JPS60140656A - Production of cadmium negative electrode plate for alkaline storage battery - Google Patents

Production of cadmium negative electrode plate for alkaline storage battery

Info

Publication number
JPS60140656A
JPS60140656A JP58248905A JP24890583A JPS60140656A JP S60140656 A JPS60140656 A JP S60140656A JP 58248905 A JP58248905 A JP 58248905A JP 24890583 A JP24890583 A JP 24890583A JP S60140656 A JPS60140656 A JP S60140656A
Authority
JP
Japan
Prior art keywords
cadmium
electrode plate
powder
cadmium oxide
metallic
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
JP58248905A
Other languages
Japanese (ja)
Inventor
Masakazu Shimoda
下田 雅一
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 JP58248905A priority Critical patent/JPS60140656A/en
Publication of JPS60140656A publication Critical patent/JPS60140656A/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
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/26Processes of manufacture
    • 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

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

Abstract

PURPOSE:To eliminate the chemical conversion process and simplify the production process by coating a conductive, porous plate with a slurry-like active material kneaded with nickel powder, cadmium oxide, and metallic cadmium powder obtained by reducing cadmium oxide powder in the reducing atmosphere using an adhesive solution then drying it. CONSTITUTION:Cadmium oxide powder of 0.5-1mu is heated in a hydrogen stream to obtain metallic cadmium by reducing cadmium oxide. A mixture of metallic cadmium thus obtained, cadmium oxide, and nickel powder at a ratio of 2:7:1 is kneaded with an organic, adhesive solution, then a nickel-plated porous iron plate is coated with it and is dried to obtain an electrode plate. The electrode plate thus obtained does not contain impurities such as zinc sulfate as before, and metallic cadmium grains existing in an active material are fine, thereby the electrode plate has advantages that it is excellent in the charging/ discharging characteristics and also the capacity reduction while left as it is little.

Description

【発明の詳細な説明】 本発明はアルカリ蓄電池用カドミウム陰極板の製造法の
改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improved method for manufacturing cadmium cathode plates for alkaline storage batteries.

従来、アルカリ蓄電池用カドミウム陰極板の代表的製造
方法には次のようなものがある。第1の方法は現在もっ
とも広く用いられているもので、集電体を兼ねた活物質
保持体として、ニッケルメッキを施した鉄の薄い多孔板
やネット1r二、すにル船1;ん自ル→を土−/メ手J
し七ルロー7等の結着剤水溶液で混練したスラリーを塗
着、乾燥後、水素気流中において、例えば900℃程度
の温度で焼結して多孔度が70〜8596の多孔性基板
を得る。しかる後、この基板に高濃度の硝酸カドミウム
溶液を含浸して乾燥後、高温に保った苛性アルカリ溶液
中で電解した後水洗、乾燥あるいは単に苛性アルカリ溶
液中に浸漬後水洗乾燥するなどの方法で「焼結式」と呼
ばれている。これらの製造法は、活物質の充填工程が煩
雑で、繰り返し充填を行う必要がある等、比較的高価な
極板となっている。
Conventionally, typical methods for manufacturing cadmium cathode plates for alkaline storage batteries include the following. The first method is currently the most widely used, and uses a thin perforated iron plate with nickel plating, a net, or a net as an active material holder that also serves as a current collector. Ru → wo Sat-/Me hand J
A slurry kneaded with an aqueous binder solution such as Shishichi Rouleau 7 is applied, dried, and then sintered in a hydrogen stream at a temperature of, for example, about 900° C. to obtain a porous substrate having a porosity of 70 to 8,596. After that, this substrate is impregnated with a highly concentrated cadmium nitrate solution, dried, electrolyzed in a caustic alkaline solution kept at a high temperature, washed with water, dried, or simply immersed in a caustic alkaline solution, washed with water, and dried. It is called the "sintering method." These manufacturing methods require a complicated active material filling process and require repeated filling, resulting in relatively expensive electrode plates.

第2の方法は、前述の導電性を有する多孔板やネットか
らなる芯材に酸化カドミウムを主成分とするペースト状
活物質を直接塗着して乾燥固着する方法で、焼結式に比
べて非常に簡単であり、「ペースト式」と呼ばれている
。この製造法は、活物質がニッケル焼結多孔体に強固に
保持されている焼結式極板に比べて活物質の機械的強度
が弱く、組立工程等において、活物質が芯材から剥離脱
落し易いという欠点を有している。
The second method is to directly apply a paste-like active material containing cadmium oxide as a main component to the core material made of the conductive porous plate or net and dry it, which is more effective than the sintering method. It is very simple and is called the "paste method." In this manufacturing method, the mechanical strength of the active material is weaker than that of a sintered electrode plate in which the active material is firmly held in a nickel sintered porous body, and the active material peels off from the core material during the assembly process etc. It has the disadvantage of being easy to do.

