JPS60158552A - Manufacture of paste type cadmium anode - Google Patents

Manufacture of paste type cadmium anode

Info

Publication number
JPS60158552A
JPS60158552A JP59013860A JP1386084A JPS60158552A JP S60158552 A JPS60158552 A JP S60158552A JP 59013860 A JP59013860 A JP 59013860A JP 1386084 A JP1386084 A JP 1386084A JP S60158552 A JPS60158552 A JP S60158552A
Authority
JP
Japan
Prior art keywords
paste
plate
cracks
resistant fibers
alkali resistant
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.)
Pending
Application number
JP59013860A
Other languages
Japanese (ja)
Inventor
Takao Kikuoka
菊岡 孝雄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP59013860A priority Critical patent/JPS60158552A/en
Publication of JPS60158552A publication Critical patent/JPS60158552A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/665Composites
    • H01M4/667Composites in the form of layers, e.g. coatings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/246Cadmium electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/52Removing gases inside the secondary cell, e.g. by absorption
    • H01M10/526Removing gases inside the secondary cell, e.g. by absorption by gas recombination on the electrode surface or by structuring the electrode surface to improve gas recombination
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M2004/026Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027Negative electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/661Metal or alloys, e.g. alloy coatings
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Composite Materials (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To increase oxygen gas absorbing ability by forming a large number of cracks by heating on the surface of plate prepared by filling paste containing alkali resistant fibers in a core. CONSTITUTION:Paste is prepared in such a way that alkali resistant fibers are dispersed in cadmium oxide powder and they are kneaded with viscous solution prepared by dissolving, for example, polyvinyl alcohol in water and ehtylene glycol. The paste is spreaded on a nickel plated steel porous plate. The coated plate is passed through a slit to adjust thickness and quickly dried to form cracks on its surface. By forming cracks on the plate, effective surface area is increased, and oxygen absorbing ability is improved. Since alkali resistant fibers serves as reinforcing agent, coming off of the active material is prevented during handling.

Description

【発明の詳細な説明】 本発明は密閉形ニッケル・カドミウム蓄電池に使用され
るペースト式カドミウム陰極の酸素ガス吸収性能向上1
と関するものである。
Detailed Description of the Invention The present invention provides improvements in the oxygen gas absorption performance of paste-type cadmium cathodes used in sealed nickel-cadmium storage batteries.
It is related to.

従来密閉形ニッケル型カドミウム蓄電池のカドミウム陰
極としては、焼結式あるいはペースト式、プレス式、電
着式などが実用化されている。ペースト式電極は、酸化
カドミウム粉末または水酸化カドミウム粉末あるいはそ
れらの混合物を主体とし、繊維などの補強剤、導電性粉
末を添加したものを水または有機溶媒1こポリビニルア
ルコールやポリテトラフロロエチレン等の粘結剤を溶解
あるいは分散させた液で混練しペースト状となし、それ
を鉄にニッケルメッキした多孔板等の芯材の上に塗布し
乾燥したものである。その製造方法は簡単であり、焼結
式のように高価なニッケル粉末を多く使う必要がないの
で安価で特性の安定した電極として多く使用されている
。しかし、従来のペースト式カドミウム極は焼結式と(
らべて酸素ガス吸収性能か劣るという欠点があり、ペー
スト式陰極の酸素がス吸収性能1こついては、バインダ
の種類及び量、電極の気孔率や孔径分布、電池電解液量
の面で改良か゛なされてきた。また近年、1時間程度の
急速充電を必要とする用途力C多くなったか、これには
酸素かス吸収速度か゛遅く、過充電C川 時の電流を約0.5RA以下にするように何等かの方法
で充電状態を検出制御する必要があった。
Conventional cadmium cathodes for sealed nickel-type cadmium storage batteries have been put into practical use, such as sintered type, paste type, pressed type, and electrodeposition type. Paste-type electrodes are made mainly of cadmium oxide powder, cadmium hydroxide powder, or a mixture thereof, with reinforcing agents such as fibers, and conductive powder added to water or an organic solvent such as polyvinyl alcohol or polytetrafluoroethylene. It is made by kneading a liquid with a binder dissolved or dispersed therein to form a paste, which is then applied onto a core material such as a perforated plate made of nickel plated iron and dried. The manufacturing method is simple, and unlike the sintering method, there is no need to use a large amount of expensive nickel powder, so it is widely used as an inexpensive electrode with stable characteristics. However, the conventional paste type cadmium electrode is different from the sintered type (
However, the oxygen gas absorption performance of the paste type cathode is inferior, and improvements need to be made in terms of the type and amount of binder, the porosity and pore size distribution of the electrode, and the amount of battery electrolyte. It has been done. In addition, in recent years, there have been many applications that require rapid charging of about 1 hour, and this is due to the slow absorption rate of oxygen and gas, so it is necessary to do something to reduce the current during overcharging to about 0.5 RA or less. It was necessary to detect and control the charging state using the following method.

