JPS6240826B2 - - Google Patents
Info
- Publication number
- JPS6240826B2 JPS6240826B2 JP56118812A JP11881281A JPS6240826B2 JP S6240826 B2 JPS6240826 B2 JP S6240826B2 JP 56118812 A JP56118812 A JP 56118812A JP 11881281 A JP11881281 A JP 11881281A JP S6240826 B2 JPS6240826 B2 JP S6240826B2
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- electrode
- oxidizer
- electrical connection
- separator
- 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
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0204—Non-porous and characterised by the material
- H01M8/0223—Composites
- H01M8/0228—Composites in the form of layered or coated products
-
- 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
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
- H01M8/0256—Vias, i.e. connectors passing through the separator material
-
- 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
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Fuel Cell (AREA)
Description
【発明の詳細な説明】
本発明は、単電池を多数個積層した積層構造の
燃料電池において、相隣り合う単電池の燃料極と
酸化剤極を、または燃料極、酸化剤極同志を接続
し、かつ燃料極及び酸化剤極から効率良く電気を
取り出す構造に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fuel cell having a stacked structure in which a large number of unit cells are stacked, and which connects the fuel electrodes and oxidizer electrodes of adjacent unit cells, or the fuel electrodes and oxidizer electrodes of adjacent unit cells. , and relates to a structure for efficiently extracting electricity from a fuel electrode and an oxidizer electrode.
燃料電池は燃料極に燃料を、酸化剤極に酸化剤
を供給することにより、連続的に発電することが
できる一種の直流発電機である。発電部を構成す
る単電池は燃料極、酸化剤極、電解液室、燃料
室、酸化剤室からなり、電気出力に応じてこれら
を直列又は並列に接続する。燃料電池は発電する
際に各種分極現象によつて電気的損失が生じる
が、これらとは別に各電極から外部へ電気を取り
出す際又は相隣り合う単電池の電極を接続する際
にも電気的損失が生じる。これらは全て熱に変換
されて蓄積すると積層電池の温度を上昇させるこ
とになり、電極やセパレータ等の熱歪みの原因と
なる。分極現象による損失は触媒の活性能力の低
下、燃料や酸化剤の供給不足、イオン伝導性を妨
げる要因等に起因するもので、触媒の開発や電極
内部構造の改良によつて大きな反応界面を得るよ
うな電極の開発努力がなされている。 A fuel cell is a type of DC generator that can continuously generate electricity by supplying fuel to a fuel electrode and an oxidant to an oxidizer electrode. The unit cell that constitutes the power generation section consists of a fuel electrode, an oxidizer electrode, an electrolyte chamber, a fuel chamber, and an oxidizer chamber, which are connected in series or in parallel depending on the electrical output. When fuel cells generate electricity, electrical losses occur due to various polarization phenomena, but apart from these, electrical losses also occur when extracting electricity from each electrode to the outside or when connecting the electrodes of adjacent cells. occurs. When all of these are converted into heat and accumulated, the temperature of the stacked battery increases, causing thermal distortion of the electrodes, separators, etc. Loss due to polarization phenomenon is caused by a decrease in the active ability of the catalyst, insufficient supply of fuel and oxidizer, factors that impede ionic conductivity, etc.A large reaction interface can be obtained by developing catalysts and improving the internal structure of electrodes. Efforts are being made to develop such electrodes.
一方、各電極から電気を取り出す際、又は相隣
り合う単電池の電極を接続する際の電気損失は、
純然たる電気抵抗に起因するものであり、これを
非常に小さくすることも熱効率の向上、小型軽量
化にとつて重要である。 On the other hand, the electrical loss when extracting electricity from each electrode or when connecting the electrodes of adjacent cells is
This is caused by pure electrical resistance, and making this extremely small is also important for improving thermal efficiency and reducing size and weight.