一方、カドミウムを陰極活物質とするアルカリ蓄電池は
、陰極板の容量を陽極板の容量より2〜3割多くして、
電池容量を陽極板支配としている。これは、陰極板の方
が深い充放電に弱く、充放電サイクルの進行に伴う容量
低下の度合か大きいためである。こうした理由により、
組立時の極板の状態は通常、陽極板は完全放電状態で、
陰極板は電池容量の2〜3割程度充電された状態となっ
ている。これは、ペースト式の陰極板でも同様で、酸化
カドミウムを主体としたペーストを芯材に塗着、乾燥後
苛性アルカリ溶液中で化成し、酸化カドミウムの一部を
金属カドミウムに還元するか、あるいは、完全に金属カ
ドミウムに還元した後放電して一部の金属カドミウムを
残した状態にし電池に組込んでいる。
On the other hand, in alkaline storage batteries that use cadmium as the cathode active material, the capacity of the cathode plate is 20 to 30% greater than the capacity of the anode plate.
Battery capacity is dominated by the anode plate. This is because the cathode plate is more susceptible to deep charging and discharging, and the capacity decreases to a greater degree as the charging and discharging cycles progress. For these reasons,
The state of the electrode plate at the time of assembly is usually that the anode plate is in a fully discharged state,
The cathode plate is charged to about 20 to 30% of the battery capacity. This is also the case with paste-type cathode plates, where a paste consisting mainly of cadmium oxide is applied to the core material, dried and then chemically converted in a caustic alkaline solution to reduce some of the cadmium oxide to metallic cadmium. After it is completely reduced to metallic cadmium, it is discharged, leaving some metallic cadmium, and is then incorporated into a battery.

さらに、化成した極板は水洗、乾燥1稈を必要とするた
め、ペーストの塗着から組立までを連続したラインで行
うとすると、生産設備ラインは非常に長大なものとなり
、実用的でなかった。
Furthermore, the chemically formed electrode plates require one culm of washing and drying, so if the process from applying the paste to assembly was carried out in a continuous line, the production equipment line would be extremely long, which would be impractical. .

このような一点から、前述のペースト式極板の化成工程
をなくして、アルカリ蓄電池製造工程を簡略化するため
1こ、出発原料の一部を金属カドミウムとすることが提
案されている。
From this point of view, it has been proposed to use metal cadmium as a part of the starting material in order to eliminate the above-mentioned chemical conversion process of paste-type electrode plates and simplify the alkaline storage battery manufacturing process.

この金属カドミウムは?8池内での活性度等の理由によ
り、できるかぎり微細粉末であることが望ましい。こう
した、微細な金属カドミウムを得る方法として、硫酸カ
ドミウム水溶液に亜鉛粉末を添加することによって、金
属カドミウムを析出させる方法が提案されているが、こ
うして得られたカドミウム中には硫酸亜鉛が残留してい
るため、長時間の水洗を必要とする等の欠点を有してい
た。
What about this metal cadmium? 8 For reasons such as activity within the pond, it is desirable that the powder be as fine as possible. As a method for obtaining such fine metal cadmium, a method has been proposed in which metal cadmium is precipitated by adding zinc powder to a cadmium sulfate aqueous solution, but zinc sulfate remains in the cadmium obtained in this way. Therefore, it has disadvantages such as requiring a long time of washing with water.

本発明は、酸化カドミウム粉末を直接還元することによ
り、不純物を含まない微細な金属カドミウムを得んとす
るものである。
The present invention aims to obtain fine metallic cadmium containing no impurities by directly reducing cadmium oxide powder.

次に本発明の一実施例を説明する。Next, one embodiment of the present invention will be described.

05〜1μの酸化カドミウム粉末を水素気流中で約29
0℃1こ加熱して、酸化カドミウムを還元して金属カド
ミウムを得る。こうして得られた金属カドミウムと酸化
カドミウムおよびニッケル粉末の2ニア:lからなる混
合物を有機粘着溶液で混練した後、ニッケルメンキした
鉄多孔板上に塗着乾燥し目的の極板を得た。
Cadmium oxide powder of 05 to 1 μm was heated to about 29 μm in a hydrogen stream.
The mixture is heated to 0° C. to reduce cadmium oxide and obtain metal cadmium. The thus obtained mixture of 2:1 of metal cadmium, cadmium oxide, and nickel powder was kneaded with an organic adhesive solution, and then applied and dried on a nickel-coated iron porous plate to obtain the desired electrode plate.

こうして得られた極板は、従来のように硫酸亜鉛等の不
純物を含まず、活物質中に存在する金属カドミウム粒子
も微細であるため充放電特性がすぐれているたけでなく
、放置中の容量低下も少ない等の利点を有する。
The electrode plates obtained in this way do not contain impurities such as zinc sulfate unlike conventional ones, and the metal cadmium particles present in the active material are also fine, so they not only have excellent charge and discharge characteristics, but also have a high capacity when left unused. It has advantages such as less deterioration.

特許出願人patent applicant

Claims (1)

【特許請求の範囲】[Claims] 酸化カドミウム粉末を還元性雰囲気中で還元して得られ
た金属カドミウム粉末と酸化カドミウムおよびニッケル
粉末とを粘着溶液で混練して得たスラリー状活物質を導
電性を有する多孔板に塗着乾燥することを特徴とするア
ルカリ蓄電池用カドミウム陰極板の製造法。
A slurry active material obtained by kneading metallic cadmium powder obtained by reducing cadmium oxide powder in a reducing atmosphere, cadmium oxide and nickel powder with an adhesive solution is applied to a conductive porous plate and dried. A method for producing a cadmium cathode plate for an alkaline storage battery, characterized by:
JP58248905A 1983-12-28 1983-12-28 Production of cadmium negative electrode plate for alkaline storage battery Pending JPS60140656A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58248905A JPS60140656A (en) 1983-12-28 1983-12-28 Production of cadmium negative electrode plate for alkaline storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58248905A JPS60140656A (en) 1983-12-28 1983-12-28 Production of cadmium negative electrode plate for alkaline storage battery

Publications (1)

Publication Number Publication Date
JPS60140656A true JPS60140656A (en) 1985-07-25

Family

ID=17185171

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58248905A Pending JPS60140656A (en) 1983-12-28 1983-12-28 Production of cadmium negative electrode plate for alkaline storage battery

Country Status (1)

Country Link
JP (1) JPS60140656A (en)

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