JPS6041833B2 - Fuel cell - Google Patents
Fuel cellInfo
- Publication number
- JPS6041833B2 JPS6041833B2 JP53073898A JP7389878A JPS6041833B2 JP S6041833 B2 JPS6041833 B2 JP S6041833B2 JP 53073898 A JP53073898 A JP 53073898A JP 7389878 A JP7389878 A JP 7389878A JP S6041833 B2 JPS6041833 B2 JP S6041833B2
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- separation plate
- fuel cell
- gas separation
- gas
- 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
- 239000000446 fuel Substances 0.000 title claims description 12
- 238000000926 separation method Methods 0.000 claims description 24
- 239000006260 foam Substances 0.000 claims description 13
- 238000009792 diffusion process Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 description 30
- 239000011159 matrix material Substances 0.000 description 6
- 239000003792 electrolyte Substances 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Classifications
-
- 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
- Fuel Cell (AREA)
Description
【発明の詳細な説明】
本発明は燃料電池特にマトリックス型酸素、水素燃料
電池に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to fuel cells, particularly matrix oxygen, hydrogen fuel cells.
一般にマトリックス型電池は第1図に示すように異極
性のガス拡散電極1、2の背面に金属又はグラファイト
よりなるガス分離板3を介在させて夫々のガス室を形成
する構造をとつている。In general, a matrix type battery has a structure in which a gas separation plate 3 made of metal or graphite is interposed on the back side of gas diffusion electrodes 1 and 2 of different polarity to form respective gas chambers, as shown in FIG.
またガス分離板3は導電性てあるために単電池を複数個
連結する場合の接続部の働きをし、電解質マトリック4
と電極1、2および電極とガス分離板3とは互に密着す
ることになる。 しかし酸素又は水素などの活物質ガス
はガス分離板3の凹部に流れていて電極に接触している
凸部には流れていない。In addition, since the gas separation plate 3 is conductive, it functions as a connection part when connecting multiple cells, and the electrolyte matrix 4
The electrodes 1 and 2 and the electrodes and the gas separation plate 3 are brought into close contact with each other. However, active material gas such as oxygen or hydrogen flows into the recesses of the gas separation plate 3 and does not flow into the projections that are in contact with the electrodes.
したがつて実際に作用している電極面はガス分離板の凹
部に面した部分だけであつて凸部と接している部分は反
応にあづからない。このことからガス分離板として凹部
の広いものが望ましいが、このような分離板を使用する
と電極を接触する凸部が少ないため電極とマトリックス
間の密着性を損うと共に長期間の使用で電極面に変形を
生じ、電池を維持できなくなる。したがつてガス分離板
の凸部を少くすることができず、この凸部に接する電極
面積は全面積の10〜30%にも達している。このよう
な電極有効面積の減少は電極利用率を低下させて電池特
性に悪い影響をおよぼす。 本発明このような反応にあ
づからない電極面積を極力小さくして電池特性を向上さ
せることを目的とするもので、ガス拡散電極とガス分離
板との間に導電性多孔質発泡体を介在させたことを特徴
とする。Therefore, the electrode surface that actually acts is only the part facing the concave part of the gas separation plate, and the part in contact with the convex part does not participate in the reaction. For this reason, it is desirable to use a gas separation plate with wide recesses; however, when such a separation plate is used, there are few protrusions that make contact with the electrodes, which impairs the adhesion between the electrodes and the matrix, and the electrode surface deteriorates over long periods of use. deformation occurs, making it impossible to maintain the battery. Therefore, it is not possible to reduce the number of convex portions of the gas separation plate, and the electrode area in contact with these convex portions reaches 10 to 30% of the total area. Such a reduction in the effective area of the electrode reduces the electrode utilization rate and adversely affects the battery characteristics. The purpose of the present invention is to improve battery characteristics by minimizing the area of the electrodes that are not exposed to such reactions, and by interposing a conductive porous foam between the gas diffusion electrode and the gas separation plate. It is characterized by having
ここに云う導電性多孔質発泡体は多孔度95〜98%
、孔径0、川〜0.5wnの耐電解液性の金属例えはス
テンレス発泡体である。The conductive porous foam mentioned here has a porosity of 95 to 98%.
An example of an electrolyte-resistant metal with a pore size of 0 and 0.5 wn is stainless steel foam.
以下その実施例を説明するに、第2図は両面に凹凸部
を有するガス分離板3を用いた場合で、この分離板と各
ガス拡散電極1、2との間に前記発泡体よりなる層5、
5が密接介在している。To explain the embodiment below, FIG. 2 shows a case where a gas separation plate 3 having uneven parts on both sides is used, and a layer made of the foamed material is interposed between this separation plate and each gas diffusion electrode 1, 2. 5,
5 are closely intervening.
この場合はガス分離板の凸部に対応する電極面にも発泡
体層5を介してガスが供給されるので、電極の有効作用
面積が増大すると共に、電極全面に発泡体層5が密接し
ているので、電極を確実に保持してその変形を防止する
ことができる。 又第3図の実施例は、凹凸のあるガス
分離板のかわりに金属薄板3″を用いてガスの分離を行
い、このガス分離薄板3″と各電極1,2との間にブロ
ック状の前記発泡体5″,5″を介在させた場合である
。In this case, gas is also supplied to the electrode surface corresponding to the convex portion of the gas separation plate through the foam layer 5, so the effective action area of the electrode increases and the foam layer 5 is brought into close contact with the entire surface of the electrode. Therefore, it is possible to securely hold the electrode and prevent its deformation. In the embodiment shown in FIG. 3, a thin metal plate 3'' is used instead of the uneven gas separation plate to separate gas, and a block-shaped plate is placed between the thin gas separation plate 3'' and each electrode 1, 2. This is the case where the foamed bodies 5'', 5'' are interposed.
