JPS6322422B2 - - Google Patents
Info
- Publication number
- JPS6322422B2 JPS6322422B2 JP57039912A JP3991282A JPS6322422B2 JP S6322422 B2 JPS6322422 B2 JP S6322422B2 JP 57039912 A JP57039912 A JP 57039912A JP 3991282 A JP3991282 A JP 3991282A JP S6322422 B2 JPS6322422 B2 JP S6322422B2
- Authority
- JP
- Japan
- Prior art keywords
- gas separation
- electrode
- sealing material
- separation plate
- fuel cell
- 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.)
- Expired
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)
Description
【発明の詳細な説明】
この発明は、積層形燃料電池において、ガス分
離板と単電池とのシールを行う製造方法に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a manufacturing method for sealing a gas separation plate and a unit cell in a stacked fuel cell.
従来この種の燃料電池として第1図に示すもの
があつた。図において、1,1′はガス分離板、
2は酸化剤電極のシール用ガスケツト、3は酸化
剤電極、4は電解質マトリツクス、5は燃料電極
で、酸化剤電極3、電解質マトリツクス4、燃料
電極5で単電池を構成する。6は燃料電極のシー
ル用ガスケツトである。第1図の1〜6の単位体
を積層したものが第2であり、7は絶縁板、8は
集電板、9は単位体を複数個積層した積層体、1
0は酸化剤としての空気、11は燃料である。 A conventional fuel cell of this type is shown in FIG. In the figure, 1 and 1' are gas separation plates,
2 is a gasket for sealing the oxidizer electrode, 3 is the oxidizer electrode, 4 is the electrolyte matrix, and 5 is the fuel electrode. The oxidizer electrode 3, the electrolyte matrix 4, and the fuel electrode 5 constitute a single cell. 6 is a gasket for sealing the fuel electrode. The second one is a stack of unit bodies 1 to 6 in FIG.
0 is air as an oxidizing agent, and 11 is fuel.
次に動作について説明する。ガス分離板1,
1′の間に電極、ガスケツトおよび電解質マトリ
ツクスを第1図の順で積層する。即ち、酸化剤電
極3の窓枠状ガスケツト2の内側に酸化剤電極3
をはめこみ、これに電解質マトリツクス4を重
ね、さらに燃料電極5の窓枠状ガスケツト6の内
側に燃料電極5をはめこんだものを重ねる。この
要領を繰り返し、複数個の単位体を第2図のよう
に積層し、積層形燃料電池を組み立てる。組み立
て後、空気10および燃料11を供給し集電板8
から出力を取り出し積層電池を運転する。 Next, the operation will be explained. gas separation plate 1,
1', electrodes, gaskets and electrolyte matrix are stacked in the order shown in FIG. That is, the oxidizer electrode 3 is placed inside the window frame-shaped gasket 2 of the oxidizer electrode 3.
The electrolyte matrix 4 is placed on top of the electrolyte matrix 4, and the fuel electrode 5 fitted inside the window frame-shaped gasket 6 of the fuel electrode 5 is placed on top of the electrolyte matrix 4. This process is repeated to stack a plurality of unit bodies as shown in FIG. 2 to assemble a stacked fuel cell. After assembly, air 10 and fuel 11 are supplied to the current collector plate 8.
The output is extracted from the battery and the stacked battery is operated.
従来の積層形燃料電池は以上のように構成され
ているので、ガス分離板と単電池間のガスおよび
液のシールを行うためには、両電極とそれぞれの
ガスケツトの厚みを積層した状態で等しい厚さに
しなければならず、電極とガスケツトの材料定数
をもとに厚みの設計を行なわなければならなかつ
た。また、ガスケツトとして、かなり弾性を求め
られるため、フツ素ゴム系の材料を用いている
が、高温下のリン酸電解質を用いる電池などでは
劣化が激しく長期のシール性を保つことはむずか
しいなどの欠点があつた。 Conventional stacked fuel cells are constructed as described above, so in order to seal the gas and liquid between the gas separation plate and the cell, the thickness of both electrodes and their respective gaskets must be equal in the stacked state. The thickness had to be designed based on the material constants of the electrodes and gasket. In addition, as gaskets require considerable elasticity, fluoro rubber materials are used, but they have drawbacks such as severe deterioration in batteries that use phosphoric acid electrolytes at high temperatures, making it difficult to maintain long-term sealing performance. It was hot.
