JPH0997619A - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPH0997619A JPH0997619A JP7252746A JP25274695A JPH0997619A JP H0997619 A JPH0997619 A JP H0997619A JP 7252746 A JP7252746 A JP 7252746A JP 25274695 A JP25274695 A JP 25274695A JP H0997619 A JPH0997619 A JP H0997619A
- Authority
- JP
- Japan
- Prior art keywords
- gasket
- fuel cell
- cell
- exchange membrane
- separator plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Fuel Cell (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、燃料として純水素、ま
たはメタノール及び化石燃料からの改質水素などの還元
剤を用い、空気や酸素を酸化剤とする燃料電池に関する
ものであり、特に固体高分子電解質型燃料電池のガスケ
ットに関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fuel cell using pure hydrogen as a fuel or a reducing agent such as reformed hydrogen from methanol and fossil fuel and using air or oxygen as an oxidant, and particularly to a solid-state fuel cell. The present invention relates to a gasket for a polymer electrolyte fuel cell.
【0002】[0002]
【従来の技術】例えば固体高分子電解質型燃料電池は、
固体高分子電解質にプロトン伝導体であるカチオン交換
膜を用い、燃料として水素を、酸化剤として酸素を導入
した場合には、次の(化1)、(化2)反応が起こるこ
とが知られている。2. Description of the Related Art For example, a solid polymer electrolyte fuel cell is
It is known that when a cation exchange membrane which is a proton conductor is used as a solid polymer electrolyte and hydrogen is introduced as a fuel and oxygen is introduced as an oxidant, the following (formula 1) and (formula 2) reactions occur. ing.
【0003】[0003]
【化1】 Embedded image
【0004】[0004]
【化2】 Embedded image
【0005】負極では水素がプロトンと電子に解離す
る。プロトンはカチオン交換膜中を正極に向かって移動
し、電子は導電性のセパレータ板と直列に積層されたセ
ルとさらに外部の回路を移動して正極に至り、このとき
発電が行われる。一方、正極ではカチオン交換膜中を移
動してきたプロトンと外部回路を移動してきた電子と外
部から導入された酸素とが反応し水を生成する。この反
応は発熱を伴うので全体として水素と酸素から電気と水
と熱を発生する。At the negative electrode, hydrogen dissociates into protons and electrons. Protons move in the cation exchange membrane toward the positive electrode, and electrons move in a cell laminated in series with a conductive separator plate and an external circuit to reach the positive electrode, at which time power is generated. On the other hand, in the positive electrode, the protons that have moved in the cation exchange membrane, the electrons that have moved in the external circuit, and oxygen introduced from the outside react to generate water. Since this reaction is exothermic, hydrogen, oxygen, and electricity generate electricity, water, and heat as a whole.
【0006】固体高分子電解質型燃料電池が他の燃料電
池と大きく異なる点は、電解質が固体高分子であるイオ
ン交換膜で構成されている点である。このイオン交換膜
にはパーフルオロカーボンスルホン酸膜(米国、デュポ
ン社製 商品名ナフィオン)等が用いられるが、この膜
が十分なプロトン導電性を示すためには膜が十分に水和
している必要がある。イオン交換膜を水和させる方法と
しては、例えばJ.Electorochem.So
c.135(1988)2209頁に記載されているよ
うに反応ガスを加湿器に通すことによって水蒸気をセル
内に導入してイオン交換膜の乾燥を防ぐ方法が取られ
る。また、各セルをシールする方法としては、例えば
J.Power Sources,29(1990)3
67頁に記載されているようにイオン交換膜の面積を電
極面積よりも大きくし、イオン交換膜の電極と接合され
ていない周囲部分を上下のガスケットで挟み込む方法が
取られる。The solid polymer electrolyte fuel cell is greatly different from other fuel cells in that the electrolyte is composed of an ion exchange membrane which is a solid polymer. A perfluorocarbon sulfonic acid membrane (Nafion, trade name, manufactured by DuPont, USA) is used for this ion exchange membrane, but the membrane must be sufficiently hydrated in order for this membrane to exhibit sufficient proton conductivity. There is. As a method for hydrating the ion exchange membrane, for example, J. Electrochem. So
c. 135 (1988) page 2209, a method is adopted in which the reaction gas is passed through a humidifier to introduce water vapor into the cell to prevent the ion exchange membrane from drying. As a method of sealing each cell, for example, J. Power Sources, 29 (1990) 3
As described on page 67, the area of the ion exchange membrane is made larger than the electrode area, and the peripheral portion of the ion exchange membrane which is not joined to the electrodes is sandwiched by upper and lower gaskets.
