated by the fuel cell stack 1 and water generated by condensation in the water condenser 46. In the middle of the water passage from the water injection pump 41 constituting the supply side of the circulation path to the water injection nozzle 45, a direct injection water electromagnetic valve 43 for adjusting the injection amount is interposed, and a nozzle is provided on the suction side of the water injection pump 41. A filter 42 for preventing clogging of 45 is inserted. Similarly, a storage solenoid valve 47 for adjusting the injection amount is inserted in the middle of the water passage from the water injection pump 41 to the storage nozzle 46. The recovery side of the circulation path includes a water path returning from the fuel cell stack 1 to the water tank 40, and a water path returning from the water condenser 46 to the water tank 40 via the pump 44. The water tank 40 is provided with a water temperature sensor 47 and a water level sensor 48, so that the water temperature and the water level of the tank can be monitored.
[0018]
The electric load system 5 of the fuel cell is constituted by a lead wire connected from the fuel cell stack 1 via the relay 53 to the inverter 51 for controlling the motor 52. In this system, a secondary battery composed of a storage battery is used as a driving power source for ancillary equipment such as an air supply fan 31, a water condenser 46 fan, a water injection pump 41, a water tank 40 freezing countermeasure heater, and various solenoid valves of a fuel cell device. A battery 54 is provided, and the secondary battery 54 is connected in parallel to the fuel cell. This secondary battery 54 is used for accumulating the regenerative current of the motor 52 and for supplementing the output when the output of the fuel cell is insufficient.
[0019]
In the fuel cell system having such a configuration, the hydrogen supply electromagnetic valve 24 is closed, and hydrogen is stored in the hydrogen storage alloy by the supply of hydrogen gas from a filling path (not shown). The supply of water to the water supply system 4 is performed by opening the water supply electromagnetic valve 48 and supplying water to the water tank 40. Then, in the power generation state, the hydrogen supply solenoid valve 24 is opened to supply the hydrogen occluded in the hydrogen storage alloy under the pressure regulation by the hydrogen pressure regulating valve 23 to the fuel cell stack 1 while the air supply fan 31 is activated, An operation of sending air to the fuel cell stack 1 via the air manifold 34 is performed. In this power generation state, the direct injection water electromagnetic valve 43 is opened while operating the water direct injection pump 41 of the water supply system 4 continuously or intermittently as necessary, and water is injected from the water injection nozzle 45 into the air manifold 34. As a result, an operation of mixing water into the air supplied to the fuel cell stack 1 in a mist state is performed. This water enters the cooling space S2 from the upper opening of the cooling space S2 shown in FIG. 2 and FIG. 3 of each separator of the fuel cell stack 1 together with the air, is vaporized, passes through the air flow path S1, and becomes the air electrode of each cell. Except for those supplied to the 12 side, they are discharged to the lower part of the housing from the lower opening constituting the discharge part of the cooling space S2, and collected in the water tank 40.
[0020]
The air and the water in the water vapor state, which are sent to the fuel cell stack 1 and heated by the fuel cell stack 1 as described above, enter the storage 21 of the hydrogen storage alloy via the duct from the lower portion of the housing, and After being heated, the air is guided to a water condenser 46 through a duct, and is separated into dry air and condensed water. The dried air is discharged to the outside air through a filter, and the condensed water is passed through a pump 44 to a water tank. Return to 40. Further, the water that has passed through the fuel cell stack 1 in a liquid state returns directly to the water tank 40.
[0021]
The feature of this system is that the air flow path S1 and the cooling space S2 in the fuel cell stack 1 can be arranged in a unified distribution path, and air and water can be distributed at the same time. There is no need to provide.
[0022]
Next, a detailed configuration of the separator 10B inserted between the unit cells 10A of each unit cell 10 of the fuel cell stack 1 will be described. As shown in FIG. 4 in a disassembled state, the separator 10B includes a pair of current collectors for contacting the air electrode 12 and the fuel electrode 13 (see FIG. 2) of the unit cell 10A to take out current. 14 and 15 and frames 16 and 17 that are superimposed on them and support the unit cell 10A. In this embodiment, the current collecting members 14 and 15 are formed of a thin metal plate, for example, having a plate thickness of about 0.1 mm. The constituent metal is a metal having conductivity and corrosion resistance, for example, a metal obtained by subjecting a stainless steel, a nickel alloy, a titanium alloy, or the like to a corrosion resistance conductive treatment.
