JPH0554891A - Paste type cadmium anode plate for alkaline storage battery - Google Patents

Paste type cadmium anode plate for alkaline storage battery

Info

Publication number
JPH0554891A
JPH0554891A JP3217688A JP21768891A JPH0554891A JP H0554891 A JPH0554891 A JP H0554891A JP 3217688 A JP3217688 A JP 3217688A JP 21768891 A JP21768891 A JP 21768891A JP H0554891 A JPH0554891 A JP H0554891A
Authority
JP
Japan
Prior art keywords
paste
cadmium
anode plate
cathode plate
battery
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.)
Granted
Application number
JP3217688A
Other languages
Japanese (ja)
Other versions
JP3178018B2 (en
Inventor
Mitsuru Koseki
満 小関
Masakazu Shimoda
雅一 下田
Toshio Henmi
敏夫 逸見
Taisuke Kuroda
泰介 黒田
Hirotaka Tsuji
裕貴 辻
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 JP21768891A priority Critical patent/JP3178018B2/en
Publication of JPH0554891A publication Critical patent/JPH0554891A/en
Application granted granted Critical
Publication of JP3178018B2 publication Critical patent/JP3178018B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • 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

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  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To enhance the oxygen-gas absorption performance and the high rate discharge characteristics of an alkaline storage battery based on the use of a paste type cadmium anode plate, by providing a conductor layer composed of a furnace black powder and a thermally gelatinizable cellulose derivative adhesive paste on the surface of the paste type cadmium anode plate for alkaline battery. CONSTITUTION:100 parts by weight of water, 5 weight part of furnace black powder (specific surface area 1475m<2>/g, DBP oil absorption 3.3ml/g), and 5 parts by weight of methyl cellulose are mixed while agitated, to prepare a carbon powder suspension. This suspension is applied thin onto the surface of the formed paste type cadmium anode plate and is dried to obtain a complete anode plate. This anode plate is combined with a sintered type cathode plate to prepare a sealed type nickel/cadmium battery. The furnace black preferably has a specific surface area of 1000 to 1500m<2>/g, and DBP oil absorption of 3 to 5ml/g. Further, the adhesive paste preferably is hydroxypropyl methyl cellulose, or hydroxy propyl cellulose, in addition to methyl cellulose.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は密閉型アルカリ蓄電池に
用いられるペースト式カドミウム陰極板の酸素ガス吸収
性能の改良と上記陰極板を用いた電池の高率放電特性の
向上に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in oxygen gas absorption performance of a paste type cadmium cathode plate used in a sealed alkaline storage battery and an improvement in high rate discharge characteristics of a battery using the cathode plate.

【0002】[0002]

【従来の技術】従来、アルカリ蓄電池用ペースト式カド
ミウム陰極板は、酸化カドミウム、水酸化カドミウム、
金属カドミウム等からなる活物質粉末に糊料、溶媒、補
強繊維等を加え、これらを混練してペースト状となし、
このペーストをニッケルメッキした鉄穿孔板のような導
電性芯材の両面に塗着し、乾燥することによって作製さ
れている。従って、焼結式カドミウム陰極板に比べ製造
工程を簡略化出来、活物質充填量が増やせるので高エネ
ルギー密度化出来る等の利点を有している。
2. Description of the Related Art Conventionally, a paste type cadmium cathode plate for an alkaline storage battery is a cadmium oxide, a cadmium hydroxide,
A paste, a solvent, reinforcing fibers, etc. are added to an active material powder made of metal cadmium, etc., and these are kneaded to form a paste,
This paste is applied to both surfaces of a conductive core material such as a nickel-plated iron perforated plate and dried. Therefore, compared with the sintered cadmium cathode plate, the manufacturing process can be simplified and the active material filling amount can be increased, so that the energy density can be increased.

