JPS6240827B2 - - Google Patents
Info
- Publication number
- JPS6240827B2 JPS6240827B2 JP56119609A JP11960981A JPS6240827B2 JP S6240827 B2 JPS6240827 B2 JP S6240827B2 JP 56119609 A JP56119609 A JP 56119609A JP 11960981 A JP11960981 A JP 11960981A JP S6240827 B2 JPS6240827 B2 JP S6240827B2
- Authority
- JP
- Japan
- Prior art keywords
- fuel
- electrode
- oxidizer
- chamber
- 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
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
-
- 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
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/2465—Details of groupings of fuel cells
-
- 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
- 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】
本発明は気体燃料又は液体燃料を用いる燃料電
池において、相隣り合う単電池を電気的に効率良
く接続するようにした燃料電池に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fuel cell using gaseous fuel or liquid fuel, in which adjacent unit cells are electrically and efficiently connected.
一般に燃料電池は燃料極に燃料を、酸化剤極に
酸化剤を供給する限り連続的に発電することがで
きる一種の直流発電機と言われている。燃料のも
つ化学エネルギーを直接電気エネルギーに変換す
る燃料電池は、燃料極、酸化剤極、燃料室、酸化
剤室、電解液室からなる単電池を所定の電気出力
が得られるように多数積層して構成されている。
しかしながら、これら単電池を電気的に接続する
過程で電気的損失が生じ、余分な熱の発生による
電池温度の上昇、発電効率の低下をもたらすとい
う欠点があつた。すなわち、従来、電極から集電
するために電極の周囲に金属製の出力端子を溶接
し、その一部を燃料室又は酸化剤室を形成するセ
パレータの外側に露出させ、それらを外部で接続
していた。このため、相隣り合う単電池を電気的
に接続する出力端子が長くなるために、この部分
での損失が無視できない。しかも、電極面積が大
きくなる程、損失が大きくなる。本発明はこれら
欠点を解決するために、相隣り合う単電池を短か
い距離で電気的に接続する構造を提供するもので
ある。 In general, a fuel cell is said to be a type of DC generator that can continuously generate electricity as long as fuel is supplied to the fuel electrode and oxidizer is supplied to the oxidizer electrode. Fuel cells, which directly convert the chemical energy of fuel into electrical energy, consist of a fuel electrode, an oxidizer electrode, a fuel chamber, an oxidizer chamber, and an electrolyte chamber, and are stacked in large numbers to obtain a specified electrical output. It is composed of
However, electrical loss occurs in the process of electrically connecting these single cells, which has the drawback of causing excess heat to be generated, resulting in an increase in battery temperature and a decrease in power generation efficiency. That is, conventionally, a metal output terminal is welded around the electrode in order to collect current from the electrode, a part of which is exposed outside the separator that forms the fuel chamber or oxidizer chamber, and these are connected externally. was. For this reason, the output terminal that electrically connects adjacent single cells becomes longer, and the loss in this portion cannot be ignored. Moreover, the larger the electrode area, the larger the loss. In order to solve these drawbacks, the present invention provides a structure in which adjacent unit cells are electrically connected over a short distance.
以下、本発明の一実施例について従来の燃料電
池と比べながら説明する。第1図は電極1の周囲
に出力端子2を溶接した従来電極である。第2図
は燃料電極4、酸化剤極5、燃料室9、酸化剤室
10、電解液室6からなる従来の接続構造をもつ
単電池を積層した燃料電池である。7は燃料室9
を形成する燃料室セパレータであり、8は酸化剤
室10を形成する酸化剤室セパレータである。こ
れら単電池は接続端子3を介して電気的に接続さ
れている。 Hereinafter, one embodiment of the present invention will be described in comparison with a conventional fuel cell. FIG. 1 shows a conventional electrode in which an output terminal 2 is welded around an electrode 1. FIG. 2 shows a fuel cell in which unit cells having a conventional connection structure consisting of a fuel electrode 4, an oxidizer electrode 5, a fuel chamber 9, an oxidizer chamber 10, and an electrolyte chamber 6 are stacked. 7 is the fuel chamber 9
8 is a fuel chamber separator forming an oxidizer chamber 10, and 8 is an oxidizer chamber separator forming an oxidizer chamber 10. These cells are electrically connected via connection terminals 3.
従来の燃料電池はこのような構造であるために
前述のような欠点があつた。 Since conventional fuel cells have such a structure, they have the above-mentioned drawbacks.
