JPS6178057A - Method for manufacturing alkaline battery - Google Patents

Method for manufacturing alkaline battery

Info

Publication number
JPS6178057A
JPS6178057A JP19952384A JP19952384A JPS6178057A JP S6178057 A JPS6178057 A JP S6178057A JP 19952384 A JP19952384 A JP 19952384A JP 19952384 A JP19952384 A JP 19952384A JP S6178057 A JPS6178057 A JP S6178057A
Authority
JP
Japan
Prior art keywords
battery
powder
pole mixture
alkaline
negative pole
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
JP19952384A
Other languages
Japanese (ja)
Inventor
Osamu Takahashi
修 高橋
Hitoshi Takagishi
高岸 仁
Kiyoshi Hosoda
細田 清志
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.)
FDK Twicell Co Ltd
Original Assignee
Toshiba Battery 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 Toshiba Battery Co Ltd filed Critical Toshiba Battery Co Ltd
Priority to JP19952384A priority Critical patent/JPS6178057A/en
Publication of JPS6178057A publication Critical patent/JPS6178057A/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
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • 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
    • H01M4/06Electrodes for primary cells
    • H01M4/08Processes of manufacture
    • H01M4/12Processes of manufacture of consumable metal or alloy electrodes

Landscapes

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

Abstract

PURPOSE:To prevent uneven charging amount of negative pole mixture by mixing zinc powder, anti-alkaline gelatinizing agent and soluble surface active agent and filling into a battery vessel and by injecting alkali electrolyte to form the negative pole mixture. CONSTITUTION:Zinc powder or zinc alloy powder, gelatinizing agent as polyacryal acid soda and soluble surface active agent of alkali metal salt such as di-n-octyl sulfosaxinate are mixed and filled into a sealing plate 7, and alkali electrolyte is injected to form gel type negative pole mixture 6. And it is com bined with positive pole mixture 2 containing manganese dioxide mainly, a separator 3 and a nonwoven fabric 4 to form an alkaline battery. Then, wetness of gelatinizing agent and alkali electrolyte is improved by surface active agent, and uniform negative pole mixture 6 can be obtained in a short time. And uneven filling amount is prevented to improve battery performance.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明はアルカリ電池の製造方法に関し、更に詳しくは
、重負荷放電特性が優れた・アルカリ電池の製造方法に
関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a method for manufacturing an alkaline battery, and more particularly to a method for manufacturing an alkaline battery with excellent heavy load discharge characteristics.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

アルカリ電池は概ね次のようにして製造されている。そ
れを図に示した構造のボタン型アルカリ電池を例として
説明する。
Alkaline batteries are generally manufactured as follows. This will be explained using a button-type alkaline battery having the structure shown in the figure as an example.

1は、正極端子も兼ねる外缶で通常二yケルメッキを施
した鉄で構成されている。この外缶1の底部には、酸化
銀若しくは二酸化マンガンのような正極活物質を所定の
形状に賦形した合剤成形体2が外缶1の内壁に密着して
収納される。つぎK、成形体2の上面に、例えば微孔性
ポリエチレンシートの両面にセロファンを積層して成る
厚み約0.1−のセパレータ3が載置され、ついで、七
ノくレータ3の上には不織布4が配設される。
1 is an outer can that also serves as a positive terminal, and is usually made of iron plated with 2YK. At the bottom of the outer can 1, a molded mixture 2 formed by shaping a positive electrode active material such as silver oxide or manganese dioxide into a predetermined shape is housed in close contact with the inner wall of the outer can 1. Next, on the upper surface of the molded body 2, a separator 3 with a thickness of about 0.1 mm, which is made by laminating cellophane on both sides of a microporous polyethylene sheet, is placed. A nonwoven fabric 4 is provided.