【0003】しかし、ペースト式カドミウム陰極板は上
記のような構成であるため、活物質層中に焼結式のよう
なニッケル焼結体の導電ネットワークを持たず、また、
放電生成物である水酸化カドミウムは導電性が低いの
で、充電時に生成する金属カドミウムは導電性の高い部
分、特に芯材近傍に偏在する傾向がある。電池を過充電
した場合には陽極板から酸素ガスが発生し、陰極板で次
の(1)式で示す反応によって吸収されるが、この反応
は陰極板の表面部で起こり易いので、上記のように極板
表面部に金属カドミウムが生成し難いペースト式カドミ
ウム陰極板では酸素ガス吸収性能が低いという欠点があ
った。
However, since the paste-type cadmium cathode plate has the above-mentioned structure, it does not have a conductive network of a nickel-sintered body like that of the sintered type in the active material layer, and
Since cadmium hydroxide, which is a discharge product, has low conductivity, metal cadmium generated during charging tends to be unevenly distributed in a highly conductive part, particularly in the vicinity of the core material. When the battery is overcharged, oxygen gas is generated from the anode plate and absorbed by the reaction represented by the following formula (1) at the cathode plate, but this reaction easily occurs on the surface of the cathode plate. As described above, the paste type cadmium cathode plate in which metal cadmium is hard to be generated on the surface of the electrode plate has a drawback that the oxygen gas absorption performance is low.

【0004】[0004]

【化1】Cd+1/2O2+H2O → Cd(OH)2 この欠点を解消するため、特開昭60−63875号公
報や特開昭60−202666号公報にはペースト式カ
ドミウム陰極板表面にアセチレンブラック含有層を形成
し、極板表面の導電性を高めることによって、充電時に
金属カドミウムを極板表面にも生成させ、酸素ガス吸収
性能を向上させんとする提案がなされている。
## STR00001 ## Cd + 1 / 2O 2 + H 2 O → Cd (OH) 2 In order to solve this drawback, Japanese Patent Laid-Open No. 60-63875 and Japanese Patent Laid-Open No. 60-202666 disclose a paste type cadmium cathode plate surface. It has been proposed to form an acetylene black-containing layer and increase the conductivity of the surface of the electrode plate so that metal cadmium is also generated on the surface of the electrode plate during charging to improve the oxygen gas absorption performance.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、ペース
ト式カドミウム陰極板の表面にアセチレンブラック含有
層を形成する場合、溶媒中にアセチレンブラックと脱落
防止のための糊料を均一に分散させた懸濁液を用い、陰
極板を懸濁液に浸漬するか陰極板表面に懸濁液を塗布す
る方法が取られている。上記懸濁液は塗布層の均質性を
確保するため、十分に撹拌し分散性を良くする必要があ
るが、撹拌によってアセチレンブラックの鎖状構造が崩
壊し、そのことによって導電性が低下して、充分な酸素
ガス吸収性能が得られないという問題点があった。導電
性を確保するため塗布層を厚くすると酸素ガスの透過性
が悪くなり、電解液の拡散も阻害されるので酸素ガス吸
収性能が低下するばかりでなく、高率放電時の電池電圧
特性も悪くなるという問題点があった。
However, in the case of forming an acetylene black-containing layer on the surface of a paste type cadmium cathode plate, a suspension in which acetylene black and a paste for preventing falling are uniformly dispersed in a solvent. Is used to immerse the cathode plate in the suspension or to apply the suspension to the surface of the cathode plate. In order to ensure the homogeneity of the coating layer, the suspension needs to be sufficiently stirred to improve the dispersibility, but the stirring causes the chain structure of acetylene black to collapse, which lowers the conductivity. However, there is a problem that sufficient oxygen gas absorption performance cannot be obtained. If the coating layer is thickened to ensure conductivity, the oxygen gas permeability will deteriorate and the diffusion of the electrolyte will be hindered, which will not only reduce the oxygen gas absorption performance, but also the battery voltage characteristics during high-rate discharge. There was a problem that

【0006】本発明の目的は、上記問題点を除去し、酸
素ガス吸収性能を更に向上させ、高率放電特性にも優れ
たペースト式カドミウム陰極板を提供することにある。
An object of the present invention is to eliminate the above problems, to further improve the oxygen gas absorption performance, and to provide a paste type cadmium cathode plate which is excellent in high rate discharge characteristics.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
に、本発明のアルカリ蓄電池用ペースト式カドミウム陰
極板は、酸化カドミウム、水酸化カドミウム、金属カド
ミウムの1種以上を主活物質とする活物質層の表面に、
BET比表面積1000〜1500m2/g、フタル酸
ジブチル吸油量(以下「DBP吸油量」という)が3〜
5ml/gであるファーネスブラック粉末と熱ゲル化す
るセルロース誘電体糊料からなる導電層が設けられてい
ることを特徴とするものであって、熱ゲル化するセルロ
ース誘導体糊料として好敵にはメチルセルロース、ヒド
ロキシプロピルメチルセルロース、ヒドロキシプロピル
セルロースの内のいずれか、あるいはそれらを混合して
用いるものである。
In order to solve the above problems, the paste type cadmium cathode plate for an alkaline storage battery of the present invention has an active material containing at least one of cadmium oxide, cadmium hydroxide and metal cadmium as a main active material. On the surface of the material layer,
BET specific surface area of 1000 to 1500 m 2 / g, dibutyl phthalate oil absorption (hereinafter referred to as “DBP oil absorption”) is 3 to
A conductive layer comprising a furnace black powder of 5 ml / g and a heat-gelling cellulose dielectric paste is provided, which is favorably used as a heat-gelling cellulose derivative paste. Any one of methyl cellulose, hydroxypropyl methyl cellulose, hydroxypropyl cellulose, or a mixture thereof is used.