この発明は上記のような従来のものの欠点を除
去するためになされたもので、それぞれのガスケ
ツトに当たるものを、FEP(4フツ化エチレン―
6フツカプロピレン共重合体)あるいはPFA(パ
ーフロロアルキルビニルエーテル共重合体)のよ
うな高温リン酸に耐えかつ溶融成型可能な材料を
用い、ガス分離板と単電池間のシールを行なう積
層形燃料電池の製造方法を提供することを目的と
している。 This invention was made to eliminate the drawbacks of the conventional gaskets as described above, and each gasket was replaced with FEP (tetrafluoroethylene).
A stacked fuel cell that uses a material that can withstand high-temperature phosphoric acid and can be melt-molded, such as PFA (perfluoroalkyl vinyl ether copolymer) or PFA (perfluoroalkyl vinyl ether copolymer), to create a seal between the gas separation plate and the unit cell. The purpose is to provide a manufacturing method for.
以下、この発明の一実施例を図について説明す
る。第3図において、1および1′はガス分離板、
16および16′は、燃料電極14に対するガス
分離板1および1′におけるシール面、17およ
び17′はリン酸供給溝、18および18′はリン
酸供給孔であり、リン酸供給溝17および17′
と結がつている。11は酸化剤電極12とガス分
離板1間のシール材であり、12は酸化剤電極で
ある。13は電解質マトリツクス、14は燃料電
極、15は燃料電極14とガス分離板1′間のシ
ール材で中空かつ帯状のもので19はこの中空部
である。 An embodiment of the present invention will be described below with reference to the drawings. In Fig. 3, 1 and 1' are gas separation plates;
16 and 16' are sealing surfaces of the gas separation plates 1 and 1' for the fuel electrode 14, 17 and 17' are phosphoric acid supply grooves, and 18 and 18' are phosphoric acid supply holes; ′
It is connected with. 11 is a sealing material between the oxidizing agent electrode 12 and the gas separation plate 1, and 12 is the oxidizing agent electrode. 13 is an electrolyte matrix, 14 is a fuel electrode, 15 is a hollow band-shaped sealing material between the fuel electrode 14 and the gas separation plate 1', and 19 is this hollow portion.
次に動作について説明する。まず、ガス分離板
1′のシール面16′に燃料側シール材15を載
せ、シール材15と15の内側間に燃料電極14
を配置し、換言すれば燃料電極14の両側面にシ
ール材15と15をそれぞれ沿わせ、ガス分離板
1′上に載せる。このとき、燃料電極14はガス
分離板の燃料流路用溝の凸部に接するようにする
と同時にガス分離板1′のリン酸供給溝17′とシ
ール材15の中空部19が一致するようにする。
次に電解質マトリツクス13を載せさらに酸化剤
電極12と、それに沿わせたシール材11を積層
し、上からガス分離板1を載せ単位体を構成す
る。この後、さらに上記の操作をくり返し第2図
のごとく複数個の単位体からなる積層形燃料電池
を組み立てる。上記のシール材はPFAあるいは
FEPのような高温下でのリン酸に耐え、PTFE
(4フツ化エチレン重合体)と違がつて溶融成型
できる材料から構成する必要がある。またこのと
きのシール材としては厚さが各電極の厚みよりも
幾分厚くなるように粉末を成型したものである。 Next, the operation will be explained. First, the fuel-side sealing material 15 is placed on the sealing surface 16' of the gas separation plate 1', and the fuel electrode 14 is placed between the inner sides of the sealing materials 15 and 15.
In other words, the sealing materials 15 and 15 are placed along both sides of the fuel electrode 14, respectively, and placed on the gas separation plate 1'. At this time, the fuel electrode 14 is brought into contact with the convex part of the fuel flow groove of the gas separation plate, and at the same time, the phosphoric acid supply groove 17' of the gas separation plate 1' is made to coincide with the hollow part 19 of the sealing material 15. do.
Next, the electrolyte matrix 13 is placed, and the oxidizer electrode 12 and the sealing material 11 are laminated along it, and the gas separation plate 1 is placed on top to form a unit. Thereafter, the above operations are repeated to assemble a stacked fuel cell consisting of a plurality of units as shown in FIG. The above sealing material is PFA or
Resistant to phosphoric acid under high temperature like FEP, PTFE
Unlike (tetrafluoroethylene polymer), it must be made of a material that can be melt-molded. Further, the sealing material at this time is made of powder molded so that its thickness is somewhat thicker than the thickness of each electrode.