【0007】ガスケットの材質としてはポリテトラフル
オロエチレン(米国,デュポン社製商品名テフロン)を
コーティングしたガラス繊維布やフッ素ゴムが用いられ
ている。As a material for the gasket, a glass fiber cloth or fluororubber coated with polytetrafluoroethylene (trade name: Teflon manufactured by DuPont, USA) is used.
【0008】また、米国特許第4,826,741号明
細書ではシリコンゴムやフッ素ゴムが用いられている。
この構成時、ガスケットは約50〜200μmのイオン
交換膜の厚みを吸収しつつ隣合うセパレータ板間の絶縁
とガスシールを行わなければならない。そこで、セルの
締めつけ圧力を大きくしてガスケットをつぶしたり、ガ
スケットのイオン交換膜が当たる部分の厚みを膜厚分だ
け薄くする微細な加工が必要であった。In US Pat. No. 4,826,741, silicone rubber and fluororubber are used.
In this structure, the gasket must absorb the thickness of the ion exchange membrane of about 50 to 200 μm and perform insulation and gas sealing between the adjacent separator plates. Therefore, it is necessary to perform fine processing by increasing the cell clamping pressure to crush the gasket, or to reduce the thickness of the portion of the gasket that contacts the ion exchange membrane by the thickness of the membrane.
【0009】[0009]
【発明が解決しようとする課題】しかしながら上記従来
の方法では、セルの積層数が増すにつれて吸収すべきイ
オン交換膜の厚みが積算されて大きくなるために吸収し
きれなくなったり、非常に大きな締めつけ圧力を必要と
し、強度を確保するためにエンドプレートやボルトナッ
トなどの他のハウジングが大がかりなものになる。ま
た、ガスケットやイオン交換膜やセパレータ板の厚みの
ばらつきによって十分なガスシール性が確保できないな
どの欠点を有していた。さらに、イオン交換膜は含水率
の変化にともなって膜厚が変化するため、従来のガスケ
ット材料では応力緩和性が大きいことから、当初確保さ
れていたシール性が運転途中で低下するという危険を有
していた。However, in the above-mentioned conventional method, as the number of laminated cells increases, the thickness of the ion-exchange membrane to be absorbed is integrated and becomes large, so that the absorption cannot be completed or a very large tightening pressure is applied. And other housings such as end plates and bolts and nuts become large in order to secure strength. In addition, there is a drawback that sufficient gas sealability cannot be secured due to variations in the thickness of the gasket, the ion exchange membrane, and the separator plate. Furthermore, since the thickness of the ion exchange membrane changes with the change of the water content, the conventional gasket material has a large stress relaxation property, so there is a risk that the initially secured sealing property will deteriorate during operation. Was.
【0010】本発明は上記従来の課題を解決するもの
で、低い締めつけ圧力で高いシール性を発揮するガスケ
ットを用いることによって、より軽く経済性の高い燃料
電池、特に固体高分子電解質型燃料電池を提供すること
を目的とする。The present invention solves the above-mentioned problems of the prior art. By using a gasket that exhibits a high sealing property at a low tightening pressure, a lighter and more economical fuel cell, particularly a solid polymer electrolyte fuel cell, is provided. The purpose is to provide.
【0011】[0011]
【課題を解決するための手段】この目的を達成するため
に、本発明によれば、正極、電解質板、負極からなる単
位セルの周縁にガスケットを配し、セパレータ板を介在
して積層された燃料電池において、ガスケットをセパレ
ータ板の少なくとも片面に独立気泡のスポンジ層を接着
層を介して接着した構成としたものである。In order to achieve this object, according to the present invention, a gasket is placed around the periphery of a unit cell composed of a positive electrode, an electrolyte plate and a negative electrode, and a separator plate is interposed between the gaskets. In a fuel cell, a gasket has a structure in which a sponge layer of closed cells is adhered to at least one surface of a separator plate via an adhesive layer.