不織布4の上にはリング状の絶縁バッキング5を介し、
後述の負極合剤6を充填した陰極端子も兼ねる封口板7
が冠着され、最後に外缶1の開口縁を内側に折曲して全
体を緊締する。
A ring-shaped insulating backing 5 is placed on top of the nonwoven fabric 4,
A sealing plate 7 that also serves as a cathode terminal filled with a negative electrode mixture 6 to be described later.
is capped, and finally the opening edge of the outer can 1 is bent inward and the whole is tightened.

以上のような製造工程において、用いる負極合剤6及び
その電池内への充填は、従来、次のような態様をとって
いる。
In the manufacturing process as described above, the negative electrode mixture 6 used and its filling into the battery have conventionally taken the following manner.

すなわち、亜鉛粉末又は水化亜鉛粉末のような亜鉛合金
粉末を、ゲル化剤を用いて予めゲル状圧したアルカリ電
解液の中に分散させてゲル状負極合剤t−1i1[L、
このゲル状負極合剤から充填に必要な所定量を秤量して
それを電池に充填していた。
That is, a gelled negative electrode mixture t-1i1[L,
A predetermined amount necessary for filling was weighed out of this gelled negative electrode mixture and filled into the battery.

しかしながら、この充填方法の場合には、必要とするゲ
ル状負極合剤の正確な秤量が困難で充填量に大きなばら
つきが生ずる。
However, with this filling method, it is difficult to accurately weigh the required gelled negative electrode mixture, resulting in large variations in the filling amount.

このことは、電池の品質の安定化、規格の統一化の要請
からすれば、陰極、陽極の電気容量のバランスを大きく
とらなければならないことを不可避とする。しかしなが
ら、ボタン型アルカリ電池のよう区内容積が小さい電池
にとって、大きな電気容量バランスの設定は高電気容量
化を阻む要因の1つになる。また負極合剤の充填量のば
らつきは、電池の電気容量そのもののはらつきを招き、
放電特性の不均一化を招く。
This makes it inevitable that the electric capacities of the cathode and anode must be well balanced in view of the demands for stabilizing battery quality and unifying standards. However, for batteries with small internal volumes such as button-type alkaline batteries, setting a large capacitance balance is one of the factors that prevents high capacitance. In addition, variations in the filling amount of the negative electrode mixture lead to variations in the electric capacity of the battery itself.
This leads to non-uniform discharge characteristics.

このようなことから、最近では、亜鉛又は亜鉛合金の粉
末とポリアクリル酸ソーダのようなゲル化剤とを乾燥状
態で混合し、この乾燥混合粉末を所定量秤量してそれを
まず電池内に充填し、しかるのち、ここにアルカリ電解
液を注液して全体をゲル化するという方法が行なわれて
いる。
For this reason, recently, zinc or zinc alloy powder and a gelling agent such as sodium polyacrylate are mixed in a dry state, a predetermined amount of this dry mixed powder is weighed, and the mixture is first poured into a battery. The method used is to fill the container, and then inject an alkaline electrolyte into the container to gel the whole.

しかしながら、この方法の場合ゲル化剤の表面活性が小
さいので、アルカリ電解液を注液したとき両者のなじみ
が悪く、ゲル化剤が電解液を取り巻いた微小液滴を形成
して電解液の均一な分散に長時間を要したり、又はゲル
化剤が飛散したりする現象が頻発して電池組立工程に不
必要な工数増加を招いている。また、ゲル化剤が均一に
分散せず均質なゲル状負極合剤が形成されないので、得
られた電池の放電特性、とシわけ重負荷による放電特性
の低下及び貯蔵特性の低下をも引き起している。
However, in this method, the surface activity of the gelling agent is low, so when the alkaline electrolyte is injected, the two do not mix well, and the gelling agent forms minute droplets surrounding the electrolyte, resulting in a uniform electrolyte. Phenomena in which it takes a long time for the gelling agent to be dispersed or the gelling agent is scattered frequently occur, resulting in an unnecessary increase in the number of man-hours in the battery assembly process. In addition, since the gelling agent is not uniformly dispersed and a homogeneous gelled negative electrode mixture is not formed, the discharge characteristics of the resulting battery deteriorate, particularly due to heavy loads and storage characteristics. are doing.