[0023]
One of the current collecting members 14 is formed of a horizontally long rectangular plate material and forms a part of a space defining member that defines the cooling space S2, and is formed by press working that partially raises the plate surface within a predetermined range. A plurality of protrusions 141 are formed by extrusion. These convex portions 141 are arranged in a continuous straight line, parallel to the longitudinal sides (short sides in the illustrated form) of the plate material, and at equal intervals, so as to completely traverse the plate surface. Is composed. At the upper end of the current collecting member 14 in the vertical direction, the peak portion of the wavy bent portion 140, that is, the valley portion sandwiched between the convex portions 141 is bent so as to be inclined in the peak direction, so that the tip portion is flush with the peak portion. An inclined portion 145 is formed to function as a lid according to the subject of the present invention. Furthermore, each convex part 141 is flattened by crushing its lower part in the thickness direction. The cross-sectional shape of the portion other than the flattened portion 141 ′ of the inclined portion 145 and the convex portion 141 is roughly shown as a rectangular wave-shaped cross section in FIG. 2 for convenience. It is more practical to make the shape slightly wider.
[0024]
Referring to FIG. 2, a groove-shaped space S1 defined between convex portions 141 and having an open side facing unit air electrode 12 of unit cell 10A allows air to flow to air electrode 12 side, as described later in detail. It is used as an air flow path for circulation. The plane of the top 142 of each convex portion 141 is a contact portion with which the air electrode 12 contacts. The groove-shaped space S2 defined on the back side of the convex portion 141 is used as a cooling space (flow path in this embodiment), which will be described later in detail. A large number of through holes 143 that penetrate the current collecting member 14 are formed so that the air flow path S1 and the cooling space S2 partially communicate with each other. The opening positions of these through holes 143 are arbitrary, but both side surfaces of the convex portion 141 are common sense. Further, long elliptical holes 144 that are long in the vertical direction are formed near both ends in the horizontal side (long side in the illustrated form) direction of the current collecting member 14. When the separator 10B is laminated by stacking the current collecting member 14 on the current collecting member 15 and the frames 16 and 17, the oblong holes 144 define the hydrogen passages L1 and L2 that align and penetrate these members. Constitute.
[0025]
Returning to FIG. 4, the other current collecting member 15 is formed of a rectangular plate that matches the current collecting member 14 so as to constitute the other of the space defining members that define the cooling space S2. Are extruded. The convex portion 151 has a flat top 152 (see FIG. 2) and a substantially rectangular cross-sectional shape similarly to the case of the above-mentioned convex portion 141. However, in this case, the convex portion 151 It is provided intermittently in the vertical direction. In other words, the protrusions 151 are arranged such that the horizontal (longer side) pitch is aligned with the pitch of the convexes 141 of the current collector 14, and the vertical (short side) pitch is set to an appropriate interval. It is a round or rectangular projection. The left half section in FIG. 2 shows a cut section at the arrangement portion of the projections 151, and the right half section shows a cut section at the arrangement portion. The vertical and horizontal spaces S3 formed between the projections 151 constitute a planar space whose side facing the fuel electrode 13 of the unit cell 10 is open, and is a hydrogen flow path through which hydrogen as fuel flows. . The plane of the top 152 of the projection 151 serves as a contact portion with which the fuel electrode 13 contacts. Further, the rear side of the convex portion 151 is a short cylindrical space S4 in which the side facing the current collecting member 14 is open, and is fitted to the space S2 of the current collecting member 14, and as a result, the cooling space S2 is interposed. Thus, a configuration is provided in which both ends are open to the long side of the plate material. Like the current collecting member 14, the current collecting member 15 also has a long oval hole 153 formed in the short side direction near both ends in the long side direction, and is overlapped with the current collecting member 14 and the frames 15 and 16. When the separators 10B are stacked together, the hydrogen passages L1 and L2 are formed to penetrate these members in alignment. In this embodiment, the convex portion 151 has a short columnar shape that intermittently abuts on the fuel electrode 13 with a small area, thereby forming a hydrogen passage S3 vertically and horizontally between the columnar convex portions 151, The purpose is to suppress stagnation and stagnation of the flow of hydrogen gas. In addition, since the contact area of the hydrogen gas with the fuel electrode 13 is increased by doing so, improvement in power generation efficiency can be expected.
