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JP4868302B2 - Fuel cell, cell structure and manufacturing method thereof - Google Patents
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JP4868302B2 - Fuel cell, cell structure and manufacturing method thereof - Google Patents

Fuel cell, cell structure and manufacturing method thereof Download PDF

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JP4868302B2
JP4868302B2 JP2004304743A JP2004304743A JP4868302B2 JP 4868302 B2 JP4868302 B2 JP 4868302B2 JP 2004304743 A JP2004304743 A JP 2004304743A JP 2004304743 A JP2004304743 A JP 2004304743A JP 4868302 B2 JP4868302 B2 JP 4868302B2
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electrolyte
conductive substrate
electrode
cell
electrodes
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JP2006120366A (en
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昌幸 国松
健 伊藤
皓一 木村
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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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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Description

本発明は、燃料電池およびその製造方法に関し、より詳細には、小型化が可能な燃料電池およびその製造方法に関する。   The present invention relates to a fuel cell and a method for manufacturing the same, and more particularly to a fuel cell that can be miniaturized and a method for manufacturing the same.

近年、環境問題や資源問題への対策が重要になっており、その対策のひとつとして燃料電池が注目されている。特に、直接型燃料電池は、メタノールを燃料に用い、改質やガス化を行わずに直接発電することができるため、構造がシンプルで、小型化、軽量化が容易であり、携帯電話や携帯用のコンピュータ等の小型コンシューマ電源として有望である。直接メタノール型燃料電池では、一般に燃料極側にメタノール水溶液を供給すると、電池反応によって炭酸ガスが発生し、燃料排気物としては廃燃料と炭酸ガスが排出される。一方、空気極側では、酸化剤として空気を供給すると、電池反応により水が発生し、空気とともに排出される。   In recent years, countermeasures against environmental problems and resource problems have become important, and fuel cells have attracted attention as one of the countermeasures. In particular, direct fuel cells use methanol as fuel and can directly generate power without reforming or gasification, so the structure is simple, and it is easy to reduce the size and weight. It is promising as a small-sized consumer power supply for computers. In a direct methanol fuel cell, generally, when an aqueous methanol solution is supplied to the fuel electrode side, carbon dioxide gas is generated by the cell reaction, and waste fuel and carbon dioxide gas are discharged as fuel exhaust. On the other hand, when air is supplied as an oxidant on the air electrode side, water is generated by a battery reaction and is discharged together with air.

このように直接メタノール型燃料電池を用いる場合、直接メタノール型燃料電池の作動電圧は、セル当たりの出力電圧が低いため、複数のセルを直列に接続して昇圧する必要がある。このため、通常は図1に示すようにセパレータを介して積層する等により昇圧を行なっていることから、大型化が避けられず、よりいっそうの小型化が必要である。   When a direct methanol fuel cell is used in this way, the operating voltage of the direct methanol fuel cell has a low output voltage per cell, so it is necessary to boost the voltage by connecting a plurality of cells in series. For this reason, normally, as shown in FIG. 1, the pressure is increased by laminating via a separator or the like, so an increase in size is inevitable, and a further reduction in size is required.

従来の燃料電池は、電解質材料を2つの電極で挟みセパレータを介して積層し電池ケース等に収容して形成されるものが一般的であり、このような燃料電池の小型化を計るため図2に示すような半導体を作成するための微細加工技術などが用いられて電極を微細化することが提案されている(例えば、特許文献1参照)。   A conventional fuel cell is generally formed by sandwiching an electrolyte material between two electrodes through a separator and accommodating it in a battery case or the like. In order to reduce the size of such a fuel cell, FIG. It has been proposed that the electrodes be miniaturized by using a microfabrication technique or the like for producing a semiconductor as shown in FIG.

特開平2004−111343号公報Japanese Patent Laid-Open No. 2004-111343 特開平2002−280016号公報JP-A-2002-280016 特開平2003−264003号公報Japanese Patent Laid-Open No. 2003-264003

しかしながら、燃料電池の電解質部については、電解質として通常用いられる材料に上述の半導体微細加工技術を使用することはできず、逆に微細加工が可能なセラミック系材料を電解質材料として用いると極端に性能が低下することから、電極が小型化されても電解質部の形状が従来とほとんど変わらないため、電池全体としては効果的に小型化ができないという問題がある。   However, for the electrolyte part of fuel cells, the above-mentioned semiconductor microfabrication technology cannot be used as a material normally used as an electrolyte. Conversely, if a ceramic material that can be microfabricated is used as an electrolyte material, the performance is extremely high. Since the shape of the electrolyte portion is almost the same as the conventional one even when the electrode is downsized, the battery as a whole cannot be effectively downsized.