さて、組立てられた積層形燃料電池を押圧板等
で積層方向に圧力を加える。このときの圧力とし
ては電池動作時同様1〜5Kg/cm2の範囲が望まし
い。この後ち、電池自身を不活性ガス雰囲気の中
へ入れるか、燃料11および空気12の代わりに
不活性ガスを流すかいずれにしろ電極を不活性ガ
ス雰囲気にした上で、シール材を融着すべく熱処
理する。熱処理はPFA,FEPの場合ともにそれ
ぞれの融点付近(融点±50℃)で行なうのがよ
い。これは融点より温度が高くなればなるほどシ
ール材が一部分解し、シール性を発揮できず、融
点よりかなり低い温度で熱処理した場合融着が完
全に進まず、シール材としての機械的強度も弱
く、かつシール性も劣つたものになるからであ
る。 Now, pressure is applied to the assembled stacked fuel cell using a pressing plate or the like in the stacking direction. The pressure at this time is preferably in the range of 1 to 5 kg/cm 2 as in the case of battery operation. After this, either the battery itself is placed in an inert gas atmosphere, or an inert gas is flowed in place of the fuel 11 and air 12, the electrodes are placed in an inert gas atmosphere and the sealing material is fused. Heat treat as much as possible. For both PFA and FEP, heat treatment should be carried out near their respective melting points (melting point ±50°C). This is because the higher the temperature is than the melting point, the more the sealing material partially decomposes and cannot exhibit its sealing properties, and when heat treated at a temperature much lower than the melting point, the fusion does not progress completely and the mechanical strength of the sealing material is weak. , and the sealing performance is also poor.
熱処理の際、同時に積層方向に圧力がかかつて
いるためシール材は初め電極より厚みが幾分大で
あつたものが、電極と等しい厚みになる。この状
態から電池の動作温度まで積層電池の温度を下
げ、リン酸はリン酸補給孔から燃料電池のシール
材中空部19を通つて電解質マトリツクス13に
到達し電解質全体を湿潤状態にする。 During the heat treatment, pressure is simultaneously applied in the stacking direction, so the sealing material, which was initially somewhat thicker than the electrodes, becomes as thick as the electrodes. From this state, the temperature of the stacked battery is lowered to the operating temperature of the battery, and phosphoric acid reaches the electrolyte matrix 13 from the phosphoric acid supply hole through the sealing material hollow part 19 of the fuel cell, making the entire electrolyte wet.
以上の操作ののちに積層形燃料電池を運転し、
出力を取り出す。 After the above operations, operate the stacked fuel cell,
Get the output.
なお、上記実施例ではシール材11および15
に粉末成型したものについて説明したが、溶融成
型したシール材であつてもよく上記実施例と同様
の効果を奏する。 In addition, in the above embodiment, the sealing materials 11 and 15
Although the sealing material has been described as being powder-molded, it may also be a sealing material that is melt-molded and the same effects as in the above embodiments can be obtained.
また、上記実施例では燃料電極および酸化剤電
極のシール材の形状を第3図のようにしたが電極
およびガス分離板の形状に応じた他の形状であつ
てもよく、上記実施例と同様の効果を奏する。 Further, in the above embodiment, the shape of the sealing material of the fuel electrode and the oxidizer electrode was as shown in FIG. It has the effect of
以上のように、この発明によれば電極の厚さよ
り厚く高温下のリン酸に耐え、熱で溶融可能な材
料からなるシール材を上記電極側面に沿わせ電解
質マトリツクスとガス分離板との間に配置し、単
電池と上記ガス分離板の積層方向に圧力を加えな
がら熱処理して、上記シール材が上記電解質マト
リツクスと上記ガス分離板に融着するようにした
ので、シール材の融着前の厚さを厳密に調整しな
くても、シール材が電極と同じ厚さになるように
融着され、電解質マトリツクスとガス分離板が一
体化され、かつ高い信頼性をもつシールが得られ
る効果がある。 As described above, according to the present invention, a sealing material made of a material that is thicker than the thickness of the electrode and is resistant to phosphoric acid at high temperatures and can be melted by heat is placed along the side surface of the electrode between the electrolyte matrix and the gas separation plate. The cells were placed and heat treated while applying pressure in the laminated direction of the cell and the gas separation plate so that the sealant was fused to the electrolyte matrix and the gas separation plate. Even without strictly adjusting the thickness, the sealing material is fused to the same thickness as the electrode, the electrolyte matrix and gas separation plate are integrated, and a highly reliable seal can be obtained. be.
