JPS648430B2 - - Google Patents
Info
- Publication number
- JPS648430B2 JPS648430B2 JP57042368A JP4236882A JPS648430B2 JP S648430 B2 JPS648430 B2 JP S648430B2 JP 57042368 A JP57042368 A JP 57042368A JP 4236882 A JP4236882 A JP 4236882A JP S648430 B2 JPS648430 B2 JP S648430B2
- Authority
- JP
- Japan
- Prior art keywords
- mesh
- less
- particle size
- activated carbon
- resin
- 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
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/96—Carbon-based electrodes
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inert Electrodes (AREA)
Description
本発明は空気電池用の新規な組成を有する陽極
に関し、更に詳しくは樹脂を活性炭と混合後加熱
し固結した無焼成電極において、原料樹脂及び活
性炭の主として粒度を規制することにより高い起
電力と放電々流密度を保持し、かつ、電解液の浸
透を制御し得る陽電極の構成に関するものであ
る。
空気電池とは復極剤に空気中の酸素を用いた一
次電池で、(空気―炭素|電解液|亜鉛)な
る構成をもつものであるが、その炭素極は無防水
では電解液の浸透速度が早く電池の寿命を著しく
短くするので、焼成電極の場合は電極をパラフイ
ン、樹脂等の防水剤の溶液に浸漬後溶媒を揮散さ
せ薄い防水膜を被覆させて電解液の浸透を制御
し、また無焼成電極の場合には活性炭と樹脂溶液
を練合して成型後乾燥固結させるか、あるいは
0.5μ以下のコロイド状樹脂末と活性炭とを混合し
加熱する工程を経て防水膜の生成と固結とを同時
に行なう等のものであつた。要するに、前記いず
れの方法にしても炭素面に薄い防水皮膜を被覆し
て極に電解液の浸透するのを制御するということ
を原理とするものであつた。
これに対し本発明は、前記した公知諸方法と発
明の原理を異にし、樹脂粒子と活性炭の粒子径を
適当に選択、配合してそれらを混合後加熱、溶着
させるものであり、これにこれら原料成分の配合
比の検討も加えて、起電力高く、かつ、電解液の
浸透速度の遅い強靭な電極を得るに至り、これを
実用的に利用したものである。
すなわち、本発明は原料として粒径200メツシ
ユ以下の活性炭と粒径100メツシユ以下及び300メ
ツシユ以下の2種類の樹脂を用いることよりな
り、これら3種類の原料を混合後加熱溶着し、添
付図面で説明するように活性炭層中に大・小2種
類の粒径の樹脂が混在して沈着する状態を形成さ
せ成型するものである。
なお、これら3種類の原料の配合比に臨界的範
囲は見出し難いが、好ましくは活性炭75〜80重量
%、粒径300メツシユ以下の樹脂13〜17重量%及
び粒径100メツシユ以下の樹脂3〜12重量%の範
囲であることが推奨される。
本発明の実施の一例を示せば、粒径200メツシ
ユ以下の活性炭75重量%、粒径2〜40μのポリエ
チレン15重量%及び粒径100〜200メツシユのポリ
エチレン10重量%を混合し、成型器に入れ1cm2当
り約500gの圧力を掛けながら120〜130℃で5〜
10分間加熱後放冷する。
かくして得た厚さ1.7mmの平板状陽極の一面を
対空気面、他面を対液面とし、亜鉛を陰極とし、
そして苛性ソーダまたは苛性カリ溶液を電解液と
する公知の方式の電池を組み立て、一定の電流密
度で電圧が急低下する時点まで放電し、その時の
電池の性能を求めると次の通りであつた。
The present invention relates to an anode having a novel composition for air batteries, and more specifically to an unfired electrode in which a resin is mixed with activated carbon and then heated and solidified. The present invention relates to a configuration of a positive electrode that can maintain discharge current density and control permeation of electrolyte. An air battery is a primary battery that uses oxygen in the air as a depolarizing agent, and has a composition of (air - carbon | electrolyte | zinc), but the permeation rate of the electrolyte is low when the carbon electrode is not waterproof. In the case of fired electrodes, the electrodes are immersed in a solution of waterproofing agent such as paraffin or resin, and then the solvent is evaporated and a thin waterproof membrane is coated to control the penetration of the electrolyte. In the case of unfired electrodes, activated carbon and resin solution are kneaded and molded and then dried and solidified, or
The process involves mixing colloidal resin powder of 0.5 μm or less with activated carbon and heating it to simultaneously generate and solidify a waterproof film. In short, all of the above methods are based on the principle of coating the carbon surface with a thin waterproof film to control penetration of the electrolyte into the electrode. On the other hand, the present invention differs from the known methods described above in principle, by appropriately selecting and blending the particle diameters of resin particles and activated carbon, and heating and welding them after mixing. By examining the blending ratio of raw material components, we were able to obtain a strong electrode with a high electromotive force and a slow permeation rate of electrolyte, which we have put to practical use. That is, the present invention uses activated carbon with a particle size of 200 mesh or less and two types of resins with particle sizes of 100 mesh or less and 300 mesh or less as raw materials. After mixing these three types of raw materials, they are heated and welded, and as shown in the attached drawings. As explained, molding is performed by forming a state in which resins of two types of particle sizes, large and small, are mixed and deposited in the activated carbon layer. It is difficult to find a critical range for the blending ratio of these three types of raw materials, but preferably activated carbon is 75-80% by weight, resin with a particle size of 300 mesh or less is 13-17% by weight, and resin with a particle size of 100 mesh or less is 3-3% by weight. A range of 12% by weight is recommended. To illustrate an example of the implementation of the present invention, 75% by weight of activated carbon with a particle size of 200 mesh or less, 15% by weight of polyethylene with a particle size of 2 to 40μ, and 10% by weight of polyethylene with a particle size of 100 to 200 mesh are mixed, and the mixture is placed in a molding machine. Heat at 120 to 130°C for 5 to 50 minutes while applying approximately 500g of pressure per 1cm2 .