〔発明の目的〕[Purpose of the invention]

本発明は、ゲル状負極合剤を用いるアルカリ電池におい
て、上記した問題点を解消し、組立時の作業性が浸れ、
重負荷放電特性が向上し、初期電気容量大、貯蔵寿命が
長いアルカリ電池を製造する方法の提供を目的とする。
The present invention solves the above-mentioned problems in an alkaline battery using a gel negative electrode mixture, improves workability during assembly, and
The purpose of the present invention is to provide a method for manufacturing an alkaline battery that has improved heavy load discharge characteristics, a large initial electric capacity, and a long shelf life.

〔発明の概要〕[Summary of the invention]

本発明のアルカリ電池の製造方法は、亜鉛粉末又は亜鉛
合金粉末と、耐アルカリ性ゲル化剤と、水溶性界面活性
剤とを混合し、得られた混合粉末を電池容器の所定個所
に充填し、ついでそこにアルカリ電解液を注液すること
を特徴とする。
The method for manufacturing an alkaline battery of the present invention includes mixing zinc powder or zinc alloy powder, an alkali-resistant gelling agent, and a water-soluble surfactant, and filling the resulting mixed powder into a predetermined portion of a battery container. The method is characterized in that an alkaline electrolyte is then injected therein.

本発明方法は、ゲル化剤とアルカリ電解液との濡れを水
溶性界面活性剤で向上せしめ、もって前述したような問
題を解消することに技術思想の基礎を置く。
The technical concept of the method of the present invention is based on improving the wetting between the gelling agent and the alkaline electrolyte using a water-soluble surfactant, thereby solving the above-mentioned problems.

まず、亜鉛粉末又は亜鉛合金粉末は、従来からアルカリ
電池の負極として用いられているようなものでよく格別
限定されるものではない。亜鉛合金としては、所定量の
水銀で処理した氷化亜鉛。
First, the zinc powder or zinc alloy powder may be one that has been conventionally used as a negative electrode for alkaline batteries, and is not particularly limited. As a zinc alloy, frozen zinc is treated with a specified amount of mercury.

鉛、インジウム、ガリウムなどを0.01〜1.0重量
%含有する亜鉛合金がめげられる。これらの粉末は通常
40〜250メツシユ(タイラーIII)で用いられる
Zinc alloys containing 0.01 to 1.0% by weight of lead, indium, gallium, etc. are preferred. These powders are typically used in 40 to 250 mesh (Tyler III).

耐アルカリ性ゲル化剤としては、ポリアクリル酸ソーダ
など従来から用いられているものでよい。
As the alkali-resistant gelling agent, conventionally used ones such as sodium polyacrylate may be used.

ゲル化剤の配合量は得られた負毬合剤全体の重量に対し
通常5重量%以内、好ましくは0.2〜2重量%である
The blending amount of the gelling agent is usually within 5% by weight, preferably 0.2 to 2% by weight, based on the total weight of the obtained negative mold mixture.

つぎに1水溶性界面活性剤としては上記ゲル化剤とアル
カリ電解液との濡れを向上せしめるものであればなくて
あってもよいが、少量の使用でもその効果が発揮される
ということからして、ジ−n−オクチルスルホサクシネ
ートのアルカリ金属塩、ジノニルナフタレンスルホネー
トのアルカリ金属塩のそれぞれ1種又は2種以上である
ことが好ましい。
Next, 1. The water-soluble surfactant may be omitted as long as it improves the wetting between the gelling agent and the alkaline electrolyte, but its effect is exhibited even when used in small amounts. Preferably, one or more of an alkali metal salt of di-n-octyl sulfosuccinate and an alkali metal salt of dinonylnaphthalene sulfonate are used.