[0026]
The current collecting members 14 and 15 having the above-described configuration are overlapped and fixed such that the respective convex portions 141 and 151 are both on the outside. At this time, the plate surface portion on which the convex portions 141 and 151 are not formed, that is, the back surface of the hydrogen flow path S3 and the back surface of the air flow path S1 are in contact with each other, and are in a state where they can be energized mutually. Further, by overlapping the current collecting members 14 and 15, a cooling space in which the space S2 and the space S4 are combined is formed between them. When the unit cell 10A is fitted to the current collecting member 14, the open surface side of the space S1 is closed to form a tubular air flow path, and a part of the wall surrounding the flow path is formed by the air electrode 12. Will be. Then, air and water are supplied from the air flow path S1 to the air electrode 12 of the unit cell 10A. Similarly, when the unit cell 10A is fitted to the current collecting member 15, the open surface side of the space S3 is closed to form a planar hydrogen flow path, and a part of the wall surrounding the flow path is formed by the fuel electrode 13. Will be done. Then, hydrogen is supplied from the fuel passage S3 to the fuel electrode 13 of the unit cell 10A.
[0027]
Frames 16 and 17 are respectively superposed on the current collecting members 14 and 15 having the above-described configuration. As shown in FIGS. 3 and 4, the frame 16 superposed on the current collecting member 14 has substantially the same outer shape as that of the current collecting member 14, and the vertical frame 161 on both sides is divided into upper and lower horizontal frame portions 162, 163. The lower horizontal frame portion 163 is lower than the lower side of the horizontal frame portion 163 so as not to be flush with the lower sides of the vertical frame portions 161 and the current collecting members 14 and 15 on both sides. Are slightly shifted upward so as to be positioned upward. At the center surrounded by these frames, a window 164 for accommodating the convex portion 141 of the current collecting member 14 is defined. Also, the frame body 16 is formed with oval holes 165 at positions and shapes corresponding to the oval holes 144 of the current collecting member 14 near both ends. The horizontal frame portions 162 and 163 of the frame body 16 and the vertical frame portion 161 of the portion to which they are connected are made thinner than the entire vertical frame portion 161. The horizontal frame portions 162 and 163 on the surface on which the power is collected are located at positions corresponding to the convex portion forming range of the current collecting member 14, and the surface retreated from the contact surface with the current collecting member 14 over the entire short side direction. Has formed. Therefore, when the frame 16 is overlaid on the current collecting member 14, the convex portion 141 of the current collecting member 14 contacts the air electrode 12 of the unit cell 10 </ b> A in the window 164 and faces the horizontal frame portions 162 and 163. In the part that does, it has a relationship that abuts them. Thus, between the current collecting member 14 and the frame 16, the convex portion 141 of the current collecting member 14 and the inner surface of the horizontal frame portion 162 are located at the upper part, and the convex portion 141 of the current collecting member 14 is located at the window 164. As a large number of tubular spaces surrounded by the convex portion 141 of the current collecting member 14 and the inner surface of the horizontal frame portion 163 at the lower portion of the air electrode 12 surface of 10A, the upper end extends to the inner surface of the horizontal frame portion 162 at the tip of the lid portion 145. An air flow path S1 which is closed by the contact and has a lower end opened between the horizontal frame portion 163 and the current collecting member 14 and extending in the vertical direction is defined.
[0028]
The frame 17 superimposed on the current collecting member 15 is formed in a frame shape having a smaller vertical dimension than the frame 16, and in this case, an opening larger than the window 171 is formed in the main body 170 in the lateral direction. The height of this opening defines the height of the window 171, and the width of the opening is set to a width that matches the width between the outer ends of the oblong holes 153 at both ends of the current collecting member 15. A pair of vertical frame portions 172 are provided near both ends of the opening in the width direction. The width between the vertical frame portions 172 defines the width of the window 171, and the width defined by the vertical frame portions 172 and the width of the opening of the main body portion 170 is an oblong hole at both ends of the current collecting member 15. An elongated hole 173 having a size matching the width of the elongated hole 153 and substantially matching the position and shape of the elongated hole 153 is formed. The vertical frame portion 172 is made thinner than the main body portion 170. Due to the relationship between the thicknesses, the vertical frame portion 172 is provided at the position where the vertical frame portion 172 is provided on the surface on which the current collecting member 15 is overlapped. A surface that is recessed from the contact surface by an amount corresponding to the height of the portion 151 is formed. Therefore, when the frame 17 is superimposed on the current collecting member 15, the projection 151 of the current collecting member 15 contacts the vertical frame 172 in the vertical frame 172, and the fuel electrode of the unit cell 10 </ b> A in the window 171. 13 comes into contact. In the portion sandwiched between the long holes 173 in this manner, a planar hydrogen flow path S3 that is uniformly formed so as to cover the projection 151 is formed.