これに対して、第3図は電極を複数個の小面積
にこれらが電気的導通状態で分割配置し、それら
に導電性弾性材料を密着させて、相隣り合う単電
池を電気的に接続する構造の本発明の一実施例に
おける燃料電池を示すもので、各電極である燃料
極4′、酸化剤極5′は縦方向に4分割されて燃料
極の小面積4′a、酸化剤極の小面積5a′を構成
し、分離帯の燃料、酸化剤各室9,10側には電
極の基体であるニツケル金網のような集電材11
が露出しており、この集電材11が電極を分割し
た複数個の小面積を電気的に接続しており、その
反対の電解液室6側には絶縁枠12で電解液を遮
断している。各室9,10を構成するセパレータ
14には導電性弾性材料13がついており、その
先端は燃料極4′、酸化剤極5′のそれぞれの小面
積の集電材11に密着している。第4図は600cm2
電極面積をもつ単電池で、従来の燃料電池と銀を
添加したシリコン弾性材料を導電性弾性材料13
に用いた本発明の一実施例における燃料電池との
特性比較を示したもので、燃料に水素、酸化剤に
酸素を用いた電池で、電流密度100mA/cm2で約
50mVの性能向上が得られた。また、従来問題と
されていた熱の発生も十分に抑制することができ
た。 On the other hand, in Fig. 3, electrodes are arranged in multiple small areas in electrical continuity, and a conductive elastic material is attached to the electrodes to electrically connect adjacent cells. This figure shows a fuel cell according to an embodiment of the present invention, in which each electrode, a fuel electrode 4' and an oxidizer electrode 5', is divided into four in the vertical direction, with a small area 4'a of the fuel electrode, a small area 4'a of the fuel electrode, and a small area 4'a of the oxidizer electrode. A current collecting material 11 such as a nickel wire mesh, which is the base of the electrode, is placed on the fuel and oxidizer chambers 9 and 10 side of the separation zone.
is exposed, and this current collector 11 electrically connects a plurality of small areas obtained by dividing the electrode, and on the opposite side of the electrolyte chamber 6, an insulating frame 12 blocks the electrolyte. . A conductive elastic material 13 is attached to the separator 14 constituting each of the chambers 9 and 10, and its tip is in close contact with a small-area current collector 11 of each of the fuel electrode 4' and the oxidizer electrode 5'. Figure 4 is 600cm 2
A single cell with an electrode area, a conventional fuel cell and a silicon elastic material doped with silver are combined with a conductive elastic material 13
This figure shows a comparison of the characteristics with a fuel cell according to an embodiment of the present invention used in a battery using hydrogen as a fuel and oxygen as an oxidizing agent.
A performance improvement of 50 mV was obtained. Furthermore, the generation of heat, which had been a problem in the past, could be sufficiently suppressed.
以上のように、本発明により発電効率が向上
し、余分な熱の発生を抑制できるという利点があ
ることから、その工業的価値は大きい。 As described above, the present invention has the advantage of improving power generation efficiency and suppressing generation of excess heat, and therefore has great industrial value.
第1図は従来電極の正面図、第2図は従来の燃
料電池の概略説明図、第3図は本発明の一実施例
を示す燃料電池の概略説明図、第4図は従来の燃
料電池と本発明の燃料電池との特性比較曲線図で
ある。
1は電極、4′は燃料極、4′aは燃料極の小面
積、5′は酸化剤極、5′aは酸化剤極の小面積、
13は導電性弾性材料、14はセパレータ。
Fig. 1 is a front view of a conventional electrode, Fig. 2 is a schematic explanatory diagram of a conventional fuel cell, Fig. 3 is a schematic explanatory diagram of a fuel cell showing an embodiment of the present invention, and Fig. 4 is a conventional fuel cell. FIG. 3 is a characteristic comparison curve diagram between the fuel cell of the present invention and the fuel cell of the present invention. 1 is an electrode, 4' is a fuel electrode, 4'a is a small area of the fuel electrode, 5' is an oxidizer electrode, 5'a is a small area of an oxidizer electrode,
13 is a conductive elastic material, and 14 is a separator.
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、前記酸化剤極の酸化剤室側の面と燃料極の燃
料室側の面の一部に、それぞれ対向して集電材を
露出させ、該集電材間に前記セパレータを貫通し
て導電性弾性材料を密着配置させたことを特徴と
する燃料電池。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 constructed by combining an oxidizer chamber that supplies an oxidizer to the oxidizer electrode and a fuel chamber that supplies fuel to the fuel electrode. In a fuel cell in which a large number of fuel cells are stacked with separators formed facing each other on both sides, a current collecting material is provided on a part of the oxidizer chamber side surface of the oxidizer electrode and a part of the fuel chamber side surface of the fuel electrode, respectively. A fuel cell characterized in that a conductive elastic material is closely disposed between the current collectors by penetrating the separator and exposing the current collectors.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56119609A JPS5819872A (en) | 1981-07-30 | 1981-07-30 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56119609A JPS5819872A (en) | 1981-07-30 | 1981-07-30 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5819872A JPS5819872A (en) | 1983-02-05 |
| JPS6240827B2 true JPS6240827B2 (en) | 1987-08-31 |
Family
ID=14765642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56119609A Granted JPS5819872A (en) | 1981-07-30 | 1981-07-30 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5819872A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4580650A (en) * | 1983-07-28 | 1986-04-08 | Nissan Motor Co., Ltd. | Industrial truck |
| JPH0628781Y2 (en) * | 1986-10-31 | 1994-08-03 | 新神戸電機株式会社 | Liquid fuel cell |
-
1981
- 1981-07-30 JP JP56119609A patent/JPS5819872A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5819872A (en) | 1983-02-05 |
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