本発明は、かかる純然たる電気抵抗に起因する
損失の問題を解決するセパレータに関するもの
で、以下本発明の一実施例について従来の燃料電
池と対比しながら説明する。 The present invention relates to a separator that solves the problem of loss caused by pure electrical resistance, and one embodiment of the present invention will be described below in comparison with a conventional fuel cell.
第1図は各電極の周囲に集電用金属製端子を取
り付け、それらを積層電池の外部へ取り出して、
相隣り合う単電池の電極を接続する従来の電気接
続構造を持つ電池を示したものである。単電池は
前述したように酸化剤極1、燃料極2、電解液室
3、酸化剤室5及び燃料室6から構成されてお
り、これら単電池は両面に対向して酸化剤室5と
燃料室6を形成するセパレータ4を介して積層さ
れている。各電極1,2には集電用の電気接続端
子9を溶接し、これらを積層電池外部に取り出し
て相隣り合う単電池を電気的に接続している。第
2図は第1図に示す酸化剤極1の全周囲に、第3
図は同じく第1図に示す酸化剤極1の一辺に電気
接続端子9を溶接して取り付けたものである。こ
のような従来の燃料電池において、第2図の電極
構造のものでは電極中央部で、第3図の電極構造
のものでは電極下部で発電した電気は電気接続端
子9に到達するまでに、その間の抵抗によつて熱
に変換されるために、電極やセパレータ等の熱歪
みの原因となつた。これに対して、第4図は電気
接続片10を有し、かつ、酸化剤室、燃料室を形
成した表面を電気伝導性材11で被覆したセパレ
ータ4aを介して単電池を積層した本発明の一実
施例における燃料電池を示すもので、単電池積層
状態において酸化剤極1と燃料極2との電極面同
志が電気接続片10を介して接触接続状態となつ
ている。単電池の構成は第1図と同じであるが、
セパレータ4aには電気接続片10が固定されて
おり、さらにその酸化剤室、燃料室を形成した表
面には電気伝導性材11で被覆されて、電池接続
片10と電気伝導性材11は接続状態になつてい
る。なお、第1図、4図において、7は電解液供
給通路、8は電解液排出通路である。第5図は第
4図において有効寸法200mm×300mmを持つ電極の
ためのセパレータ4aを示すもので、15個の電気
接続片10が固定され、さらに0.1mm厚さニツケ
ル板で被覆されている。電気接続片10の数及び
電気伝導性材11の厚さは電極面積の大きさや電
流密度によつても自由に選ぶことができる。第6
図は、従来の接続構造を持つ600cm2電極の電池と
本発明の電気接続片10を15個固定し電気伝導材
11で被覆したセパレータ4aを用いた水素一酸
素燃料電池の電流密度−平均単電池電圧特性であ
る。いづれも、単電池を6個積層した積層電池の
燃料電池の性能を示してある。電気接続片10の
材質としてニツケルを用いたが、銀を添加したシ
リコンゴム等の弾性材料を用いてもほとんど同程
度の性能を得ることができた。本発明の電気接続
片10を有し電気伝導材11で被覆したセパレー
タ4aを用いることにより、電流密度100mA/
cm2では約32mv、200mA/cm2では約50mv単電
池電圧が向上している。また従来問題とされた電
極やセパレータ等の熱歪みも生じなくなつた。な
お電気伝導性材11や電気接続片10の材質を選
ぶことにより、アルカリ電解液を用いる水素−酸
素型のみならず、ヒドラジン空気型のような液体
燃料電池や酸性電解液を用いる水素−空気型等の
燃料電池にも適用できる。 Figure 1 shows that metal terminals for current collection are attached around each electrode, and these terminals are taken out to the outside of the stacked battery.
This figure shows a battery with a conventional electrical connection structure that connects the electrodes of adjacent single cells. As mentioned above, each cell is composed of an oxidizer electrode 1, a fuel electrode 2, an electrolyte chamber 3, an oxidizer chamber 5, and a fuel chamber 6. They are laminated with a separator 4 interposed therebetween to form a chamber 6. Electrical connection terminals 9 for current collection are welded to each electrode 1, 2, and these are taken out to the outside of the stacked battery to electrically connect adjacent unit cells. Figure 2 shows that a third electrode is placed around the oxidizer electrode 1 shown in Figure 1.