また、従来の電解質材料に電極を狭持する電池の場合、通常、電極同士の短絡や燃料漏れなどを防止するため、電極よりもやや大型の電解質材料を用いるが、電解質材料の電極よりも大きい部分は燃料電池の作用としては使用できない部分となる(例えば、図2を参照すると、電極201が電解質膜202を挟み込むような構造になっているので、電解質のうち電極にはさまれていない部分は全く電解質部としての役割を果たさず無駄になっている)ため、結果的に高価な電解質材料を無駄にするという問題がある。   In addition, in the case of a battery in which an electrode is sandwiched between conventional electrolyte materials, an electrolyte material that is slightly larger than the electrode is usually used in order to prevent short-circuit between electrodes or fuel leakage, but it is larger than the electrode of the electrolyte material. The portion becomes a portion that cannot be used as an operation of the fuel cell (for example, referring to FIG. 2, since the electrode 201 has a structure sandwiching the electrolyte membrane 202, the portion of the electrolyte that is not sandwiched between the electrodes) Does not play a role as an electrolyte part at all), resulting in a problem of wasting expensive electrolyte material.

本発明は、このような問題に鑑みてなされたもので、電解質部の構造を微細化可能なものとすることにより、燃料電池の新しいセル構造を提案し、電解質を効率的に利用することを目的とする。また、電解質材料の無駄を回避することにより低コストの燃料電池を提供することを目的とする。   The present invention has been made in view of such problems, and by making the structure of the electrolyte portion miniaturizable, it proposes a new cell structure of a fuel cell and uses the electrolyte efficiently. Objective. Another object of the present invention is to provide a low-cost fuel cell by avoiding waste of electrolyte material.

このような目的を達成するために、本発明のセル構造は、1つの不導体基板を貫通して形成される複数の孔部に電解質材料を満たして形成された複数の電解質部と、該複数の電解質部の各々の前記不導体基板表面における露出面、該孔部の上面および下面に電極材料を被覆することにより配置される複数の電極とを備え、該複数の電解質部の各々の露出面に配置される電極のうちの1つは、該電解質部に隣接する電解質部の両側に配置される電極のうち、該電極のうちの1つと前記不導体基板をはさんで反対側に配置された他の電極と接続することにより、前記不導体基板の上面または下面のいずれかのみに燃料を供給することにより発電可能であることを特徴とする。 In order to achieve such an object, the cell structure of the present invention includes a plurality of electrolyte portions formed by filling a plurality of holes formed through one non-conductive substrate with an electrolyte material, and the plurality of electrolyte portions. A plurality of electrodes disposed on the exposed surface of the non- conductive substrate surface of each of the electrolyte portions by covering an upper surface and a lower surface of the hole portion with an electrode material, and exposing each of the plurality of electrolyte portions One of the electrodes arranged on the surface is arranged on the opposite side between one of the electrodes and the non-conductive substrate among the electrodes arranged on both sides of the electrolyte part adjacent to the electrolyte part. By connecting to the other electrode, it is possible to generate power by supplying fuel only to either the upper surface or the lower surface of the non-conductive substrate .

また、本発明の燃料電池は、電極と、電解質部と、燃料供給部と、酸素供給部とを備えた燃料電池であって、前記電解質部は、1つの不導体基板を貫通して形成される複数の孔部に電解質材料を満たして形成された複数の電解質部であり、前記電極は、該複数の電解質部の各々の前記不導体基板表面における露出面、該孔部の上面および下面に電極材料を被覆することにより配置される複数の電極であり、前記燃料供給部は、前記不導体基板の片面のみに配置され、該複数の電解質部の各々の露出面に配置される電極のうちの1つは、該電解質部に隣接する電解質部の両側に配置される電極のうち、該電極のうちの1つと前記不導体基板をはさんで反対側に配置された他の電極と接続することにより、前記不導体基板の上面または下面のいずれかのみに燃料を供給することにより発電可能であることを特徴とする。 The fuel cell of the present invention is a fuel cell comprising an electrode, an electrolyte part, a fuel supply part, and an oxygen supply part, wherein the electrolyte part is formed through one non-conductive substrate. A plurality of electrolyte parts formed by filling the plurality of holes with an electrolyte material, and the electrodes are exposed on the non- conductive substrate surface of each of the plurality of electrolyte parts, and the upper and lower surfaces of the hole parts A plurality of electrodes disposed by coating the electrode material with the fuel material , wherein the fuel supply portion is disposed only on one surface of the non-conductive substrate, and the electrode disposed on each exposed surface of the plurality of electrolyte portions. One of the electrodes arranged on both sides of the electrolyte part adjacent to the electrolyte part is connected to one of the electrodes and another electrode arranged on the opposite side across the non-conductive substrate. The upper or lower surface of the non-conductive substrate Characterized in that it is a possible power by supplying fuel only to Reka.