第1図は従来の燃料電極の単位体の構成を分解
して示す斜視図、第2図は従来の積層形燃料電池
の斜視図、第3図はこの発明の一実施例による単
位体の構成を分解して示す斜視図である。
図中11,15はシール材である。なお、図
中、同一符号は同一、又は相当部分を示す。
FIG. 1 is an exploded perspective view showing the structure of a conventional fuel electrode unit, FIG. 2 is a perspective view of a conventional stacked fuel cell, and FIG. 3 is a structure of a unit according to an embodiment of the present invention. FIG. 2 is an exploded perspective view. In the figure, 11 and 15 are sealing materials. In addition, in the figures, the same reference numerals indicate the same or equivalent parts.
Claims (1)
電極とを有する単電池及びガス分離板を複数個積
層する積層形燃料電池の製造方法において、上記
電極の厚さより厚く、高温下のリン酸に耐え、熱
で溶融可能な材料からなるシール材を上記電極側
面に沿わせ上記電解質マトリツクスと上記ガス分
離板との間に配置し、上記単電池と上記ガス分離
板の積層方向に圧力を加えながら熱処理して、上
記シール材が上記電解質マトリツクスと上記ガス
分離板に融着するようにした積層形燃料電池の製
造方法。 2 シール材として4フツ化エチレン―6フツカ
プロピレン共重合体及びパーフロロアルキルビニ
ルエーテル共重合体のいずれか一方を使用するこ
とを特徴とする特許請求の範囲第1項記載の積層
形燃料電池の製造方法。[Scope of Claims] 1. A method for manufacturing a stacked fuel cell in which a plurality of unit cells and gas separation plates each having a fuel electrode, an electrolyte matrix, and an oxidizer electrode are stacked, the fuel cell being thicker than the thickness of the electrodes and under high temperature conditions. A sealing material made of a material that can withstand phosphoric acid and can be melted by heat is placed along the side surface of the electrode between the electrolyte matrix and the gas separation plate, and in the stacking direction of the cell and the gas separation plate. A method for manufacturing a stacked fuel cell, wherein the sealing material is fused to the electrolyte matrix and the gas separation plate by heat treatment while applying pressure. 2. Production of a stacked fuel cell according to claim 1, wherein either one of a tetrafluoroethylene-hexafluoropropylene copolymer and a perfluoroalkyl vinyl ether copolymer is used as a sealing material. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57039912A JPS58157063A (en) | 1982-03-12 | 1982-03-12 | Sealing of layer-built fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57039912A JPS58157063A (en) | 1982-03-12 | 1982-03-12 | Sealing of layer-built fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58157063A JPS58157063A (en) | 1983-09-19 |
| JPS6322422B2 true JPS6322422B2 (en) | 1988-05-11 |
Family
ID=12566152
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57039912A Granted JPS58157063A (en) | 1982-03-12 | 1982-03-12 | Sealing of layer-built fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58157063A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59207563A (en) * | 1983-05-11 | 1984-11-24 | Hitachi Ltd | Fuel cell |
| US4514475A (en) * | 1984-03-30 | 1985-04-30 | The United States Of America As Represented By The United States Department Of Energy | Fuel cell separator with compressible sealing flanges |
| US4588661A (en) * | 1984-08-27 | 1986-05-13 | Engelhard Corporation | Fabrication of gas impervious edge seal for a bipolar gas distribution assembly for use in a fuel cell |
| JPH01151161A (en) * | 1987-12-08 | 1989-06-13 | Mitsubishi Electric Corp | Fuel cell |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA1129946A (en) * | 1977-10-14 | 1982-08-17 | Joannes J.P. Leyen | Method for the manufacture of an electrochemical cell or battery |
-
1982
- 1982-03-12 JP JP57039912A patent/JPS58157063A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58157063A (en) | 1983-09-19 |
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