[0029]
Further, a detailed configuration not shown in the drawings will be described. Preferably, the cross-sectional area of the flow path forming the cooling space S2 is set to gradually decrease from the upper side to the lower side. With such a configuration, the pressure loss of the air flowing from the cooling space S1 to the air flow path S2 can be reduced. Such a flow path configuration can be realized by appropriately setting the height and / or width of the convex portion 141 of the current collecting member 14.
[0030]
In addition, hydrophilic processing is performed on the inner wall surfaces of the air passage S1 and the cooling space S2 as necessary. Specifically, this treatment is performed such that the contact angle between the inner wall surface and water is 40 ° or less, preferably 30 ° or less. As a treatment method, a method of applying a hydrophilic treatment agent to the surface is employed. Examples of the treatment agent to be applied include polyacrylamide, polyurethane resin, titanium oxide (TiO2), and the like. As another hydrophilic treatment, a treatment for roughening the roughness of the metal surface may be mentioned. For example, plasma processing is an example. The hydrophilic treatment is preferably performed on a portion where the temperature is highest. For example, the cooling space inner wall surface F1 on the back side of the top 142 of the protrusion 141 in contact with the unit cell 10A, and the air flow path on the front side of the protrusion 141 It is desirable that the processing is preferentially performed in the order of the side wall surface F2, the back side cooling space side wall surface F3, and the air flow path bottom surface F4. Further, the inner wall surface F5 of the projection 151 constituting a part of the cooling space S2 may be subjected to a hydrophilic treatment. By performing the hydrophilic treatment, wetting of the inner wall surface is promoted, and the effect of the latent heat cooling of water is improved.
[0031]
The separators 10B are configured by holding the current collecting members 14 and 15 by the frames 16 and 17 configured as described above, and the fuel cell stack 1 is configured by alternately stacking the separators 10B and the unit cells 10A. . On the upper surface of the fuel cell stack 1 thus stacked, openings of a large number of cooling spaces S2 are arranged side by side at intervals as shown in FIG. Air and water intakes are formed with openings of the same arrangement in the stacking direction at intervals corresponding to the thickness. On the lower surface of the fuel cell stack 1, as shown in FIG. 6, openings at the lower ends of the flow path constrictions S 2 ′ of the cooling space S 2 are provided in the discharge section of the rectangular air flow path in the lateral direction at intervals. At the same time, a water discharge section having openings of the same arrangement arranged in the stacking direction is formed at intervals corresponding to the thickness of the horizontal frame portion 163 of the frame 17 and the frame 16.
[0032]
The configuration according to the subject of the present invention in each unit cell of the fuel cell having the above configuration can be summarized by referring to the longitudinal section of the separator shown in FIG. 3 and the upper surface of the separator shown in FIG. The side end is closed to the supply of air and water by the separator 10B. Since the separator 10B includes the current collecting members 14 and 15 as space defining members that define the cooling space S2, the inlet-side end of the air flow path S1 is closed by the current collecting member 14. The current collecting members 14 and 15 of the separator 10B are formed by bringing a pair of plate members made of a press-formed product of a conductive metal plate material into contact with each other in the plate surface direction, and a cooling space S2 is formed between both plate members. At the same time, the one end of the plate-shaped member, that is, the end of the current collecting member 14 is bent to close the inlet end of the air flow path S1. The current collecting member 14 has a wavy bent portion 140 formed by bending to protrude the plate surface and extending through the plate member, and a valley portion sandwiched between the peaks of the wavy bent portion 140 at a vertical end. Has an inclined portion 145 formed by bending to incline in the direction of the hill, and the tip thereof is flush with the hill, and cooperates with the other plate-like member 15 to form a cooling space S2 inside the wavy bent portion 140. And the inclined end 145 closes the inlet end of the air flow path S1.