さらに、本発明のセル構造の製造方法は、1つの不導体基板を貫通して複数の孔部を形成するステップと、前記形成された孔部に電解質材料を満たし、複数の電解質部を形成するステップと、該複数の電解質部の各々の前記不導体基板表面における露出面、該孔部の上面および下面に電極材料を被覆することにより、複数の電極を配置するステップとを備え、該複数の電解質部の各々の露出面に配置される電極のうちの1つは、該電解質部に隣接する電解質部の両側に配置される電極のうち、該電極のうちの1つと前記不導体基板をはさんで反対側に配置された他の電極と接続することにより、前記不導体基板の上面または下面のいずれかのみに燃料を供給することにより発電可能であることを特徴とする。 Furthermore, in the method for manufacturing a cell structure of the present invention, a plurality of holes are formed through one non-conductive substrate, and the formed holes are filled with an electrolyte material to form a plurality of electrolytes. And a step of disposing a plurality of electrodes on the exposed surface of the non- conductive substrate surface of each of the plurality of electrolyte portions by covering an upper surface and a lower surface of the hole portion with an electrode material. One of the electrodes disposed on each exposed surface of the electrolyte part includes one of the electrodes disposed on both sides of the electrolyte part adjacent to the electrolyte part and the non-conductive substrate . It is possible to generate power by supplying fuel only to either the upper surface or the lower surface of the non-conductive substrate by connecting to another electrode disposed on the opposite side across the gap .

以上説明したように、本発明によれば、不導体の一部に電解質材料を満たして形成される電解質部と、電解質部の側面部に配置される電極とを備えることにより、燃料電池の新しいセル構造を提案し、電解質を効率的に利用することができる。また、電解質材料の無駄を回避することにより低コストの燃料電池を提供することができる。   As described above, according to the present invention, a new fuel cell is provided by including an electrolyte part formed by filling a part of a nonconductor with an electrolyte material and an electrode disposed on a side part of the electrolyte part. A cell structure is proposed and the electrolyte can be used efficiently. Moreover, a low-cost fuel cell can be provided by avoiding waste of the electrolyte material.

以下、図面を参照しながら本発明の実施形態について詳細に説明する。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

(燃料電池の構造)
図3は、本発明の一実施形態にかかる燃料電池の構造示す断面図である。従来の燃料電池における電解質部は、上述の通り板状等の電解質材料をそのまま使用していたのに対し、本発明の電解質部は不導体基板に形成された穴部に電解質材料を満たすような形で作成される。すなわち、本発明の電解質部は、従来技術のように電解質材料自体を切削等してセル構造に組み込まれる形態に形成するのではなく、セルを構成する不導体基板等に電解質部を満たす部分があり、その部分に電解質部が形成されるように電解質材料が満たされるようになっている。したがって、燃料電池に用いられる電解質部がこのような構造を有すれば本発明の技術的範囲にあり、その構造の形状や電解質部の形成方法はどのようなものであっても良い。例えば、電解質部の形成方法としては、不導体部に孔部をあけておいてその孔部に電解質溶液を流し込む方法も可能であり、また電解質材料と不導体部を共に形成させる方法によることもできる。結局、その形成方法によらず何らかの形状、材質の不導体に電解質材料を埋め込んだような構造の電解質部を有する燃料電池は、本発明の技術的範囲に含まれるということができる。
(Fuel cell structure)
FIG. 3 is a cross-sectional view showing the structure of a fuel cell according to an embodiment of the present invention. The electrolyte portion in the conventional fuel cell uses the plate-like electrolyte material as it is as described above, whereas the electrolyte portion of the present invention fills the electrolyte material in the hole formed in the non-conductive substrate. Created in shape. That is, the electrolyte part of the present invention is not formed into a form that is incorporated into the cell structure by cutting the electrolyte material itself as in the prior art, but a portion that fills the electrolyte part in a non-conductive substrate or the like constituting the cell. Yes, and the electrolyte material is filled so that the electrolyte part is formed in that part. Therefore, if the electrolyte part used for the fuel cell has such a structure, it is within the technical scope of the present invention, and the shape of the structure and the method for forming the electrolyte part may be any method. For example, as a method of forming the electrolyte part, a method of forming a hole in the non-conductor part and pouring the electrolyte solution into the hole part is also possible, or a method of forming both the electrolyte material and the non-conductor part. it can. After all, it can be said that a fuel cell having an electrolyte part with a structure in which an electrolyte material is embedded in a non-conductor of any shape and material regardless of the formation method is included in the technical scope of the present invention.