【0008】[0008]

【作用】本発明は、鋭意検討の結果、陰極板表面に設け
た導電層を高比表面積且つ高DBP吸油量のファーネス
ブラック粉末と熱ゲル化するセルロース誘導体糊料で構
成することによって、酸素ガス吸収性能がより一層向上
し、同時に高率放電特性も改善されることを見出したこ
とにもとづいている。高比表面積を有することは電解液
が浸透出来ないミクロ孔が多いことを示しており、酸素
ガスの導電層内での透過性が良いこと、高DBP吸油量
を有することは鎖状構造あるいは中空構造が発達してい
ることを示しており、導電層形成のための懸濁液作製時
の撹拌によっても導電性が低下せず、陰極板表面に金属
カドミウムを有効に生成させ得ること、また電解液の保
液性が良いため、高率放電時の電解液の拡散が良いこ
と、更に、熱ゲル化するセルロース誘導体糊料を用いる
ことによって、陰極板表面に上記懸濁液を塗布した後の
乾燥での塗布層の収縮、緻密化が抑制されるので、上記
のガス透過性と電解液保液性が保持されることが主な理
由と考えられる。
According to the present invention, as a result of intensive studies, the conductive layer provided on the surface of the cathode plate is composed of a furnace black powder having a high specific surface area and a high DBP oil absorption amount and a cellulose derivative paste which is heat-gelled to obtain an oxygen gas. It is based on the finding that the absorption performance is further improved, and at the same time, the high rate discharge characteristic is also improved. Having a high specific surface area indicates that there are many micropores that cannot penetrate the electrolyte, and that oxygen gas has good permeability in the conductive layer and that it has a high DBP oil absorption has a chain structure or a hollow structure. It shows that the structure is well developed, the conductivity is not deteriorated even by stirring during the preparation of the suspension for forming the conductive layer, and it is possible to effectively generate metal cadmium on the surface of the cathode plate. Since the liquid retaining property of the liquid is good, the diffusion of the electrolytic solution at the time of high-rate discharge is good, and further, by using the cellulose derivative paste which thermally gels, after applying the above suspension to the surface of the cathode plate, Since the shrinkage and the densification of the coating layer during drying are suppressed, it is considered that the main reason is that the above-mentioned gas permeability and electrolyte retaining property are maintained.

【0009】[0009]