The figure shows an electrical connection terminal 9 welded and attached to one side of the oxidizer electrode 1 shown in FIG. 1 as well. In such conventional fuel cells, electricity generated at the center of the electrode in the case of the electrode structure shown in FIG. 2 and at the bottom of the electrode in the case of the electrode structure shown in FIG. This caused thermal distortion of electrodes, separators, etc., as it was converted into heat by the resistance of the metal. In contrast, FIG. 4 shows the present invention in which single cells are stacked via a separator 4a having an electrical connection piece 10 and whose surface forming an oxidizer chamber and a fuel chamber is coated with an electrically conductive material 11. This shows a fuel cell in one embodiment, in which the electrode surfaces of an oxidizer electrode 1 and a fuel electrode 2 are in contact with each other via an electrical connection piece 10 in a stacked state of the single cells. The configuration of the cell is the same as in Figure 1, but
An electrical connection piece 10 is fixed to the separator 4a, and the surface forming the oxidizer chamber and fuel chamber is coated with an electrically conductive material 11, and the battery connection piece 10 and the electrically conductive material 11 are connected. It is becoming a state. In addition, in FIGS. 1 and 4, 7 is an electrolyte supply passage, and 8 is an electrolyte discharge passage. FIG. 5 shows the separator 4a for the electrodes in FIG. 4 having effective dimensions of 200 mm x 300 mm, to which 15 electrical connection pieces 10 are fixed and further covered with a 0.1 mm thick nickel plate. The number of electrical connection pieces 10 and the thickness of electrically conductive material 11 can be freely selected depending on the size of the electrode area and current density. 6th
The figure shows the current density-average unit current density of a hydrogen-oxygen fuel cell using a 600 cm 2- electrode battery with a conventional connection structure and a separator 4a with 15 electrical connection pieces 10 of the present invention fixed and covered with an electrically conductive material 11. This is the battery voltage characteristic. In each case, the performance of a fuel cell made of a stacked battery consisting of six single cells stacked is shown. Although nickel was used as the material for the electrical connection piece 10, almost the same performance could be obtained using an elastic material such as silicone rubber doped with silver. By using the separator 4a having the electrical connection piece 10 of the present invention and covered with the electrically conductive material 11, a current density of 100 mA/
The cell voltage has improved by about 32 mV at cm 2 and about 50 mV at 200 mA/cm 2 . Furthermore, thermal distortion of electrodes, separators, etc., which was a problem in the past, no longer occurs. By selecting the materials of the electrically conductive material 11 and the electrical connection piece 10, you can choose not only the hydrogen-oxygen type using an alkaline electrolyte, but also the hydrogen-air type using a liquid fuel cell such as a hydrazine-air type or an acidic electrolyte. It can also be applied to fuel cells such as
以上のように本発明によれば、従来問題とされ
た電気抵抗に起因する熱損失の問題点も解消され
ると共に電池性能が向上し、小形軽量の燃料電池
が得られ、また製作や組立ても容易にできる利点
を持つているので、その工業的価値は大である。 As described above, according to the present invention, the conventional problem of heat loss caused by electrical resistance is solved, the battery performance is improved, a small and lightweight fuel cell is obtained, and the manufacturing and assembly are easy. Since it has the advantage of being easily produced, its industrial value is great.