図3の示す本実施形態の燃料電池は、不導体基板301に開けられた孔部に高分子電解質304を流し込んで乾燥、固定化した構造の電解質部を持つ。ここで、不導体基板は、本実施形態の燃料電池のセル構造の基盤をなすものであり、このようにして形成された電解質部に電極303、302が形成されて燃料電池のセル構造となる。したがって、このような目的を達成するものであれば、プラスチックやガラス等いずれの固体の不導体材料を使用することもでき、形状も本実施形態にあるような板状のものに限られることはない。   The fuel cell of the present embodiment shown in FIG. 3 has an electrolyte part having a structure in which a polymer electrolyte 304 is poured into a hole formed in a non-conductive substrate 301 and dried and fixed. Here, the non-conductive substrate forms the basis of the cell structure of the fuel cell according to the present embodiment, and the electrodes 303 and 302 are formed on the electrolyte portion formed in this way to form the cell structure of the fuel cell. . Therefore, any solid non-conductive material such as plastic or glass can be used as long as it achieves such an object, and the shape is limited to a plate-like material as in this embodiment. Absent.

図4は、本実施形態の燃料電池を作成するに当たり、複数の孔部をあけられた不導体基板を示す図である。不導体基板301には、規則正しく一定の円柱型の孔部401が形成されており、孔部401は不導体基板301を貫通するように形成されている。このように孔部を形成することにより、例えば上面側に燃料極を置き、底面側に空気極を配置すれば容易にセルを作成することができるのである。ただし、孔部401は不導体基板を貫通する必要はなく、底面側に空気あるいは燃料を供給する構造を設ければ上面側だけあるいは、両面共に開口する必要はない。   FIG. 4 is a view showing a non-conductive substrate in which a plurality of holes are formed in producing the fuel cell of the present embodiment. The non-conductive substrate 301 is regularly formed with a fixed cylindrical hole 401, and the hole 401 is formed so as to penetrate the non-conductive substrate 301. By forming the hole in this manner, for example, if the fuel electrode is placed on the upper surface side and the air electrode is placed on the bottom surface side, the cell can be easily created. However, the hole 401 does not need to penetrate the non-conductive substrate, and if the structure for supplying air or fuel is provided on the bottom surface side, it is not necessary to open only the top surface or both surfaces.

本実施形態では、図4に示す不導体基板301の孔部401内にある電解質材料が電解質部304を構成するが、この電解質部304に電極を両側から埋め込む。図3を参照すると、上側から燃料であるメタノール水溶液306が供給されるので、燃料極303を不導体基板301の上側に埋め込み、空気極302を下側に埋め込めばよいことが理解できる。本実施形態では3つのセルが燃料極303と空気極302とを導体接続部305により電気的に連結させて直列構造をとるようになっているが、当然3つに限られるわけではなく、連結方法も図3に示されるようなもの以外の方法とすることができるのは明らかである。なお、導体接続部305は本実施形態では、後述するような直列接続構造によるが、その他の方法も目的が達成される限り使用することができる。   In the present embodiment, the electrolyte material in the hole 401 of the non-conductive substrate 301 shown in FIG. 4 constitutes the electrolyte part 304, and electrodes are embedded in the electrolyte part 304 from both sides. Referring to FIG. 3, since the methanol aqueous solution 306 as fuel is supplied from the upper side, it can be understood that the fuel electrode 303 may be embedded above the non-conductive substrate 301 and the air electrode 302 may be embedded below. In the present embodiment, the three cells have a series structure in which the fuel electrode 303 and the air electrode 302 are electrically connected by the conductor connecting portion 305, but of course, the number of cells is not limited to three. Obviously, the method can be other than that shown in FIG. In this embodiment, the conductor connection portion 305 has a series connection structure as described later, but other methods can be used as long as the object is achieved.

実際に、多くの直列接続構造が提案されているが(例えば、特許文献2または3参照)、本実施形態のセル構造をこれらの技術と組み合わせて、より一層の効果を奏することは、当業者であれば理解することができる。   Actually, many series connection structures have been proposed (see, for example, Patent Document 2 or 3), but it is a person skilled in the art to combine the cell structure of this embodiment with these techniques to achieve further effects. If so, you can understand.