これらの塩におけるアルカリ金属としては、ナトリウム
、カリウム、リチウム、セシウムなどがあげられるが、
とりわけナトリウム、カリウムは好適である。
Alkali metals in these salts include sodium, potassium, lithium, cesium, etc.
Particularly suitable are sodium and potassium.

これらの塩はそれぞれ単独で用いられてもよいし、適宜
に2s以上を併用してもよい。配合量は、得られた負極
合剤の全体重量に対し0.02〜0,5重量%でよい。
Each of these salts may be used alone, or 2s or more may be used in combination as appropriate. The blending amount may be 0.02 to 0.5% by weight based on the total weight of the obtained negative electrode mixture.

あまり多く用いると、混合時に発泡する。If too much is used, it will foam during mixing.

本発明方法にあっては、まず、上記3成分を混合する。In the method of the present invention, first, the above three components are mixed.

混合の順序は格別限定されるものではないが、乾燥状態
にある亜鉛粉末又は亜鉛合金粉末とゲル化剤の粉末とを
混合し、ここに水溶性界面活性剤を所定量配合して更に
混合するという方法が好ましい。
The order of mixing is not particularly limited, but dry zinc powder or zinc alloy powder and gelling agent powder are mixed, a predetermined amount of water-soluble surfactant is added thereto, and the mixture is further mixed. This method is preferable.

このようKして得られた混合粉末を、所定量秤量したの
ちそれを既に図で示した負極合剤の収納個所に充填する
After weighing a predetermined amount of the mixed powder thus obtained, it is filled into the negative electrode mixture storage location already shown in the figure.

この充填作業に先立って、上記混合粉末を相対湿度56
〜95チKU4湿されている恒湿槽の中に例えば1〜2
4時間放置してゲル化剤に湿気を与え、しかるのちに1
全体をほぐしながら乾燥することが好ましい。このよう
な処理を施すと、混合粉末におけるゲル化剤と界面活性
剤とが相互に均質・安定化して混合粉末の流動性が向上
し、もって充填時の秤量操作で計量ばらつきが小さくな
りて有用である。
Prior to this filling operation, the mixed powder was heated at a relative humidity of 56°C.
~95cm KU4 For example, 1~2 pieces in a humidified chamber.
Leave it for 4 hours to moisten the gelling agent, then add 1
It is preferable to dry the entire product while loosening it. When this kind of treatment is applied, the gelling agent and surfactant in the mixed powder become mutually homogeneous and stable, improving the fluidity of the mixed powder, which is useful because it reduces the measurement variation during the weighing operation during filling. It is.

電池に混合粉末を充填後、そこに所定量のアルカリ電解
液を注液する。既に均質に存在する水溶性界面活性剤の
作用により、ゲル化剤は飛散することなく分散し、電解
液本短時間で混合粉末に円滑に湿潤して全体が均質なゲ
ル状負極合剤となる。
After filling the battery with the mixed powder, a predetermined amount of alkaline electrolyte is poured into it. Due to the action of the water-soluble surfactant, which is already homogeneous, the gelling agent is dispersed without scattering, and the electrolyte is smoothly wetted with the mixed powder in a short time, forming a homogeneous gel-like negative electrode mixture as a whole. .

最後にセパレータ3、不織布4及び絶縁バッキング5を
介し、正極活物質を内壁に密着した電池外缶1と嵌合し
て、この上に封口板を冠着し全体を緊締して本発明のア
ルカリ電池が製造される。
Finally, the positive electrode active material is fitted to the battery outer case 1 which is tightly attached to the inner wall via the separator 3, the non-woven fabric 4 and the insulating backing 5, and a sealing plate is attached on top of this and the whole is tightened. Batteries are manufactured.