[0033]
The fuel cell stack having such a configuration operates as schematically shown in FIG. 7 by supplying air, water, and hydrogen to each unit cell. In this case, since the air and water are uniformly supplied from the upper surface of the stack, the opening of the air flow path S1 is provided with a current collecting member 14 so that water does not directly enter the air flow path S1. It is closed by an upper slope 145. As shown in the drawing, the air and water supplied to the cooling space S2 enter the upper portion of the cooling space in a state where water droplets are mixed in a mist state in the air flow (hereinafter, this state is referred to as a mixed flow). In the steady operation state of the fuel cell, the mixed flow in the cooling space S2 is heated because the unit cell 10A generates heat by the reaction. The water droplets in the mixed flow adhere to the wall surface of the cooling space S2 by the hydrophilic treatment, and evaporate by heating to generate a latent heat cooling effect of removing heat from the wall surface. The water that has thus become steam enters the air flow path S1 together with the air whose flow is indicated by the outline arrow in the figure as shown by the shaded arrow in the figure, as shown by the shaded arrow in the figure, and flows to the air electrode 12 side of the unit cell 10A. It adheres and wets the cathode 12. Excess air and steam entering the air flow path S1 are discharged from the lower opening of the air flow path S1 below the fuel cell stack.
[0034]
On the other hand, the air and water that have not entered the air flow path S1 are discharged from the lower opening of the cooling space S2 below the fuel cell stack as it is, but due to the action of the flow path narrowing portion S2 ′. The water in the liquid state flowing down the wall reaches the channel narrowing portion S2 'and stays there, causing a phenomenon of blocking the channel by capillary action, and this water causes direct discharge of air from the cooling space S2. It acts to hinder. Therefore, substantially all of the air supplied to the cooling space S2 is sent into the air passage S1, and then discharged from the fuel cell stack via the air passage S1. In addition, the liquid water that fulfills the function of plugging air is drained sequentially by the lowermost water staying in the channel narrowing portion S2 'being pushed by the upper water and dropping as water droplets.
[0035]
On the other hand, the supply of hydrogen to the fuel flow path S3 is performed by using one of the hydrogen flow paths L1 and L2 (see FIG. 2) penetrating both sides of each unit cell 10 in their stacking direction. It is performed from the fuel flow path S3 connected to it through the space between them. Thus, hydrogen is supplied to the fuel electrode 13 of the unit cell 10A. On the fuel electrode 13 side, surplus hydrogen that has entered the fuel flow path S3 is discharged to the opposite hydrogen flow path, and is discharged or recovered by a system pipe connected to the hydrogen flow path.
[0036]
As described in detail above, according to this embodiment, since the inlet end of the air flow passage S1 is closed by the lid 145 integrally formed on the end of the separator 10B, the inlet end of each air flow passage S1 is closed. This leads to an increase in the number of manufacturing steps for filling the end portion, an increase in the number of components, and an increase in the number of components, such as adding a complicated lid member to the separator 10B to close the inlet end of the cut air flow path S1. Without closing, the inlet end of the air flow path S1 can be closed with a simple configuration. Thus, supply of air and water vapor to the air flow path S1 via the cooling space S2 is realized, and blockage of the air flow path S1 by water, such as when air and water are directly supplied to the air flow path S1. Eliminate concerns.
[0037]
In addition, since the end of the space defining member 14 that defines the cooling space S2 is the lid 145, the air flow can be prevented without affecting other members such as the frames 16 and 17 that constitute the separator 10B. The entrance end of the road S1 can be closed. Further, since the lid portion 145 is formed by bending the plate-shaped member 14, it is possible to perform the processing simultaneously with the processing of forming the cooling space S2 in the space defining member 14 made of a metal material constituting the separator 10B. An increase in man-hours can be prevented. In addition, since the both ends of the plate-like member 14 constituting the space defining member have the lid 145 formed by bending and the flow path narrowing portion S2 ', the plate material is used when the space defining member is pressed. Can be balanced at both ends, thereby preventing warpage in the plate surface of the plate material, that is, a phenomenon in which one side of the plate material shrinks and deforms into a fan shape, thereby improving the press working accuracy. In addition, since the lid 145 is formed as an inclined portion, the cooling space S2 and the wavy bent portion 140 that defines the air flow path S1 are smoothly connected to each other. Shape.