【0012】[0012]
【作用】この構成では、独立気泡のスポンジ層がイオン
交換膜の厚みを気泡の圧縮によって吸収する。また、部
分的な凹凸に対しても個々の独立した気泡が圧縮するた
めにセパレータ板のウネリや粗さも吸収することができ
る。さらに、密閉された気泡を圧縮させるので応力緩和
が小さく、スポンジ層がセパレータ板に接着されている
ために、内部に高圧のガスを用いた場合にもスポンジ層
と基板との接着力によってスポンジ層が外側に逃げるこ
とはない。In this structure, the closed-cell sponge layer absorbs the thickness of the ion exchange membrane by compressing the bubbles. In addition, since individual independent air bubbles are compressed against partial unevenness, the swell and roughness of the separator plate can be absorbed. Furthermore, since the closed air bubbles are compressed, stress relaxation is small, and since the sponge layer is adhered to the separator plate, the sponge layer is adhered to the substrate even when high-pressure gas is used inside. Does not escape to the outside.
【0013】[0013]
【実施例】以下、本発明の実施例について、図面を参照
しながら説明する。Embodiments of the present invention will be described below with reference to the drawings.
【0014】図3は、一般的な固体高分子電解質型燃料
電池の積層電池の外観図である。グラッシーカーボンな
どの導電性の素材からなるセパレータ板2と絶縁性のガ
スケット1が交互に積み重ねられ、最外側のセパレータ
板に銅製の集電板3が密着されている。この積層体を絶
縁板4を介してステンレス製のエンドプレート5ではさ
み、エンドプレート間をボルト、ナットで締めつける構
造となっている。FIG. 3 is an external view of a laminated cell of a general solid polymer electrolyte fuel cell. Separator plates 2 made of a conductive material such as glassy carbon and insulating gaskets 1 are alternately stacked, and a copper current collector plate 3 is adhered to the outermost separator plate. This laminated body is sandwiched by stainless steel end plates 5 with an insulating plate 4 interposed therebetween, and the end plates are fastened with bolts and nuts.
【0015】もちろん各パーツの材質は導電性、絶縁
性、耐熱性、ガス透過性などの条件が電池性能に悪影響
をおよぼさなければ、上記の素材に限定されるものでは
ない。Of course, the material of each part is not limited to the above materials as long as the conditions such as conductivity, insulation, heat resistance and gas permeability do not adversely affect the battery performance.
【0016】図4は一般的な積層電池内部セルの断面図
を示した図である。中央のイオン交換膜11の両面に電
極12が接合され、その接合体の上下に溝付きのセパレ
ータ板2が位置している。イオン交換膜の面積は電極1
2よりも大きくなっており、周囲をガスケットではさみ
込み、各セルのシールとセパレータ板どうし間の絶縁を
行っている。図に示したように必要に応じて積層体の内
部にガス通路13を設置する場合(内部マニホールド
型)には、ガスケットがこのガス通路のシールも行う。
溝付きのセパレータ板2は溝の部分に多孔質状の溝付き
板をはめ込む場合やメッシュなどを用いるなどの様々な
構造が可能であり、この構造が本発明を限定するもので
はない。FIG. 4 is a view showing a cross-sectional view of a general laminated battery internal cell. Electrodes 12 are bonded to both surfaces of the central ion exchange membrane 11, and grooved separator plates 2 are located above and below the bonded body. The area of the ion exchange membrane is electrode 1
It is larger than 2, and the periphery is sandwiched by gaskets to insulate between the seals of each cell and the separator plates. As shown in the figure, when the gas passage 13 is installed inside the laminate (internal manifold type) as required, the gasket also seals the gas passage.
The grooved separator plate 2 can have various structures such as a case where a porous grooved plate is fitted in the groove portion or a mesh is used, and this structure does not limit the present invention.
【0017】(実施例1)図1は本発明の実施例1のセ
ルの断面を示す。図中ガスケット21は、セパレータ板
の片面に厚み0.7mmのエチレン−プロピレンゴム
(EPDM)の独立気泡のスポンジ層23を接着層22
を介して接着したものである。本発明のガスケット21
は、イオン交換膜11に接する部分の独立した気泡が、
セパレータ板2どうしに挟まれた部分よりもさらに圧縮
されることによってイオン交換膜11の厚みを吸収しつ
つセパレータ板間、イオン交換膜とセパレータ間の両方
のシールを行うことができた。締めつけ圧力は従来の気
泡のないフッ素ゴムを用いた場合がシール圧10kg/
cm2を必要としたのに対して、本発明のガスケットの
場合には3.5kg/cm2以上で十分であった。さら
に、スポンジ層だけのシートでは非常に柔らかいために
セル及びガス通路の内圧が高圧になるとガスケットが外
側にずれて吹き切れてしまったのに対して、本発明のガ
スケットの場合には、接着層の接着力によってスポンジ
層のズレが防止されて吹き切れを起こさなかった。(Embodiment 1) FIG. 1 shows a cross section of a cell according to Embodiment 1 of the present invention. In the figure, the gasket 21 has a 0.7 mm-thick ethylene-propylene rubber (EPDM) sponge layer 23 of closed cells on one surface of the separator plate and an adhesive layer 22.