Heat for 10 minutes and then let cool. One side of the flat anode with a thickness of 1.7 mm thus obtained was used as the air-facing surface, the other side was used as the liquid-facing surface, and zinc was used as the cathode.
A battery of a known type using caustic soda or caustic potash solution as the electrolyte was assembled and discharged at a constant current density until the voltage suddenly decreased.The performance of the battery at that time was determined as follows.
【表】
これに対し、市販の無焼成電池の性能は次の通
りであつた:[Table] In contrast, the performance of commercially available unfired batteries was as follows:
【表】
上記表1および2より、同一の電流密度と電気
容量及び液浸面積に対し、本発明による電極の厚
さは1.7mmであるが市販品は10mm厚であり、明ら
かに本発明品の電解液浸透速度が遅いことが示さ
れる。また、従来の空気電池の実用電流密度は最
高約5mA/cm2とされているが、本発明品は
10mA/cm2でも使用できる特長があることも本発
明の優秀性を示すものといえる。[Table] From Tables 1 and 2 above, for the same current density, electric capacity, and liquid immersion area, the thickness of the electrode according to the present invention is 1.7 mm, but the thickness of the commercially available product is 10 mm. This indicates that the electrolyte permeation rate is slow. In addition, the practical current density of conventional air batteries is said to be a maximum of approximately 5mA/ cm2 , but the product of the present invention
The fact that it can be used even at 10 mA/cm 2 can be said to be an indication of the superiority of the present invention.
図面は本発明電極の構造の一部の拡大模型図。
図中、黒点の大粒は粒径100メツシユ以下で小粒
は粒径300メツシユ以下の樹脂粒を示し、黒点の
中粒は粒径200メツシユ以下の活性炭素粒を示す。
The drawing is an enlarged model diagram of a part of the structure of the electrode of the present invention.
In the figure, large black dots indicate resin particles with a particle size of 100 mesh or less, small particles indicate resin particles with a particle size of 300 mesh or less, and medium black dots indicate activated carbon particles with a particle size of 200 mesh or less.
Claims (1)
成電極において、樹脂の粒径が300メツシユ以下
と100メツシユ以下である2種類よりなり、活性
炭が粒径200メツシユ以下であることを特徴とす
る空気電池用陽極。 2 樹脂の粒径300メツシユ以下のものを13〜17
重量%、同粒径100メツシユ以下のもの3〜12重
量%で活性炭の粒径200メツシユのもの75〜80重
量%の配合比であることを特徴とする特許請求の
範囲第1項記載の空気電池用陽極。[Claims] 1. An unfired electrode in which a resin is mixed with activated carbon and solidified by heating, and the resin has two types of particle sizes: 300 mesh or less and 100 mesh or less, and the activated carbon has a particle size of 200 mesh or less. An anode for an air battery characterized by: 2 Resin particle size of 300 mesh or less 13 to 17
The air according to claim 1 is characterized in that the blending ratio is 3 to 12% by weight of particles having the same particle size of 100 mesh or less and 75 to 80% by weight of activated carbon particles having a particle size of 200 mesh. Anode for batteries.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57042368A JPS58158869A (en) | 1982-03-17 | 1982-03-17 | Carbon positive pole for air cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57042368A JPS58158869A (en) | 1982-03-17 | 1982-03-17 | Carbon positive pole for air cell |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58158869A JPS58158869A (en) | 1983-09-21 |
| JPS648430B2 true JPS648430B2 (en) | 1989-02-14 |
Family
ID=12634094
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57042368A Granted JPS58158869A (en) | 1982-03-17 | 1982-03-17 | Carbon positive pole for air cell |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58158869A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2622938C (en) | 2005-12-28 | 2010-11-09 | National University Corporation Nagoya University | Smart vortex generator and aircraft, vessel and rotary machine being equipped with the same |
-
1982
- 1982-03-17 JP JP57042368A patent/JPS58158869A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58158869A (en) | 1983-09-21 |
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