[0038]
As described above, the embodiments have been exemplified for the understanding of the present invention. However, the present invention is not limited to the illustrated embodiments, and various specific configurations may be adopted within the scope of the claims. It can be implemented with modification.
[0039]
【The invention's effect】
According to the first aspect of the present invention, since the inlet end of the air flow path is closed by the lid integrally formed with the end of the separator, the inlet end of each air flow path is closed. It can be easily performed without increasing the number of manufacturing processes such as padding, adding a complicated lid member to the separator to close the inlet end of the cut air flow path, and complicating the structure and increasing the number of parts. With such a configuration, the inlet end of the air flow path can be closed. This achieves the supply of air and water vapor to the air flow path through the cooling space, and eliminates the possibility that the air flow path is blocked by water as in the case of directly supplying air and water to the air flow path. Can be.
[0040]
According to the second aspect of the present invention, the other end of the space defining member that defines the cooling space is a lid at the inlet end of the air flow path, thereby forming another member constituting the separator. The inlet end of the air flow path can be closed without affecting the air flow.
[0041]
Furthermore, according to the third aspect of the present invention, since the lid at the end on the inlet side of the air flow path is formed by bending a plate-shaped member, the space defining member made of a metal material constituting the separator can be used. The processing can be performed simultaneously with the processing for forming the cooling space, and an increase in the number of processing steps can be prevented.
[0042]
According to the configuration of the fourth aspect, the space defining member has the lid portion formed by bending and the flow path constriction portion at both ends of the plate-like member constituting the space defining member. The stress applied to the plate at the time of pressing can be balanced at both ends. As a result, it is possible to prevent a warpage in the plate surface of the plate material, that is, a phenomenon in which one side of the plate material shrinks and deforms into a fan shape, and press working accuracy is improved.
[0043]
Further, according to the configuration of the fifth aspect, the lid of the plate-shaped member has an inclined portion, so that the lid has a shape that is smoothly connected to the wavy bent portion that defines the cooling space and the air flow path. Therefore, the plate member can be formed into a shape excellent in press workability.
[Brief description of the drawings]
FIG. 1 is a configuration diagram of a fuel cell system according to an application of the present invention.
FIG. 2 is a partial cross-sectional view of a unit cell according to an embodiment of the present invention.
FIG. 3 is a partial longitudinal sectional view of the unit cell of the embodiment.
FIG. 4 is an exploded perspective view of a separator constituting the unit cell of the embodiment.
FIG. 5 is a partial top view of the unit cell according to the embodiment.
FIG. 6 is a partial bottom view of the unit cell according to the embodiment.
FIG. 7 is a schematic diagram illustrating a mechanism of cooling and draining by the separator of the embodiment.
[Explanation of symbols]
10A Unit cell 10B Separator 12 Air electrode 14, 15 Conductive member (space defining member, plate member)
140 Wavy bent part 143 Communication hole 145 Inclined part (lid)
S1 Air flow path S2 Cooling space (cooling means)
S2 'Channel narrowing part

Claims (5)

互いに隣接する単位セルの間にセパレータが配置される燃料電池において、
前記セパレータは、単位セルの少なくとも空気極に接する表面側に設けられた空気流路と、背面側に設けられて空気と水とを供給される冷却空間とからなり、該冷却空間に伝わる単位セルの熱により蒸発する水の潜熱により単位セルを冷却する冷却手段を備え、
前記冷却空間は、セパレータに形成した連通孔を介して空気流路に連通され、該空気流路の入口側端部は、セパレータの端部に一体形成した蓋部により空気と水の供給に対して閉鎖されていることを特徴とする燃料電池。
In a fuel cell in which a separator is arranged between adjacent unit cells,
The separator includes an air flow path provided on at least a surface side of the unit cell in contact with the air electrode, and a cooling space provided on the back side and supplied with air and water, and the unit cell transmitted to the cooling space. Cooling means for cooling the unit cells by latent heat of water evaporated by heat of
The cooling space is communicated with the air flow path through a communication hole formed in the separator, and the inlet end of the air flow path is provided with a lid integrally formed at the end of the separator to supply air and water. A fuel cell characterized by being closed.