【実施例】本発明の一実施例を説明する。 [実施例1]酸化カドミウム粉末、ナイロン補強繊維、
ポリビニルアルコール糊料、エチレングリコール溶媒を
混合してペースト状とし、これをニッケルメッキした鉄
穿孔板に塗着、乾燥する従来どおりの方法で作製したペ
ースト式カドミウム陰極板を、水酸化ナトリウム水溶液
中でニッケル板を対極として充放電することによって化
成し、次いで水洗、乾燥した。一方、水100重量部、
ファーネスブラック粉末a(比表面積1475m2
g、DBP吸油量3.3ml/g)5重量部、メチルセ
ルロース5重量部をスパイラルミキサーに投入し、15
0回転/分で1時間撹拌混合してカーボン粉末懸濁液を
作製した。化成したペースト式カドミウム陰極板の表面
にカーボン粉末懸濁液を6〜7mg/cm2の塗布量に
なるよう薄く塗布し、乾燥して完成陰極板を得た。この
陰極板をナイロン不織布セパレータを介して周知の方法
で作製された焼結式陽極板と組み合わせて捲回し、アル
カリ電解液と共に電池ケースに収容して公称容量120
0mAhの密閉型ニッケル・カドミウム電池Aを作製し
た。また、上記電池Aの陰極板表面のカーボン粉末塗布
層に用いたファーネスブラックaにかえて、ファーネス
ブラックb(比表面積1270m2/g、DBP吸油量
4.5ml/g)を用いた以外は同一構成の電池Bを作
製した。
EXAMPLE An example of the present invention will be described. [Example 1] Cadmium oxide powder, nylon reinforcing fiber,
A paste type cadmium cathode plate prepared by the conventional method of mixing a polyvinyl alcohol paste and an ethylene glycol solvent to form a paste, coating it on a nickel-plated iron perforated plate, and drying it in an aqueous sodium hydroxide solution. It was formed by charging and discharging a nickel plate as a counter electrode, then washed with water and dried. On the other hand, 100 parts by weight of water,
Furnace black powder a (specific surface area 1475 m 2 /
g, DBP oil absorption amount 3.3 ml / g) 5 parts by weight, and methyl cellulose 5 parts by weight were charged into a spiral mixer, and 15
A carbon powder suspension was prepared by stirring and mixing at 0 rpm for 1 hour. A carbon powder suspension was thinly applied to the surface of the formed paste type cadmium cathode plate so as to have a coating amount of 6 to 7 mg / cm 2 , and dried to obtain a completed cathode plate. This cathode plate was wound in combination with a sintered anode plate produced by a known method via a nylon non-woven fabric separator, and was wound together with an alkaline electrolyte in a battery case to have a nominal capacity of 120.
A 0 mAh sealed nickel-cadmium battery A was produced. Further, the furnace black b (specific surface area 1270 m 2 / g, DBP oil absorption of 4.5 ml / g) was used in place of the furnace black a used in the carbon powder coating layer on the surface of the cathode plate of the battery A. A battery B having a structure was produced.

【0010】[実施例2]実施例1の電池Aにおいて、
陰極板表面のカーボン塗布層に用いたメチルセルロース
糊料にかえて、ヒドロキシプロピルメチルセルロース及
びヒドロキシプロピルセルロースを用い、カーボン粉末
懸濁液の粘度が実施例1と同じになるよう調整した以外
は同一構成の電池C,Dを夫々作製した。
Example 2 In the battery A of Example 1,
Except that the methylcellulose paste used for the carbon coating layer on the surface of the cathode plate was replaced with hydroxypropylmethylcellulose and hydroxypropylcellulose, and the viscosity of the carbon powder suspension was adjusted to be the same as in Example 1, the same constitution was obtained. Batteries C and D were produced respectively.

【0011】[比較例1]実施例1において、陰極板の
表面にカーボン粉末塗布層を設けないで、その他は同一
構成の電池Eを作製した。
Comparative Example 1 A battery E having the same structure as in Example 1 except that the carbon powder coating layer was not provided on the surface of the cathode plate was manufactured.

【0012】[比較例2]実施例1において、陰極板表
面のカーボン塗布層に用いたファーネスブラックにかえ
て、アセチレンブラック(比表面積64m2/g、DB
P吸油量1.2ml/g)を用いた以外は同一構成の電
池Fを作製した。
[Comparative Example 2] In Example 1, instead of the furnace black used for the carbon coating layer on the surface of the cathode plate, acetylene black (specific surface area 64 m 2 / g, DB
A battery F having the same configuration was prepared except that a P oil absorption amount of 1.2 ml / g) was used.

【0013】[比較例3]実施例1の電池Aにおいて、
陰極板表面のカーボン塗布層を用いたメチルセルロース
糊料にかえて、熱ゲル化しないカルボキシメチルセルロ
ースを用い、カーボン粉末懸濁液の粘度が実施例1と同
じになるよう調整した以外は同一構成の電池Gを作製し
た。
[Comparative Example 3] In the battery A of Example 1,
Batteries having the same configuration except that carboxymethyl cellulose that did not gel heat was used in place of the methyl cellulose paste using the carbon coating layer on the surface of the cathode plate, and the viscosity of the carbon powder suspension was adjusted to be the same as in Example 1. G was made.