It is bonded through. Gasket 21 of the present invention
Is an independent bubble in the portion in contact with the ion exchange membrane 11,
It was possible to seal between the separator plates and between the ion exchange membrane and the separator while absorbing the thickness of the ion exchange membrane 11 by being compressed more than the portion sandwiched between the separator plates 2. The tightening pressure is 10 kg / when using the conventional bubble-free fluororubber.
Whereas cm 2 was required, in the case of the gasket of the present invention, 3.5 kg / cm 2 or more was sufficient. Further, since the sheet having only the sponge layer is very soft, when the internal pressure of the cells and the gas passages became high, the gasket was displaced to the outside and blown out, whereas in the case of the gasket of the present invention, the adhesive layer was used. The sponge layer was prevented from being displaced due to the adhesive force of and no blowout occurred.
【0018】(実施例2)図2は本発明の実施例2のセ
ルの断面を示す。ガスケット31は、厚み0.5mmの
アクリル板32の片面に厚み0.4mmのEPDMの独
立気泡のスポンジ層33を接着し、アクリル板32をセ
パレータ板2に接着層34を介して接着したものであ
る。実施例1と同様のシール効果に加えて、ガスケット
が心材を有するためにたわまず、セパレータ板に容易に
接着することができ、接着時の位置ずれを生じなかっ
た。(Embodiment 2) FIG. 2 shows a cross section of a cell of Embodiment 2 of the present invention. The gasket 31 is formed by adhering a 0.4 mm-thick EPDM closed-cell sponge layer 33 to one surface of an acrylic plate 32 having a thickness of 0.5 mm, and adhering the acrylic plate 32 to the separator plate 2 via an adhesive layer 34. is there. In addition to the sealing effect similar to that of Example 1, the gasket has the core material, so that it can be easily adhered to the separator plate without sagging, and no displacement occurred during adhesion.
【0019】なお、本実施例ではガスケットの材料とし
て前記の材質を用いたが、この固体高分子電解質型燃料
電池は作動温度が150℃以下であるので、フッ素ゴム
など種々の弾性材料が使用できる。ただし、イオン交換
膜がその交換基としてスルホン酸基をもち酸性を示し、
また水が生成し反応ガスが加湿されるために、ガスケッ
トの接触面は耐酸性、耐水蒸気性、耐熱水性等が必要で
ある。In this embodiment, the above-mentioned material was used as the material of the gasket, but since this solid polymer electrolyte fuel cell has an operating temperature of 150 ° C. or lower, various elastic materials such as fluororubber can be used. . However, the ion exchange membrane has a sulfonic acid group as its exchange group and exhibits acidity,
Further, since water is generated and the reaction gas is humidified, the contact surface of the gasket is required to have acid resistance, water vapor resistance, hot water resistance and the like.
【0020】以上の耐熱性、耐酸性、耐水蒸気性、耐熱
水性等の条件が満たされればどのような材質を選択する
ことも可能であり、本発明は実施例の材料に限定されな
い。Any material can be selected as long as the above-mentioned conditions such as heat resistance, acid resistance, steam resistance, and hot water resistance are satisfied, and the present invention is not limited to the materials of the examples.
【0021】さらに、本実施例ではガスケットを1枚使
用してイオン交換膜を一方向からシールする方法を示し
たが、ガスケットを2枚使用してイオン交換膜を挟み込
む方法を使っても同様の効果が得られた。また、上記の
実施例では固体高分子電解質型燃料電池を一例として述
べたが、リン酸型燃料電池、アルカリ型燃料電池等にお
いても同様の効果を示した。Further, in the present embodiment, the method of sealing the ion exchange membrane from one direction by using one gasket was shown, but the same method can be achieved by using the method of sandwiching the ion exchange membrane by using two gaskets. The effect was obtained. Further, although the solid polymer electrolyte fuel cell has been described as an example in the above-mentioned embodiment, the same effect is exhibited also in the phosphoric acid fuel cell, the alkaline fuel cell and the like.