この場合は発泡体5″が電極背面空間を満たしてガス室
を構成し、従来のようにガス分離板の溝切り加工は不用
となる。第4図は本発明燃料電池の放電特性で、比較の
ため前記第1図で説明した従来電池の場合を点線で示し
た。In this case, the foam 5'' fills the space behind the electrode to form a gas chamber, and the conventional grooving of the gas separation plate is not required. Figure 4 shows the discharge characteristics of the fuel cell of the present invention for comparison. Therefore, the case of the conventional battery explained in FIG. 1 is shown by a dotted line.
上述の如く本発明はガス拡散電極背面とガス分離板との
間に導電性多孔質の介在させたもので、この発泡体が電
極全面に圧接して電極とマトリックス間の密着性を向上
し、しかも電極を確実に保持してその変形を防止するこ
とが出来ると共に電極全面に反応ガスが供給されて電極
の有効作用面積を増大することができる。As mentioned above, the present invention has a conductive porous material interposed between the back surface of the gas diffusion electrode and the gas separation plate, and this foam is pressed against the entire surface of the electrode to improve the adhesion between the electrode and the matrix. Furthermore, the electrode can be held reliably to prevent its deformation, and the reactive gas can be supplied to the entire surface of the electrode, increasing the effective working area of the electrode.
尚、ガス分離板として両面に凹凸部のあるものを用いた
場合は、層状の発泡体が凸部との間に介在してこの部分
にも反応ガスが行きわたると共に、ガス分離板として薄
板を用いた場合は、ブロック状の発泡体によつてガス室
を形成することも出来る。In addition, when using a gas separation plate with uneven parts on both sides, the layered foam is interposed between the protrusions and the reactive gas spreads to these parts, and the thin plate is used as the gas separation plate. If used, the gas chamber can also be formed by a block of foam.
第1図は従来の燃料電池の要部拡大断面図、第2図及び
第3図はいづれも本発明燃料電池の要部拡大断面図てあ
る。
又第4図は本発明燃料電池の放電特性図てある。1,2
・・・・・・ガス拡散電極、3,3″・・・・・・ガス
分離板、4・・・・・マトリックス電解質、5,5″・
・導電性多孔質の発泡体。FIG. 1 is an enlarged sectional view of the main part of a conventional fuel cell, and FIGS. 2 and 3 are both enlarged sectional views of the main part of the fuel cell of the present invention. FIG. 4 shows the discharge characteristics of the fuel cell of the present invention. 1,2
...Gas diffusion electrode, 3,3"...Gas separation plate, 4...Matrix electrolyte, 5,5"
- Conductive porous foam.
Claims (1)
離板により、前記各極板の背面に夫々のガス室を形成す
るものにおいて、前記各電極背面とガス分離板との間に
導電性多孔質の発泡体を介在させたことを特徴とする燃
料電池。 2 前記ガス分離板の両面に凹凸部を有し、前記発泡体
は分離板の凸部に当接して電極背面に密着する層として
構成されていることを特徴とする前記特許請求の範囲第
1項記載の燃料電池。 3 前記ガス分離板は薄板よりなり、前記発泡体はこの
薄板と電極背面との間の空間を満たすブロックとして構
成されていることを特徴とする前記特許請求の範囲第1
項記載の燃料電池。[Scope of Claims] 1. In a device in which a gas chamber is formed on the back surface of each electrode plate by a conductive gas separation plate interposed between gas diffusion electrodes of different polarities, the back surface of each electrode and the gas separation plate A fuel cell characterized in that an electrically conductive porous foam is interposed between the fuel cell and the fuel cell. 2. The gas separation plate has uneven parts on both sides, and the foam is configured as a layer that comes into contact with the protrusions of the separation plate and adheres to the back surface of the electrode. Fuel cell as described in Section. 3. The first aspect of claim 1, wherein the gas separation plate is made of a thin plate, and the foam is configured as a block that fills a space between the thin plate and the back surface of the electrode.
Fuel cell as described in Section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53073898A JPS6041833B2 (en) | 1978-06-16 | 1978-06-16 | Fuel cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53073898A JPS6041833B2 (en) | 1978-06-16 | 1978-06-16 | Fuel cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54164231A JPS54164231A (en) | 1979-12-27 |
| JPS6041833B2 true JPS6041833B2 (en) | 1985-09-19 |
Family
ID=13531472
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53073898A Expired JPS6041833B2 (en) | 1978-06-16 | 1978-06-16 | Fuel cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6041833B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58131664A (en) * | 1982-01-29 | 1983-08-05 | Hitachi Ltd | Fuel cell |
| JPS5996668A (en) * | 1982-11-26 | 1984-06-04 | Agency Of Ind Science & Technol | Bipolar separator for fuel cell |
| JPS59139961U (en) * | 1983-03-10 | 1984-09-19 | 日本電池株式会社 | gas diffusion electrode |
| US6312845B1 (en) | 1995-10-06 | 2001-11-06 | The Dow Chemical Company | Macroporous flow field assembly |
-
1978
- 1978-06-16 JP JP53073898A patent/JPS6041833B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54164231A (en) | 1979-12-27 |
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