本発明は上記の点1こ鑑み、ペースト式陰極のC自 酸素ガス吸収性能を向上させl orb A程度の電流
で過充電しても、安全弁か作動しないようになし、1時
間程度で急速充電を可能ならしめたものである。
In view of the above point 1, the present invention improves the carbon self-oxygen gas absorption performance of the paste type cathode, prevents the safety valve from operating even if overcharged with a current of about 1 orb A, and allows rapid charging in about 1 hour. This made it possible.

本発明は乾燥時1こ極板表面部に微細なりラックを多数
入れ、陰極の有効表面積を増加させて酸素ガス吸収性能
を向上させるとともに、クラックか入ること1こよって
低下する極板ペーストの脱落弾質を保持するために(脱
落防止剤として)ポリアミドやアクリル系などの合成繊
維や金属繊維などの耐アルカリ繊維を添加することを骨
子としている。
In the present invention, a large number of fine racks are placed on the surface of the electrode plate during drying to increase the effective surface area of the cathode and improve the oxygen gas absorption performance. In order to maintain elasticity (as a fall-off prevention agent), alkali-resistant fibers such as synthetic fibers such as polyamide and acrylic fibers and metal fibers are added.

次に本発明の一実施例を示す。Next, one embodiment of the present invention will be described.

酸化カドミウム(粒径的0. fl 5 II) l 
#Iこアクリル系繊維(長さ1mm)20Fをよく分散
させた後ポリビニルアルコール23yを水ssmn及び
エチレングリコール34omitこ溶解した粘稠液て混
練し、ペースト状とした。このペースト状物質を鉄にニ
ッケルメッキした多孔仮に塗布し、スリットを通すこと
により整形した。
Cadmium oxide (particle size 0. fl 5 II) l
After #I acrylic fiber (length 1 mm) 20F was well dispersed, polyvinyl alcohol 23y was dissolved in water ssmn and ethylene glycol 34omi to form a viscous liquid and kneaded to form a paste. This paste-like material was applied to a nickel-plated porous piece of iron and shaped by passing it through a slit.

その後の乾燥は、クラックが生じやすいようIこ急速な
乾燥を行った。すなわち、120”(、の熱風を極板に
直角1ζ風速約10m/―で当て約6分で乾燥させた。
The subsequent drying was carried out rapidly so that cracks were likely to occur. That is, 120" hot air was applied to the electrode plate at a perpendicular 1ζ wind speed of about 10 m/- to dry it in about 6 minutes.

極板は乾燥後で07關であった。このようにして作製し
た極板には幅0.1 mm程度ツクラックが多数存在す
るが、耐アルカリ繊維か補強剤として入っているので、
その後の取扱い1こよって脱落することはなかった。こ
の電極を通常の方法で化成し、焼結式の酸化ニッケル電
極、ポリアミド製のセパレータと組合せて捲回し電池と
した。電池はKR−3C形とし。
The electrode plate was 0.7 mm after drying. The electrode plate produced in this way has many cracks with a width of about 0.1 mm, but since they contain alkali-resistant fibers or reinforcing agents,
It did not fall off due to subsequent handling. This electrode was chemically formed using a conventional method and combined with a sintered nickel oxide electrode and a polyamide separator to form a wound battery. The battery is KR-3C type.

電池電解液としては30%KOH水溶液を使用した。A 30% KOH aqueous solution was used as the battery electrolyte.

図面に周囲温1[20℃1こおいて1,2Aで急速充電
した場合の電池内圧の変化を示した。Aは通常のクラッ
クの全くない電極を使用した電池の電池内圧の変化であ
り、Bは本発明の実施例で示した電極を使用した電池の
電池内圧の変化である。Pは電池の安全弁作動圧である
。このように通常の電池の電池内圧Aの変化は安全弁作
動圧Pに対して余裕がなく、周囲温廣力f低くなると電
池外1こガス漏れし、著しく電池寿命を短縮する結果と
なった。これ1こ対し 本発明による電池の電池内圧B
は最高でも、安全弁作動圧Pの約1/3であり、1.2
A(ICmA相当)程度の充電ではガス漏れすることは
ないことがわかった。また放電特性は両者に差はなかっ
た。
The figure shows the change in battery internal pressure when rapidly charging at 1.2 A at an ambient temperature of 1 [20° C.]. A is the change in battery internal pressure of a battery using a normal electrode with no cracks, and B is a change in battery internal pressure of a battery using the electrode shown in the example of the present invention. P is the safety valve operating pressure of the battery. As described above, there is no margin for changes in the battery internal pressure A in a normal battery relative to the safety valve operating pressure P, and when the ambient temperature f becomes low, gas leaks outside the battery, resulting in a significant shortening of the battery life. In contrast to this, the battery internal pressure B of the battery according to the present invention
is at most about 1/3 of the safety valve operating pressure P, which is 1.2
It was found that there was no gas leakage when charging at around A (equivalent to ICmA). Furthermore, there was no difference in discharge characteristics between the two.