【0022】[0022]
【発明の効果】以上のように本発明は、燃料電池におい
て、ガスケットはセパレータ板の少なくとも片面に独立
気泡のスポンジ層を接着した構成とした。これにより、
独立気泡のスポンジ層がイオン交換膜の厚みやセパレー
タ板の凹凸を気泡の圧縮によって吸収するので、小さな
締めつけ圧力で優れたシール性能を実現できる。また、
独立気泡のスポンジ層がセパレータ板に接着層を介して
接着されているために、内部に高圧のガスを用いた場合
にも接着力によってスポンジ層が外側に逃げない。As described above, according to the present invention, in the fuel cell, the gasket has a structure in which a sponge layer of closed cells is adhered to at least one surface of the separator plate. This allows
Since the sponge layer of closed cells absorbs the thickness of the ion exchange membrane and the unevenness of the separator plate by compressing the bubbles, excellent sealing performance can be realized with a small tightening pressure. Also,
Since the sponge layer of closed cells is adhered to the separator plate via the adhesive layer, the sponge layer does not escape to the outside due to the adhesive force even when high-pressure gas is used inside.
【0023】以上の効果により、締めつけ圧力の大幅な
低減が実現できるためエンドプレート、セパレータ、電
極などの強度を低減することができ、例えばエンドプレ
ートとして従来ステンレス鋼を使用していたものに代え
てエンジニアプラスチックなどの材料を使用することが
可能となり、小型軽量で経済性の高い燃料電池が実現で
きる。Due to the above effects, the tightening pressure can be greatly reduced, so that the strength of the end plate, the separator, the electrode, etc. can be reduced. For example, instead of the end plate conventionally made of stainless steel, It is possible to use materials such as engineered plastics, and it is possible to realize a fuel cell that is small, lightweight, and highly economical.
【図1】本発明の実施例1におけるセルの断面図FIG. 1 is a sectional view of a cell according to a first embodiment of the present invention.
【図2】本発明の実施例2におけるセルの断面図FIG. 2 is a sectional view of a cell according to a second embodiment of the present invention.
【図3】一般的な固体高分子電解質型燃料電池の外観図FIG. 3 is an external view of a general solid polymer electrolyte fuel cell
【図4】一般的なセルの断面図FIG. 4 is a sectional view of a general cell.
1 ガスケット 2 セパレータ板 3 集電板 4 絶縁板 5 エンドプレート 6 水素入口 7 水素出口 8 酸素入口 9 酸素出口 10 排水ドレン 11 イオン交換膜 12 電極 13 ガス通路 21 実施例1のガスケット 22 接着層 23 スポンジ層 31 実施例2のガスケット 32 アクリル板 33 スポンジ層 34 接着層 1 Gasket 2 Separator Plate 3 Current Collector Plate 4 Insulating Plate 5 End Plate 6 Hydrogen Inlet 7 Hydrogen Outlet 8 Oxygen Inlet 9 Oxygen Outlet 10 Drain Drain 11 Ion Exchange Membrane 12 Electrode 13 Gas Passage 21 Gasket 22 of Example 1 22 Adhesive Layer 23 Sponge Layer 31 Gasket of Example 2 32 Acrylic plate 33 Sponge layer 34 Adhesive layer
フロントページの続き (72)発明者 江田 信夫 大阪府門真市大字門真1006番地 松下電器 産業株式会社内Front page continuation (72) Inventor Nobuo Eda 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.
Claims (2)
周縁にガスケットを配し、セパレータ板を介在して積層
された燃料電池において、上記ガスケットはセパレータ
板の少なくとも片面に独立気泡のスポンジ層を接着層を
介して接着した構造よりなる燃料電池。1. A fuel cell in which a gasket is arranged around the periphery of a unit cell composed of a positive electrode, an electrolyte plate and a negative electrode, and a separator plate is interposed between the gaskets, and the gasket is a closed-cell sponge layer on at least one surface of the separator plate. A fuel cell having a structure in which are adhered via an adhesive layer.