〔発明の実施列〕[Implementation sequence of the invention]

実施fill〜4 (1)電池の製造 粒度48〜100メツシユ(タイラー篩)の10重量%
汞化亜鉛粉末98りにポリアクリル酸ソーダ2fを添加
して両者を混合し、ついでここに表示した界面活性剤を
表の割合いくなるように添加し、全体を充分く混合した
。得られた混合粉末を相対湿度70チに調湿された恒湿
槽に15時間放置し、ついでこれを30〜60℃でほぐ
し乾燥した。
Implementation fill ~ 4 (1) Production of battery Particle size: 10% by weight of 48-100 mesh (Tyler sieve)
2 f of sodium polyacrylate was added to 98 g of zinc chloride powder, and the two were mixed. Then, the surfactant shown here was added in the proportion shown in the table, and the whole was thoroughly mixed. The obtained mixed powder was left in a constant humidity tank adjusted to a relative humidity of 70 degrees for 15 hours, and then loosened and dried at 30 to 60°C.

混合粉末を所定量(電池1個分)秤量し、図のボタン型
酸化銀アルカリ電池の封口板に充填し、更にここに酸化
亜鉛が溶解されている26重量%の苛性ソーダ電解液を
注液した。粉末飛散、液滴形成のような現象は与られな
かった。
A predetermined amount (for one battery) of the mixed powder was weighed and filled into the sealing plate of the button-type silver oxide alkaline battery shown in the figure, and a 26% by weight caustic soda electrolyte in which zinc oxide was dissolved was poured into the sealing plate. . No phenomena such as powder scattering or droplet formation were observed.

最後に電池外缶1と共に全体を緊締してボタン型酸化銀
アルカリ電池5R626SWを製造した。なお、比較の
ため罠界面活性剤を用いなかったことを除いては実施列
と同様の手順で同型の電池を製造した。
Finally, the entire battery together with the outer battery case 1 was tightened to produce a button-type silver oxide alkaline battery 5R626SW. For comparison, a battery of the same type was manufactured in the same manner as in the experimental series, except that no trap surfactant was used.

(2)性能 以下の項目を測定した。すなわち、囚混合粉末を電池に
充填する際の、充填量及びそのばらつき、■各taの2
0℃、30KQ定抵抗放電において1゜2Vになるまで
の放電持続時間、0各電池を60℃で表示の期間貯蔵し
たのちの放電持続時間、0放電深度O%、40%、80
%における各電池を一10℃で2時間放置し、ついで同
じ温度下で2KQの負荷をかけて5秒間放電した時の5
秒後の閉路電圧である。
(2) Performance The following items were measured. In other words, the filling amount and its dispersion when filling the battery with the mixed powder, ■ 2 of each ta
Discharge duration until 1°2V in 30KQ constant resistance discharge at 0℃, 0Discharge duration after storing each battery at 60℃ for the indicated period, 0Depth of discharge O%, 40%, 80
%, each battery was left at -10℃ for 2 hours, and then discharged for 5 seconds under the same temperature with a load of 2KQ.
This is the closed circuit voltage after seconds.

以上の結果を一括して表に示した。なお、表中、囚は秤
量回数100回の平均値とばらつき、(B)は電池10
個の平均値、(C5は貯蔵前の各電池の放電持続時間を
100としたときの相対値、■は電池20個の平均値を
表わす。
The above results are summarized in the table. In addition, in the table, the value is the average value of 100 weighings and the variation, and (B) is the average value of 100 weighings.
(C5 is a relative value when the discharge duration of each battery before storage is set as 100, ■ represents the average value of 20 batteries.