【0014】このようにして作製された電池A〜Gに開
口部を設け、圧力ゲージを密閉状態にして取り付けた。
その後、1.2A(1C)の電流で充電し、その時の電
池の内部圧力変化を測定した。2.5時間目の電池内部
圧力を表1に示す。また、充電を夫々1Cの電流で1.
5時間行った後、放電を1.2A、3.6A、6Aで行
った際の電池電圧1Vまでの放電容量も合わせて表1に
示す。
The batteries A to G thus produced were provided with an opening, and the pressure gauge was attached in a sealed state.
Then, the battery was charged with a current of 1.2 A (1 C), and the internal pressure change of the battery at that time was measured. Table 1 shows the battery internal pressure after 2.5 hours. In addition, charging is performed at a current of 1 C for each 1.
Table 1 also shows the discharge capacities up to a battery voltage of 1 V when discharged at 1.2 A, 3.6 A, and 6 A after 5 hours of discharge.

【0015】[0015]

【表1】 [Table 1]

【0016】表1からは次のようなことがわかる。The following can be seen from Table 1.

【0017】陰極板表面にカーボン塗布層を設けた電
池A〜D、F、Gはカーボン塗布層を設けていない電池
Eに比べ、明らかに電池内部圧力が低下しており、陰極
板の酸素ガス吸収性能が向上している。
Batteries A to D, F, and G having a carbon coating layer on the surface of the cathode plate had apparently lower battery internal pressures as compared with Battery E having no carbon coating layer, and the oxygen gas of the cathode plate was reduced. Absorption performance is improved.

【0018】陰極板表面のカーボン塗布層にBET比
表面積1000〜1500m2/g、DBP吸油量3〜
5ml/gのファーネスブラックを用いた本発明の電池
A〜Dはアセチレンブラックを用いた比較電池Fに比
べ、電池内部圧力が更に低くなっており、酸素ガス吸収
性能に優れている。また、高率放電における容量低下が
少なく優れている。
The carbon coating layer on the surface of the cathode plate has a BET specific surface area of 1000 to 1500 m 2 / g and a DBP oil absorption of 3 to
The batteries A to D of the present invention using 5 ml / g of furnace black have a lower battery internal pressure than the comparative battery F using acetylene black and are excellent in oxygen gas absorption performance. Further, it is excellent in that the capacity is not decreased in the high rate discharge.

【0019】陰極板表面のカーボン塗布層に熱ゲル化
するセルロース誘導体糊料を用いた本発明の電池A〜D
は熱ゲル化しないカルボキシメチルセルロース糊料を用
いた比較電池Gに比べ、電池内部圧力が更に低くなって
おり、酸素ガス吸収性能に優れている。また、高率放電
における容量低下が少なく優れている。
Batteries A to D of the present invention in which a heat-gelling cellulose derivative paste is used in the carbon coating layer on the surface of the cathode plate.
In comparison with Comparative Battery G, which uses a carboxymethyl cellulose paste that does not gel thermally, the internal pressure of the battery is even lower and the oxygen gas absorption performance is excellent. Further, it is excellent in that the capacity is not decreased in the high rate discharge.

【0020】以上のように、本発明の電池は比較例に比
べ、充電時の酸素ガス吸収性能に優れ、且つ高率放電性
能にも優れている。このことは、陰極板表面の導電層の
導電性が高いため、表面に金属カドミウムが生成し易
く、また、導電層のガス透過性と電解液の保液性が良い
という相反する性質を本発明の陰極板が兼ね備えている
ことを示すものである。
As described above, the battery of the present invention is superior to the comparative example in the oxygen gas absorption performance during charging and also in the high rate discharge performance. This is because the conductive layer on the surface of the cathode plate has high conductivity, metal cadmium is likely to be generated on the surface, and the gas permeability of the conductive layer and the liquid retaining property of the electrolytic solution are good. It is shown that the cathode plate of (1) has both.

【0021】[0021]