以上の構造を有するセル構造に燃料および酸素が供給されて燃料電池として電力を発生させることとなる。燃料および酸素の供給方法や装置の構造については、従来から良く知られており、そのような技術のいずれも本実施形態のセル構造に適用することができる。なお、本実施形態では燃料306はメタノール水溶液であり、燃料電池としての作用は、基本的に従来技術のDMFC(直接メタノール型燃料電池)と同様であるので、ここでは説明を省略するが、本実施形態の基本構造を有するセルであればDMFCはもちろん、その他のタイプの燃料電池のセルとして使用することができるのは言うまでもない。   Fuel and oxygen are supplied to the cell structure having the above structure to generate electric power as a fuel cell. The fuel and oxygen supply method and the structure of the apparatus are well known in the art, and any of such techniques can be applied to the cell structure of this embodiment. In the present embodiment, the fuel 306 is a methanol aqueous solution, and the operation as a fuel cell is basically the same as that of the DMFC (direct methanol fuel cell) of the prior art, and therefore the description thereof is omitted here. Needless to say, any cell having the basic structure of the embodiment can be used as a cell for DMFC as well as other types of fuel cells.

(燃料電池の製造方法)
次に、燃料電池の製造方法、すなわち本発明のセル構造を形成する方法について説明する。図5は、本実施形態のセル構造形成方法を示すフローチャートである。
(Fuel cell manufacturing method)
Next, a method for manufacturing a fuel cell, that is, a method for forming the cell structure of the present invention will be described. FIG. 5 is a flowchart showing the cell structure forming method of the present embodiment.

まず、不導体材料を板状に切削する等により作成し、孔を開けて孔部を形成させる(S501)。次に、形成された孔部に電解質材料を埋め込み(S502)、固定化して電解質部を形成する(S503)。本実施形態では、電解質溶液を孔部に流し込み、乾燥後熱処理を行なって固定化し、電解質部を形成する。電解質部が形成されると、電解質部の両側に電極触媒を埋め込んで(S504)、最後に配線を行なう(S505)。   First, a non-conductive material is prepared by cutting into a plate shape, and a hole is formed by forming a hole (S501). Next, an electrolyte material is embedded in the formed hole (S502) and fixed to form an electrolyte part (S503). In the present embodiment, the electrolyte solution is poured into the pores, heat-treated after drying, and fixed to form the electrolyte portion. When the electrolyte part is formed, an electrode catalyst is embedded on both sides of the electrolyte part (S504), and finally wiring is performed (S505).

以上が本発明のセル構造製造方法の一例であるが、当業者であれば、これにより得られたセル構造を用いて本技術分野で知られた、あるいは今後開発される燃料電池の製造方法をさらに適用して燃料電池を製造することがきるが、その詳細は省略する。また、こうしたセル構造から燃料電池を製造する方法は種々存在するが、本発明のセル構造を用いて、いずれの製造方法によっても燃料電池を製造することができるのは明らかである。   The above is an example of the cell structure manufacturing method of the present invention. However, those skilled in the art will know how to manufacture a fuel cell that is known in this technical field or that will be developed in the future using the cell structure thus obtained. Further, it can be applied to manufacture a fuel cell, but the details are omitted. Further, there are various methods for manufacturing a fuel cell from such a cell structure, but it is clear that a fuel cell can be manufactured by any of the manufacturing methods using the cell structure of the present invention.

(実施例1)
次に本実施形態のセル構造を用いた燃料電池の一例について図3を参照して説明する。本実施形態では、不導体301としてポリサルフォン樹脂の1mm厚の基板を用いたが、材料としてはこれに限られない。ただし、本実施例では一定の耐熱・耐酸性・耐アルコール性が必要なので、これらを満たす材料とした。
Example 1
Next, an example of a fuel cell using the cell structure of this embodiment will be described with reference to FIG. In this embodiment, a 1 mm thick substrate of polysulfone resin is used as the non-conductor 301, but the material is not limited to this. However, in this example, since certain heat resistance, acid resistance, and alcohol resistance are necessary, the material satisfying these was used.

本実施例の孔部は直径0.5mmの円形に貫通させるので、孔部401の形状は高さ1mm直径0.5mmの円柱となる。この孔部401に20wt%Naflon溶液を0.2μl注入し、室温で30分乾燥させる。その後、135℃(通常、120℃〜140℃が望ましい)に設定された電気炉により、10分間熱処理を行うことによって、孔部に高分子電解質を固着させる。これにより電解質部が形成される。   Since the hole of this embodiment is penetrated in a circle having a diameter of 0.5 mm, the shape of the hole 401 is a cylinder having a height of 1 mm and a diameter of 0.5 mm. 0.2 μl of 20 wt% Naflon solution is injected into the hole 401 and dried at room temperature for 30 minutes. Thereafter, the polymer electrolyte is fixed to the pores by performing heat treatment for 10 minutes in an electric furnace set to 135 ° C. (usually 120 ° C. to 140 ° C. is desirable). Thereby, an electrolyte part is formed.