第1図は従来の電気接続構造をもつ燃料電池の
概略説明図、第2図は第1図に用いた酸化剤極の
全周に電気接続端子を溶接した正面図、第3図は
第1図に用いた酸化剤極の一辺に電気接続端子を
溶接した正面図、第4図は本発明の一実施例を示
す電気接続片を有し、さらに電気伝導性材で被覆
したセパレータを介して単電池を積層した燃料電
池の概略説明図、第5図は本実施例における15個
の電気接続片が固定され、さらに電気伝導性材で
被覆したセパレータ正面図、第6図は従来の燃料
電池と本発明の一実施例を示す燃料電池との電流
密度−平均単電池電圧特性の比較曲線図である。
1は酸化剤極、2は燃料極、4aはセパレー
タ、5は酸化剤室、6は燃料室、10は電気接続
片、11は電気伝導性材。
Figure 1 is a schematic explanatory diagram of a fuel cell with a conventional electrical connection structure, Figure 2 is a front view of the oxidizer electrode used in Figure 1 with electrical connection terminals welded around the entire circumference, and Figure 3 is the FIG. 4 is a front view showing an electrical connection terminal welded to one side of the oxidizing agent electrode used in the figure. A schematic explanatory diagram of a fuel cell in which unit cells are stacked. Figure 5 is a front view of a separator in which 15 electrical connection pieces in this embodiment are fixed and is further covered with an electrically conductive material. Figure 6 is a diagram of a conventional fuel cell. FIG. 4 is a comparison curve diagram of current density-average cell voltage characteristics between the fuel cell shown in FIG. 1 is an oxidizer electrode, 2 is a fuel electrode, 4a is a separator, 5 is an oxidizer chamber, 6 is a fuel chamber, 10 is an electrical connection piece, and 11 is an electrically conductive material.
Claims (1)
間に位置する電解液とを有する単電池を、酸化剤
極に酸化剤を供給する酸化剤室と燃料極に燃料を
供給する燃料室とを両面に対向して形成したセパ
レータを介して多数個積層した燃料電池におい
て、セパレータに酸化剤極と燃料極を該両電極面
同志を電気的に接続するための電気接続片を設
け、かつセパレータの酸化剤室、燃料室を形成し
た表面を電気伝導性材で、電気接続片と接続状態
となるように被覆したことを特徴とする燃料電
池。 2 電気接続片及びセパレータを被覆する材料が
金属製材料からなることを特徴とする特許請求範
囲第1項記載の燃料電池。 3 電気接続片及びセパレータを被覆する材料が
導電性樹脂、又は導電性弾性材料からなることを
特徴とする特許請求範囲第1項記載の燃料電池。[Claims] 1. A unit cell having an oxidizer electrode and a fuel electrode arranged opposite to each other and an electrolyte located between the two electrodes is provided with an oxidizer chamber that supplies an oxidizer to the oxidizer electrode and a fuel electrode that supplies fuel to the fuel electrode. An electrical connection piece for electrically connecting an oxidizer electrode and a fuel electrode to the separator in a fuel cell in which a large number of fuel cells are stacked with separators formed with fuel chambers facing each other on both sides. 1. A fuel cell characterized in that the surface of the separator on which the oxidizer chamber and the fuel chamber are formed is coated with an electrically conductive material so as to be connected to an electrical connection piece. 2. The fuel cell according to claim 1, wherein the material covering the electrical connection piece and the separator is made of a metal material. 3. The fuel cell according to claim 1, wherein the material covering the electrical connection piece and the separator is made of a conductive resin or a conductive elastic material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56118812A JPS5819871A (en) | 1981-07-29 | 1981-07-29 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56118812A JPS5819871A (en) | 1981-07-29 | 1981-07-29 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5819871A JPS5819871A (en) | 1983-02-05 |
| JPS6240826B2 true JPS6240826B2 (en) | 1987-08-31 |
Family
ID=14745738
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56118812A Granted JPS5819871A (en) | 1981-07-29 | 1981-07-29 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5819871A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU6069801A (en) * | 2000-06-02 | 2001-12-11 | Sony Corporation | Fuel battery |
| JP5262241B2 (en) * | 2008-03-31 | 2013-08-14 | 三菱マテリアル株式会社 | Solid oxide fuel cell |
-
1981
- 1981-07-29 JP JP56118812A patent/JPS5819871A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5819871A (en) | 1983-02-05 |
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