【発明の効果】上述したように、本発明に係るアルカリ
蓄電池用ペースト式カドミウム陰極板は、活物質層の表
面に高比表面積、高DBP吸油量を有するファーネスブ
ラック粉末と熱ゲル化するセルロース誘導体糊料からな
る導電層が設けられているため、従来の上記導電層にア
セチレンブラックを用いたものに比べ、陰極板の酸素ガ
ス吸収性能が更に向上し、高率放電においても容量低下
の少ないものである。この優れた特性は、導電層に用い
るカーボン粉末の物性と糊料の性質を目的に合わせて組
合せることによって初めて可能となったものである。
As described above, the paste-type cadmium cathode plate for an alkaline storage battery according to the present invention is a cellulose derivative which has a high specific surface area and a high DBP oil absorption amount on the surface of the active material layer and a thermal gelation. Since a conductive layer made of a paste is provided, compared with the conventional conductive layer using acetylene black, the oxygen gas absorption performance of the cathode plate is further improved, and the capacity is less reduced even at high rate discharge. Is. This excellent property is made possible only by combining the physical properties of the carbon powder used for the conductive layer and the properties of the paste according to the purpose.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 黒田 泰介 東京都新宿区西新宿2丁目1番1号 新神 戸電機株式会社内 (72)発明者 辻 裕貴 東京都新宿区西新宿2丁目1番1号 新神 戸電機株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Taisuke Kuroda 1-1-1, Nishi-Shinjuku, Shinjuku-ku, Tokyo Inside Shin-Kindo Electric Co., Ltd. (72) Inventor Yuuki Tsuji 2-1-1, Nishi-Shinjuku, Shinjuku-ku, Tokyo No. 1 Shinshin Todo Electric Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】酸化カドミウム、水酸化カドミウム、金属
カドミウムの少なくとも1種を主活物質とする活物質層
の表面に、カーボン粉末からなる導電層が設けられてい
る陰極板において、該導電層がBET比表面積1000
〜1500m2/g、DBP吸油量3〜5ml/gであ
るファーストブラック粉末と熱ゲル化するセルロース誘
電体糊料からなることを特徴とするアルカリ蓄電池用ペ
ースト式カドミウム陰極板。
1. A cathode plate in which a conductive layer made of carbon powder is provided on the surface of an active material layer containing at least one of cadmium oxide, cadmium hydroxide and metal cadmium as a main active material. BET specific surface area 1000
~1500m 2 / g, DBP oil absorption amount 3-5 ml / g in a first black powder and cellulose dielectric paste fee for an alkaline storage battery paste type cadmium negative electrode plate, characterized in that it consists of thermogelling.
【請求項2】熱ゲル化するセルロース誘導体糊料がメチ
ルセルロース、ヒドロキシプロピルメチルセルロース、
ヒドロキシプロピルセルロースの内のいずれか、あるい
はそれらを混合したものであることを特徴とする請求項
1記載のアルカリ蓄電池用ペースト式カドミウム陰極
板。
2. A heat-gelling cellulose derivative paste is methylcellulose, hydroxypropylmethylcellulose,
The paste type cadmium cathode plate for an alkaline storage battery according to claim 1, which is one of hydroxypropyl cellulose or a mixture thereof.
JP21768891A 1991-08-29 1991-08-29 Paste cadmium cathode plate for alkaline storage batteries Expired - Fee Related JP3178018B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21768891A JP3178018B2 (en) 1991-08-29 1991-08-29 Paste cadmium cathode plate for alkaline storage batteries

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21768891A JP3178018B2 (en) 1991-08-29 1991-08-29 Paste cadmium cathode plate for alkaline storage batteries

Publications (2)

Publication Number Publication Date
JPH0554891A true JPH0554891A (en) 1993-03-05
JP3178018B2 JP3178018B2 (en) 2001-06-18

Family

ID=16708166

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21768891A Expired - Fee Related JP3178018B2 (en) 1991-08-29 1991-08-29 Paste cadmium cathode plate for alkaline storage batteries

Country Status (1)

Country Link
JP (1) JP3178018B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0848441A1 (en) * 1996-12-13 1998-06-17 Akiya Kozawa An electrochemical cell employing a fine carbon material additive
JP2009035598A (en) * 2007-07-31 2009-02-19 Denki Kagaku Kogyo Kk Acetylene black, method for producing the same and use thereof
US7698956B2 (en) 2006-03-14 2010-04-20 Oval Corporation Coriolis flow meter with vibrating direction restriction means
KR20230029530A (en) 2021-08-23 2023-03-03 니타 가부시키가이샤 Coupling for pipe and its mounting method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0848441A1 (en) * 1996-12-13 1998-06-17 Akiya Kozawa An electrochemical cell employing a fine carbon material additive
US7698956B2 (en) 2006-03-14 2010-04-20 Oval Corporation Coriolis flow meter with vibrating direction restriction means
JP2009035598A (en) * 2007-07-31 2009-02-19 Denki Kagaku Kogyo Kk Acetylene black, method for producing the same and use thereof
KR20230029530A (en) 2021-08-23 2023-03-03 니타 가부시키가이샤 Coupling for pipe and its mounting method

Also Published As

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