次に、高分子電解質の両面に電極触媒を塗布することにより本実施例の燃料電池のセル構造が作成される。電極触媒は、白金触媒や白金ルテニウム合金触媒を電解質溶液とよく混合して、ペースト状の懸濁液を準備して塗布を行なう。すなわち、この触媒懸濁液を高分子電解質の両面に塗布して室温で約30分間乾燥させ、ホットプレス器を用いて135℃(通常、120℃〜140℃が望ましい)で1分間熱処理を行なうことにより電極を形成する。最後に、基板上に金を蒸着する方法で電流リードのための配線を作成する。   Next, the cell structure of the fuel cell of this example is created by applying an electrode catalyst on both sides of the polymer electrolyte. As the electrode catalyst, a platinum catalyst or a platinum ruthenium alloy catalyst is mixed well with an electrolyte solution, and a paste-like suspension is prepared and applied. That is, this catalyst suspension is applied to both sides of the polymer electrolyte, dried at room temperature for about 30 minutes, and heat-treated at 135 ° C. (usually 120 ° C. to 140 ° C.) for 1 minute using a hot press. Thus, an electrode is formed. Finally, wiring for current leads is created by a method of depositing gold on the substrate.

図6は、本実施例のセル1個を用いた燃料電池の出力特性を示す図である。燃料にメタノール溶液(5wt%)を使用して、燃料極に直接メタノール溶液を供給し、自然吸気により空気の供給を行なってDMFC法により電力の出力を確認することができた。これにより本実施例による燃料電池の単セル性能としては、常温で1.6mW/cmの出力密度となるのが理解できる。 FIG. 6 is a graph showing the output characteristics of a fuel cell using one cell of this example. Using a methanol solution (5 wt%) as the fuel, the methanol solution was directly supplied to the fuel electrode, and air was supplied by natural aspiration, and the power output was confirmed by the DMFC method. Thus, it can be understood that the single cell performance of the fuel cell according to the present example is 1.6 mW / cm 2 at a normal temperature.

また、図8は、同様にセル3個を直列に接続して作成された燃料電池について、出力特性を取ったものである。燃料、空気条件は図6を参照して説明したセル1個の場合と同様である。図8を参照すると、本実施例のセルの場合セルの断面は直径0.5mmであるから3個用いた燃料電池の場合、ほぼ3.8mW/cmの出力密度となるのが理解できる。 FIG. 8 shows the output characteristics of a fuel cell similarly formed by connecting three cells in series. The fuel and air conditions are the same as in the case of one cell described with reference to FIG. Referring to FIG. 8, it can be understood that in the case of the cell of the present embodiment, the cell has a cross section of 0.5 mm in diameter, so that in the case of using three fuel cells, the output density is approximately 3.8 mW / cm 2 .

以上により、電解質を効率的に利用することができ、また電解質材料の無駄を回避することにより低コストの燃料電池を提供することができる   As described above, the electrolyte can be used efficiently, and a low-cost fuel cell can be provided by avoiding waste of the electrolyte material.

(実施例2)
本実施例においては、上述の実施例で使用したポリサルフォン樹脂の不導体基板に替えて、ガラス製の不導体基板を使用する。本実施例の不導体基板は十分な耐熱・耐酸性・耐アルコール性を有するので、本発明の実施には最適である。その他の点については実施例1と同様なので説明を省略する。
(Example 2)
In this embodiment, a non-conductive substrate made of glass is used instead of the non-conductive substrate of polysulfone resin used in the above-described embodiment. Since the non-conductive substrate of this example has sufficient heat resistance, acid resistance, and alcohol resistance, it is optimal for the implementation of the present invention. Since other points are the same as those in the first embodiment, description thereof is omitted.

(実施例3)
図7は、本実施例の直列接続構造を示す図である。従来技術あるいは上述の実施例1を見ても理解できるように一般に単セルでは燃料電池の要求される電圧を得ることはできないから、通常いずれかの方法によりセルを直列接続して必要な電圧を得る必要がある。必要な電圧とは、電子機器で使用するためには3〜5V程度であるが、使用機器によってはさらに高い電圧を必要とするものもある。
(Example 3)
FIG. 7 is a diagram showing a series connection structure of the present embodiment. As can be understood from the prior art or the above-described first embodiment, generally, a single cell cannot obtain the required voltage of the fuel cell. Therefore, the cells are usually connected in series by any method to obtain the required voltage. Need to get. The necessary voltage is about 3 to 5 V for use in an electronic device, but some devices require a higher voltage.