このように、ii電池内圧上昇を抑えられることがわか
ったが、これは陰極板の表面積ζこクラックが入ったこ
と1こより有効表面積が大きくなり、酸素ガス吸収能力
を大きくならしめたものと考えられる。
In this way, it was found that the rise in battery internal pressure could be suppressed, but this is thought to be due to the fact that the surface area of the cathode plate ζ was cracked, which increased the effective surface area and increased the oxygen gas absorption capacity. It will be done.

上述せる如(、本発明によればペースト式カドミウム陰
極の酸素ガス吸収性能を向上せしめ、また極板ペースト
の脱落強度を保持し得る等工業的価値基だ大なるもので
ある。
As mentioned above, the present invention has great industrial value, such as improving the oxygen gas absorption performance of a paste-type cadmium cathode and maintaining the peeling strength of the electrode plate paste.

【図面の簡単な説明】[Brief explanation of drawings]

図面は従来の電池と本発明による電池との電池内圧の比
較図である。 特許出願人 充電時間−
The drawing is a comparison diagram of battery internal pressure between a conventional battery and a battery according to the present invention. Patent applicant charging time −

Claims (1)

【特許請求の範囲】[Claims] 耐アルカリ性繊維を添加したペースト状物質を芯材に愼
入せる極板の乾燥時において極板表面部にクラックを生
じさせることを特徴とするペースト式カドミウム陰極の
製造法。
A method for producing a paste-type cadmium cathode, characterized in that a paste-like substance added with alkali-resistant fibers is poured into a core material, and cracks are generated on the surface of the electrode plate when the electrode plate is dried.
JP59013860A 1984-01-27 1984-01-27 Manufacture of paste type cadmium anode Pending JPS60158552A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59013860A JPS60158552A (en) 1984-01-27 1984-01-27 Manufacture of paste type cadmium anode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59013860A JPS60158552A (en) 1984-01-27 1984-01-27 Manufacture of paste type cadmium anode

Publications (1)

Publication Number Publication Date
JPS60158552A true JPS60158552A (en) 1985-08-19

Family

ID=11845013

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59013860A Pending JPS60158552A (en) 1984-01-27 1984-01-27 Manufacture of paste type cadmium anode

Country Status (1)

Country Link
JP (1) JPS60158552A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5094452A (en) * 1973-12-22 1975-07-28
JPS50134153A (en) * 1974-04-16 1975-10-24
JPS5553874A (en) * 1978-10-16 1980-04-19 Furukawa Battery Co Ltd:The Method of manufacturing cadmium negative electrode for alkaline battery

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5094452A (en) * 1973-12-22 1975-07-28
JPS50134153A (en) * 1974-04-16 1975-10-24
JPS5553874A (en) * 1978-10-16 1980-04-19 Furukawa Battery Co Ltd:The Method of manufacturing cadmium negative electrode for alkaline battery

Similar Documents

Publication Publication Date Title
JPH0578141B2 (en)
JPH11307116A (en) Cadmium negative electrode for alkaline storage battery
JP3555177B2 (en) Sealed lead-acid battery
JPS60158552A (en) Manufacture of paste type cadmium anode
JPS61138458A (en) Alkaline battery
JP3744677B2 (en) Method for producing sintered cadmium negative electrode
JPS5851669B2 (en) Manufacturing method of battery electrode substrate
JPS5819866A (en) Manufacture of cadmium electrode for secondary battery
JPS58201271A (en) Sealed type alkaline storage battery
JPH06295727A (en) Sealed alkaline storage battery
JP2591982B2 (en) Cadmium negative electrode plate and alkaline secondary battery using the negative electrode plate
JPS60158551A (en) Manufacture of cadmium electrode
JP2001266858A (en) Negative electrode for alkaline battery and its manufacturing method
JPH10275619A (en) Paste type cadmium electrode
JPS63164162A (en) Cadmium negative electrode for alkaline storage battery
JPS58186164A (en) Manufacture of negative electrode for alkaline battery
JPH0251874A (en) Alkaline zinc lead-acid battery
JPH04237951A (en) Manufacture of nickel electrode for alkaline storage battery
JPH1140151A (en) Nickel-metal hydride secondary battery
JPH0417260A (en) Cadmium negative electrode for alkaline storage battery
JPS61138472A (en) Alkaline battery
JPS61203559A (en) Manufacture of alkaline storage battery
JPS58186161A (en) Negative electrode for alkaline battery
JPS59165371A (en) Cathode plate for alkaline storage battery
JPS62184764A (en) Cadmium negative electrode for alkaline storage battery