イオン交換膜に接する面に少なくとも電極触媒層を有す
る正極および負極からなる単位セルの周縁にガスケット
を配し、セパレータ板を介在して積層された燃料電池に
おいて、セパレータ板の少なくとも片面に独立気泡のス
ポンジ層を接着層を介して接着した構造のガスケットを
用いた燃料電池。2. A gasket is arranged around the periphery of a unit cell composed of an ion exchange membrane made of a solid polymer and a positive electrode and a negative electrode having at least an electrode catalyst layer on the surface in contact with the ion exchange membrane, with a separator plate interposed therebetween. A fuel cell in which a gasket having a structure in which a sponge layer of closed cells is adhered to at least one surface of a separator plate via an adhesive layer in a stacked fuel cell is used.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25274695A JP3353567B2 (en) | 1995-09-29 | 1995-09-29 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25274695A JP3353567B2 (en) | 1995-09-29 | 1995-09-29 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0997619A true JPH0997619A (en) | 1997-04-08 |
| JP3353567B2 JP3353567B2 (en) | 2002-12-03 |
Family
ID=17241710
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25274695A Expired - Fee Related JP3353567B2 (en) | 1995-09-29 | 1995-09-29 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3353567B2 (en) |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0933826A1 (en) * | 1998-02-03 | 1999-08-04 | Matsushita Electric Industrial Co., Ltd. | Polymer electrolyte membrane fuel cell and seal assembly therefor |
| WO2000002279A3 (en) * | 1998-06-30 | 2000-04-13 | Manhattan Scientifics Inc | Gas-proof assembly composed of a bipolar plate and a membrane-electrode unit of polymer electrolyte membrane fuel cells |
| JP2000182639A (en) * | 1998-12-16 | 2000-06-30 | Toyota Motor Corp | Seal member and fuel cell using the same |
| WO2001029921A1 (en) * | 1999-10-18 | 2001-04-26 | Matsushita Electric Industrial Co., Ltd. | Polymer electrolyte type fuel cell and production method therefor |
| WO2001048845A3 (en) * | 1999-12-23 | 2002-10-31 | Siemens Ag | Fuel cell stack, method for the assembly thereof and use of said fuel cell stack |
| JP2002352817A (en) * | 2001-05-25 | 2002-12-06 | Matsushita Electric Ind Co Ltd | Polymer electrolyte fuel cell |
| WO2004055932A3 (en) * | 2002-11-14 | 2005-05-12 | 3M Innovative Properties Co | Fuel cell gasket |
| JP2005526368A (en) * | 2002-05-17 | 2005-09-02 | スリーエム イノベイティブ プロパティズ カンパニー | Membrane electrode assembly with compression control gasket |
| US7008714B1 (en) * | 1999-10-21 | 2006-03-07 | Matsushita Electric Industrial Co., Ltd. | Polymer electrolyte fuel cell |
| JP2008004448A (en) * | 2006-06-23 | 2008-01-10 | Toyota Motor Corp | Fuel cell stack |
| EP1839358A4 (en) * | 2005-01-12 | 2008-01-23 | Lg Chemical Ltd | ASSEMBLY OF ELECTRODE MEMBRANE WITH SEAL AND FUEL CELL SYSTEM USING THE ASSEMBLY |
| JP2008293947A (en) * | 2007-05-28 | 2008-12-04 | Samsung Sdi Co Ltd | Fuel cell stack |
| JP2009537940A (en) * | 2006-05-13 | 2009-10-29 | インテリジェント エナジー リミテッド | Gasket for fuel cell |
| JP2009299903A (en) * | 2001-03-09 | 2009-12-24 | Nok Corp | Gasket |
| JP2010067602A (en) * | 2008-08-11 | 2010-03-25 | Dainippon Printing Co Ltd | Laminate of electrolyte membrane-catalyst layer with reinforcing sheet, and polymer electrolyte fuel cell equipped therewith |
| JP2010177009A (en) * | 2009-01-29 | 2010-08-12 | Nok Corp | Cell of fuel cell |
| JP2012128996A (en) * | 2010-12-14 | 2012-07-05 | Hitachi Ltd | Fuel battery |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0582151A (en) * | 1991-09-20 | 1993-04-02 | Fuji Electric Co Ltd | Fuel cell manifold seal structure |
| JPH0696783A (en) * | 1992-09-16 | 1994-04-08 | Matsushita Electric Ind Co Ltd | Fuel cell |