本実施例では、各セルを直列接続するため図7に示すように電極を配線する。図7は、本実施例の基板を上面から見たものであるが、上面側の導電性のセル結合部材701、706等だけではなく下面側にも導電性のセル結合部材704、705等が貼り付けられており、これにより各セルの電極同士が電気的に接続される。すなわち、セル部分702の下側には、セル接合部705の一部があり、その一方セル結合部材706の一端703には導体接続部305が結合されて上面側に不導体基板301を貫通してセル接合部706に接続されている。以下同様の接続が行なわれて各セルは直列に接続され、セル接合部701からセル接合部704までが直接接続されることとなる。本実施例では、13個のセルが直列接続されることとなる。   In this embodiment, electrodes are wired as shown in FIG. 7 in order to connect the cells in series. FIG. 7 is a top view of the substrate of this embodiment, but not only the conductive cell coupling members 701 and 706 on the upper surface side but also the conductive cell coupling members 704 and 705 on the lower surface side. The electrodes of each cell are electrically connected to each other. That is, there is a part of the cell junction 705 below the cell portion 702, and the conductor connection portion 305 is coupled to one end 703 of the cell coupling member 706 so as to penetrate the non-conductive substrate 301 on the upper surface side. Connected to the cell junction 706. Thereafter, the same connection is performed, the cells are connected in series, and the cell junction 701 to the cell junction 704 are directly connected. In this embodiment, 13 cells are connected in series.

図8に、上述の実施例1のセルを本実施例の構造で直列接続した本実施例の燃料電池の出力特性を示す。このように直列接続することにより、より実用的な電圧を得ることができる。以上により、微細加工技術によって電極を直列接続にして、実用的な電圧を得ると共に電池全体の小型化が可能となる。   FIG. 8 shows the output characteristics of the fuel cell of this example in which the cells of Example 1 described above are connected in series with the structure of this example. By connecting in series in this way, a more practical voltage can be obtained. As described above, the electrodes can be connected in series by a microfabrication technique to obtain a practical voltage and to reduce the size of the entire battery.

従来の燃料電池のスタック構造の一例を示す図である。It is a figure which shows an example of the stack structure of the conventional fuel cell. 従来の半導体を作成するための微細加工技術などを用いて電極を微細化した例を示す図である。It is a figure which shows the example which refined | miniaturized the electrode using the microfabrication technique for producing the conventional semiconductor. 本発明の一実施形態にかかる燃料電池の構造を示す断面図である。It is sectional drawing which shows the structure of the fuel cell concerning one Embodiment of this invention. 本実施形態の燃料電池を作成するに当たり、複数の孔部をあけられた不導体基板を示す図である。It is a figure which shows the non-conductive board | substrate which opened the some hole part in producing the fuel cell of this embodiment. 本実施形態のセル構造形成方法を示すフローチャートである。It is a flowchart which shows the cell structure formation method of this embodiment. 本実施例のセル1個を用いた燃料電池の出力特性を示す図である。It is a figure which shows the output characteristic of the fuel cell using one cell of a present Example. 本実施例の直列接続構造を示す図である。It is a figure which shows the serial connection structure of a present Example. 本実施例のセル3個を用いた燃料電池の出力特性を示す図である。It is a figure which shows the output characteristic of the fuel cell using three cells of a present Example.

符号の説明Explanation of symbols

101 スタック構造
102 セパレータ
103 燃料極
104 固体高分子膜
105 空気極
201 電極
202 電解質膜
301 不導体基板
302、303 電極
304 高分子電解質
305 導体接続部
306 燃料
401 孔部
701、704、705、706 セル接合部
702 セル部
703 セル接合部の一端
DESCRIPTION OF SYMBOLS 101 Stack structure 102 Separator 103 Fuel electrode 104 Solid polymer film 105 Air electrode 201 Electrode 202 Electrolyte membrane 301 Non-conductive substrate 302, 303 Electrode 304 Polymer electrolyte 305 Conductor connection part 306 Fuel 401 Hole part 701, 704, 705, 706 Cell Joint part 702 Cell part 703 One end of the cell joint part

Claims (6)