前記セパレータは、冷却空間を画成する空間画成部材を備え、前記蓋部は、空間画成部材の端部に形成された、請求項1記載の燃料電池。The fuel cell according to claim 1, wherein the separator includes a space defining member that defines a cooling space, and the lid is formed at an end of the space defining member. 前記セパレータの空間画成部材は、導電性金属板材料のプレス成形品からなる一対の板状部材を板面方向に互いに当接させてなり、両板状部材の間に冷却空間を画成するとともに、一方の板状部材の端部の屈曲により蓋部を構成する、請求項2記載の燃料電池。The space defining member of the separator is formed by bringing a pair of plate members made of a press-formed product of a conductive metal plate material into contact with each other in a plate surface direction, and defines a cooling space between both plate members. 3. The fuel cell according to claim 2, wherein the lid is formed by bending an end of one of the plate members. 前記セパレータの空間画成部材は、一方の板状部材の他端部の屈曲により形成された流路狭窄部を有する、請求項3記載の燃料電池。4. The fuel cell according to claim 3, wherein the space defining member of the separator has a flow path constriction formed by bending the other end of one of the plate members. 5. 前記一方の板状部材は、その板面を隆起させる屈曲により形成されて板状部材を縦断して延びる波状屈曲部と、縦方向の端部で波状屈曲部の山部間に挟まれる谷部を山部方向に傾斜させる屈曲により形成されて先端を山部と面一にされた傾斜部を有し、
他方の板状部材と協働して波状屈曲部の内側に冷却空間を画成するとともに、傾斜部を蓋部として空気流路の入口側端部を閉鎖する、請求項3又は4記載の燃料電池。
The one plate-shaped member has a wavy bent portion formed by bending to protrude the plate surface and extending by traversing the plate-shaped member, and a valley portion sandwiched between ridges of the wavy bent portion at a longitudinal end. Has an inclined portion formed by bending to incline in the direction of the mountain portion, and the tip is flush with the mountain portion,
The fuel according to claim 3 or 4, wherein a cooling space is defined inside the wavy bent portion in cooperation with the other plate-shaped member, and the inlet side end of the air flow path is closed with the inclined portion as a lid. battery.
JP2002278171A 2002-09-24 2002-09-24 Fuel cell Expired - Fee Related JP4221985B2 (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007265799A (en) * 2006-03-28 2007-10-11 Toyota Motor Corp Separator and fuel cell stack
JP2008084702A (en) * 2006-09-28 2008-04-10 Hitachi Ltd Fuel cell separator
WO2014132707A1 (en) * 2013-02-28 2014-09-04 トヨタ車体 株式会社 Gas flow channel forming body for fuel cell, and fuel cell
JP2015521353A (en) * 2012-05-28 2015-07-27 インテリジェント エナジー リミテッドIntelligent Energy Limited Bipolar plate for fuel cell
US9806361B2 (en) 2012-05-28 2017-10-31 Intelligent Energy Limited Fuel cell plate assemblies
JP7148010B1 (en) 2022-05-02 2022-10-05 トヨタ自動車株式会社 water electrolysis stack

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007265799A (en) * 2006-03-28 2007-10-11 Toyota Motor Corp Separator and fuel cell stack
JP2008084702A (en) * 2006-09-28 2008-04-10 Hitachi Ltd Fuel cell separator
JP2015521353A (en) * 2012-05-28 2015-07-27 インテリジェント エナジー リミテッドIntelligent Energy Limited Bipolar plate for fuel cell
US9806361B2 (en) 2012-05-28 2017-10-31 Intelligent Energy Limited Fuel cell plate assemblies
WO2014132707A1 (en) * 2013-02-28 2014-09-04 トヨタ車体 株式会社 Gas flow channel forming body for fuel cell, and fuel cell
US9917310B2 (en) 2013-02-28 2018-03-13 Toyota Shatai Kabushiki Kaisha Gas flow channel forming body for fuel cell, and fuel cell
JP7148010B1 (en) 2022-05-02 2022-10-05 トヨタ自動車株式会社 water electrolysis stack
JP2023165110A (en) * 2022-05-02 2023-11-15 トヨタ自動車株式会社 water electrolysis stack

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