| JPH07249417A (en) * | 1994-03-10 | 1995-09-26 | Toyota Motor Corp | Fuel cell unit cell and method of manufacturing the same |
-
1995
- 1995-09-29 JP JP25274695A patent/JP3353567B2/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0582151A (en) * | 1991-09-20 | 1993-04-02 | Fuji Electric Co Ltd | Fuel cell manifold seal structure |
| JPH0696783A (en) * | 1992-09-16 | 1994-04-08 | Matsushita Electric Ind Co Ltd | Fuel cell |
| JPH07249417A (en) * | 1994-03-10 | 1995-09-26 | Toyota Motor Corp | Fuel cell unit cell and method of manufacturing the same |
Cited By (23)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6316139B1 (en) | 1998-02-03 | 2001-11-13 | Matsushita Electric Industrial Co., Ltd. | Fuel cell having a gasket with an adhesive layer |
| EP0933826A1 (en) * | 1998-02-03 | 1999-08-04 | Matsushita Electric Industrial Co., Ltd. | Polymer electrolyte membrane fuel cell and seal assembly therefor |
| WO2000002279A3 (en) * | 1998-06-30 | 2000-04-13 | Manhattan Scientifics Inc | Gas-proof assembly composed of a bipolar plate and a membrane-electrode unit of polymer electrolyte membrane fuel cells |
| JP2000182639A (en) * | 1998-12-16 | 2000-06-30 | Toyota Motor Corp | Seal member and fuel cell using the same |
| DE19960516B4 (en) * | 1998-12-16 | 2011-04-28 | Toyota Jidosha Kabushiki Kaisha, Toyota-shi | Seal and fuel cell with the gasket |
| US6846589B2 (en) | 1998-12-16 | 2005-01-25 | Toyota Jidosha Kabushiki Kaisha | Seal and fuel cell with the seal |
| WO2001029921A1 (en) * | 1999-10-18 | 2001-04-26 | Matsushita Electric Industrial Co., Ltd. | Polymer electrolyte type fuel cell and production method therefor |
| US7008714B1 (en) * | 1999-10-21 | 2006-03-07 | Matsushita Electric Industrial Co., Ltd. | Polymer electrolyte fuel cell |
| WO2001048845A3 (en) * | 1999-12-23 | 2002-10-31 | Siemens Ag | Fuel cell stack, method for the assembly thereof and use of said fuel cell stack |
| JP2009299903A (en) * | 2001-03-09 | 2009-12-24 | Nok Corp | Gasket |
| JP2002352817A (en) * | 2001-05-25 | 2002-12-06 | Matsushita Electric Ind Co Ltd | Polymer electrolyte fuel cell |
| US8343682B2 (en) | 2002-05-17 | 2013-01-01 | 3M Innovative Properties Company | Membrane electrode assembly with compression control gasket |
| JP2005526368A (en) * | 2002-05-17 | 2005-09-02 | スリーエム イノベイティブ プロパティズ カンパニー | Membrane electrode assembly with compression control gasket |
| WO2004055932A3 (en) * | 2002-11-14 | 2005-05-12 | 3M Innovative Properties Co | Fuel cell gasket |
| EP1839358A4 (en) * | 2005-01-12 | 2008-01-23 | Lg Chemical Ltd | ASSEMBLY OF ELECTRODE MEMBRANE WITH SEAL AND FUEL CELL SYSTEM USING THE ASSEMBLY |
| US7544219B2 (en) | 2005-01-12 | 2009-06-09 | Lg Chem, Ltd. | Gasketed membrane-electrode-assembly and fuel cell system employing the same |
| JP2009537940A (en) * | 2006-05-13 | 2009-10-29 | インテリジェント エナジー リミテッド | Gasket for fuel cell |
| JP2008004448A (en) * | 2006-06-23 | 2008-01-10 | Toyota Motor Corp | Fuel cell stack |
| JP2008293947A (en) * | 2007-05-28 | 2008-12-04 | Samsung Sdi Co Ltd | Fuel cell stack |
| US8232021B2 (en) * | 2007-05-28 | 2012-07-31 | Samsung Sdi Co., Ltd. | Stack for fuel cell |
| JP2010067602A (en) * | 2008-08-11 | 2010-03-25 | Dainippon Printing Co Ltd | Laminate of electrolyte membrane-catalyst layer with reinforcing sheet, and polymer electrolyte fuel cell equipped therewith |
| JP2010177009A (en) * | 2009-01-29 | 2010-08-12 | Nok Corp | Cell of fuel cell |
| JP2012128996A (en) * | 2010-12-14 | 2012-07-05 | Hitachi Ltd | Fuel battery |
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