1つの不導体基板を貫通して形成される複数の孔部に電解質材料を満たして形成された複数の電解質部と、
該複数の電解質部の各々の前記不導体基板表面における露出面に、該孔部の上面および下面に電極材料を被覆することにより配置される複数の電極と
を備え、該複数の電解質部の各々の露出面に配置される電極のうちの1つは、該電解質部に隣接する電解質部の両側に配置される電極のうち、該電極のうちの1つと前記不導体基板をはさんで反対側に配置された他の電極と接続することにより、前記不導体基板の上面または下面のいずれかのみに燃料を供給することにより発電可能であることを特徴とするセル構造。
A plurality of electrolyte portions formed by filling a plurality of holes formed through one non-conductive substrate with an electrolyte material;
A plurality of electrodes disposed on the exposed surface of the non-conductive substrate surface of each of the plurality of electrolyte portions by covering an upper surface and a lower surface of the hole portion with an electrode material, and each of the plurality of electrolyte portions One of the electrodes disposed on the exposed surface of the first electrode is an opposite side of the electrode disposed on both sides of the electrolyte portion adjacent to the electrolyte portion, with one of the electrodes sandwiching the non-conductive substrate. A cell structure characterized in that power can be generated by supplying fuel only to either the upper surface or the lower surface of the non-conductive substrate by connecting to another electrode disposed on the substrate.
前記不導体基板は、ポリサルフォン酸樹脂の基板であることを特徴とする請求項1に記載のセル構造。   The cell structure according to claim 1, wherein the non-conductive substrate is a polysulfonic acid resin substrate. 前記不導体基板は、ガラス製の基板であることを特徴とする請求項1に記載のセル構造。 The cell structure according to claim 1, wherein the non-conductive substrate is a glass substrate. 前記電解質材料は、高分子電解質であり、
前記電極は、白金または白金ルテニウム触媒電極であることを特徴とする請求項1ないし3のいずれかに記載のセル構造。
The electrolyte material is a polymer electrolyte,
4. The cell structure according to claim 1, wherein the electrode is a platinum or platinum ruthenium catalyst electrode.
電極と、電解質部と、燃料供給部と、酸素供給部とを備えた燃料電池であって、
前記電解質部は、1つの不導体基板を貫通して形成される複数の孔部に電解質材料を満たして形成された複数の電解質部であり、
前記電極は、該複数の電解質部の各々の前記不導体基板表面における露出面に、該孔部の上面および下面に電極材料を被覆することにより配置される複数の電極であり、
前記燃料供給部は、前記不導体基板の片面のみに配置され、
該複数の電解質部の各々の露出面に配置される電極のうちの1つは、該電解質部に隣接する電解質部の両側に配置される電極のうち、該電極のうちの1つと前記不導体基板をはさんで反対側に配置された他の電極と接続することにより、前記不導体基板の上面または下面のいずれかのみに燃料を供給することにより発電可能であることを特徴とする燃料電池。
A fuel cell comprising an electrode, an electrolyte part, a fuel supply part, and an oxygen supply part,
The electrolyte part is a plurality of electrolyte parts formed by filling a plurality of holes formed through one non-conductive substrate with an electrolyte material,
The electrodes are a plurality of electrodes arranged by coating an electrode material on an upper surface and a lower surface of the hole portion on the exposed surface of the non-conductive substrate surface of each of the plurality of electrolyte portions,
The fuel supply unit is disposed only on one side of the non-conductive substrate,
One of the electrodes disposed on the exposed surface of each of the plurality of electrolyte portions may include one of the electrodes disposed on both sides of the electrolyte portion adjacent to the electrolyte portion and the non-conductor. A fuel cell characterized in that power generation is possible by supplying fuel only to the upper surface or the lower surface of the non-conductive substrate by connecting to another electrode disposed on the opposite side across the substrate. .
1つの不導体基板を貫通して複数の孔部を形成するステップと、
前記形成された孔部に電解質材料を満たし、複数の電解質部を形成するステップと、
該複数の電解質部の各々の前記不導体基板表面における露出面に、該孔部の上面および下面に電極材料を被覆することにより、複数の電極を配置するステップと
を備え、該複数の電解質部の各々の露出面に配置される電極のうちの1つは、該電解質部に隣接する電解質部の両側に配置される電極のうち、該電極のうちの1つと前記不導体基板をはさんで反対側に配置された他の電極と接続することにより、前記不導体基板の上面または下面のいずれかのみに燃料を供給することにより発電可能であることを特徴とするセル構造の製造方法。
Forming a plurality of holes through one non-conductive substrate;
Filling the formed pores with an electrolyte material to form a plurality of electrolyte portions;
Arranging a plurality of electrodes on the exposed surface of each of the plurality of electrolyte portions on the surface of the non-conductive substrate by covering an upper surface and a lower surface of the hole with an electrode material, and the plurality of electrolyte portions One of the electrodes disposed on each exposed surface of each of the electrodes is one of the electrodes disposed on both sides of the electrolyte part adjacent to the electrolyte part and sandwiches the non-conductive substrate. A method of manufacturing a cell structure, wherein power generation is possible by supplying fuel only to either the upper surface or the lower surface of the non-conductive substrate by connecting to another electrode disposed on the opposite side.
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