〔発明の効果〕〔Effect of the invention〕

以上の結果から明らかなように、本発明方法によれば、
短時間で負極合剤を均質なゲル状にでき、しかも電池内
への充填量のばらつきを小さくすることが可能で、もっ
て重負荷による放電特性が優れ、放電持続時間も安定し
て長く、貯R4!性も良好なアルカリ電池を効率よく製
造することができる。また、負極合剤を電池に充填する
際にも、ゲル化剤の飛散、液滴化などの現象も解消する
ので電池組立工程における工数低減1作業性向上などの
効果も得られ生産性向上に資すること大である。
As is clear from the above results, according to the method of the present invention,
The negative electrode mixture can be made into a homogeneous gel in a short time, and the variation in the amount filled into the battery can be reduced, resulting in excellent discharge characteristics under heavy loads, a stable and long discharge duration, and a long storage life. R4! Alkaline batteries with good properties can be efficiently produced. Additionally, when filling batteries with the negative electrode mixture, phenomena such as scattering and droplet formation of the gelling agent are eliminated, resulting in reduced man-hours and improved workability in the battery assembly process, resulting in improved productivity. It is a great contribution.

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

図は、本発明方法を説明するために示したボタン型アル
カリ電池の断面図である。 1・・・電池外缶    2・・・正極合剤3・・・セ
パレータ   4・・・不織布5・・・絶縁バッキング
 6・・・ゲル状負極合剤7・・・封口板
The figure is a sectional view of a button-type alkaline battery shown for explaining the method of the present invention. 1...Battery outer can 2...Positive electrode mixture 3...Separator 4...Nonwoven fabric 5...Insulating backing 6...Gel-like negative electrode mixture 7...Sealing plate

Claims (1)

【特許請求の範囲】 1、亜鉛粉末又は亜鉛合金粉末と、耐アルカリ性ゲル化
剤と、水溶性界面活性剤とを混合し、得られた混合粉末
を電池容器の所定個所に充填し、ついでそこにアルカリ
電解液を注液することを特徴とするアルカリ電池の製造
方法。 2、該水溶性界面活性剤が、ジ−n−オクチルスルホサ
クシネートのアルカリ金属塩、ジノニルナフタレンスル
ホネートのアルカリ金属塩の群から選ばれる少なくとも
1種である特許請求の範囲第1項記載の方法。 3、該亜鉛合金粉末が、水銀、ガリウム、インジウム、
鉛の群から選ばれる少なくとも1種を含有する亜鉛合金
の粉末である特許請求の範囲第1項記載の方法。 4、該混合粉末を恒湿槽で湿潤処理し、ついでほぐし乾
燥を施したのち、電池容器の所定個所に充填する特許請
求の範囲第1項記載の方法。
[Claims] 1. Mix zinc powder or zinc alloy powder, an alkali-resistant gelling agent, and a water-soluble surfactant, fill the resulting mixed powder into a predetermined location of a battery container, and then fill it there. A method for producing an alkaline battery, which comprises injecting an alkaline electrolyte into the battery. 2. The water-soluble surfactant according to claim 1, wherein the water-soluble surfactant is at least one selected from the group of alkali metal salts of di-n-octylsulfosuccinate and alkali metal salts of dinonylnaphthalenesulfonate. Method. 3. The zinc alloy powder contains mercury, gallium, indium,
The method according to claim 1, which is a powder of a zinc alloy containing at least one member selected from the group of lead. 4. The method according to claim 1, wherein the mixed powder is moistened in a humidity chamber, then loosened and dried, and then filled into a predetermined location of a battery container.
JP19952384A 1984-09-26 1984-09-26 Method for manufacturing alkaline battery Pending JPS6178057A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19952384A JPS6178057A (en) 1984-09-26 1984-09-26 Method for manufacturing alkaline battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19952384A JPS6178057A (en) 1984-09-26 1984-09-26 Method for manufacturing alkaline battery

Publications (1)

Publication Number Publication Date
JPS6178057A true JPS6178057A (en) 1986-04-21

Family

ID=16409241

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19952384A Pending JPS6178057A (en) 1984-09-26 1984-09-26 Method for manufacturing alkaline battery

Country Status (1)

Country Link
JP (1) JPS6178057A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH074652U (en) * 1993-06-18 1995-01-24 繁雄 白銀 Safety fence for fall prevention

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH074652U (en) * 1993-06-18 1995-01-24 繁雄 白銀 Safety fence for fall prevention

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