JPS58155657A - Manufacture of alkaline battery - Google Patents

Manufacture of alkaline battery

Info

Publication number
JPS58155657A
JPS58155657A JP57038578A JP3857882A JPS58155657A JP S58155657 A JPS58155657 A JP S58155657A JP 57038578 A JP57038578 A JP 57038578A JP 3857882 A JP3857882 A JP 3857882A JP S58155657 A JPS58155657 A JP S58155657A
Authority
JP
Japan
Prior art keywords
steel
case
sulfuric acid
solution containing
washed
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
JP57038578A
Other languages
Japanese (ja)
Inventor
Akio Nagamine
長嶺 秋夫
Kojiro Miyasaka
宮坂 幸二郎
Nobuaki Chiba
千葉 信昭
Hitomi Sato
ひとみ 佐藤
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 JP57038578A priority Critical patent/JPS58155657A/en
Publication of JPS58155657A publication Critical patent/JPS58155657A/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
    • H01M4/661Metal or alloys, e.g. alloy 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
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • 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)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Cell Electrode Carriers And Collectors (AREA)
  • Primary Cells (AREA)

Abstract

PURPOSE:To reduce evolution of hydrogen gas, prevent electrolyte leakage, increase of impedance, rupture, and increase a battery life by cleaning the surface of copper or copper alloy, which is to be in contact with a negative active mass, of a negative current collector with a chemical polishing solution of hydrogen peroxide and sulfuric acid family, and then applying rust preventing treatment with a solution containing a rust preventive. CONSTITUTION:A reverse curl portion 5 of the circumference of a negative case 4 is covered with a synthetic resin jig 6. This case is treated with a chemical polishing solution containing 10mol of hydrogen peroxide and about 0.45mol of sulfuric acid for about 2min at room temperature. Then this case is washed with water, washed with a solution containing sulfuric acid, washed with water, nutralized, and washed with water again. By this treatment, the exposed surface of copper is polished chemically, and harmful foreign matter is removed. This cleaned case is immersed immediately in a solution containing 0.1% of benzotriazole as a rust preventive for about 15sec at 80 deg.C to form a rust preventing film, then the jig 6 is removed and the case 4 is dried.

Description

【発明の詳細な説明】 この発明は、酸化銀、二酸化マンガン等を正極活物質、
亜鉛等を負極活物質としアルカリ電解液を用いるアルカ
リ電池の製造方法に関するものである。
Detailed Description of the Invention This invention uses silver oxide, manganese dioxide, etc. as a positive electrode active material.
The present invention relates to a method for manufacturing an alkaline battery using zinc or the like as a negative electrode active material and an alkaline electrolyte.

一般にアルカリ電池は正極端子を兼ねる金属製正極容器
内に正極活物質、負極端子を兼ねる金属製負極容器内に
負極活物質環よびアルカリ電解液を充填した後、セパレ
ータを介在させ5合成高分子等からなる絶縁ガスケット
を介して両容器を嵌合し、正極容器の開口部を内方に彎
曲させて密封口している。
Generally, in an alkaline battery, a positive electrode active material is filled in a metal positive electrode container that also serves as a positive electrode terminal, a negative electrode active material ring and an alkaline electrolyte are filled in a metal negative electrode container that also serves as a negative electrode terminal, and then a separator is interposed between the two. The two containers are fitted together via an insulating gasket consisting of the following, and the opening of the positive electrode container is bent inward to form a hermetically sealed opening.

例えばボタン形酸化銀電池の場合、一般に負極容器は、
ステンレススチールと鋼または鋼合金との2層クラツド
板、あるいはニッケル、ステンレススチール、鋼または
銅合金の三層クラツド板を銅または鋼合金の側が容器の
内面になるように絞り加工して製造したものである。
For example, in the case of button-type silver oxide batteries, the negative electrode container is generally
Manufactured by drawing a two-layer clad plate of stainless steel and steel or steel alloy, or a three-layer clad plate of nickel, stainless steel, steel, or copper alloy so that the copper or steel alloy side becomes the inner surface of the container. It is.

このようにして製造した負極容器の鋼または鋼合金面に
はクラツド板の製造工程、スリット加工。
The steel or steel alloy surface of the negative electrode container manufactured in this way is subjected to the clad plate manufacturing process and slit processing.

打抜き絞り加工等の工程で、酸化物の生成、汚れやゴミ
の付着あるいはステンレス、ニッケル等の金属の微細片
が付着したりすることを避けることができない。電池組
立前には脱脂洗滌等の前処理を行なうが、これらの異物
が銅または銅合金面のキズに入ったり、付着後プレスさ
れた場合には通常の洗滌等の手段ではこれらを完全に除
去することは困難である。
In processes such as punching and drawing, it is impossible to avoid the formation of oxides, the adhesion of dirt and dust, and the adhesion of minute pieces of metal such as stainless steel and nickel. Before battery assembly, pretreatment such as degreasing and cleaning is performed, but if these foreign substances get into scratches on the copper or copper alloy surface, or if they are pressed after adhesion, they cannot be completely removed by normal cleaning or other means. It is difficult to do so.

負極容器の銅または銅合金面はアルカリ電解液のあるこ
とにより、負極活物質の氷化亜鉛と接触してアマルガム
化と亜鉛メッキとが行なわれる。
Due to the presence of an alkaline electrolyte, the copper or copper alloy surface of the negative electrode container comes into contact with the frozen zinc of the negative electrode active material to undergo amalgamation and galvanization.

このため、鋼または銅合金は亜鉛より責であるにもかか
わらず、亜鉛と接触しても水素ガス発生は抑制されるの
で、電池を密封口することができる。
Therefore, even though steel or copper alloy is more dangerous than zinc, hydrogen gas generation is suppressed even if it comes into contact with zinc, so the battery can be sealed.

しかし、ステンレススチール、ニッケル等の異物が銅ま
たは銅合金面に残っていると、これらの異物には氷化と
亜鉛メッキとが行われにくいため。
However, if foreign substances such as stainless steel or nickel remain on the copper or copper alloy surface, it is difficult for these foreign substances to freeze and galvanize.

そのまま露出した状態で残る。これらの金属は水素過電
圧が小さいので、負極容器にアルカリ溶液と亜鉛とが充
填された場合、水素ガスを発生する。
It remains exposed. Since these metals have a small hydrogen overvoltage, they generate hydrogen gas when the negative electrode container is filled with an alkaline solution and zinc.

したがって1組立て後電池内部に水素ガスが充易い構造
は、電池としての重大な欠陥である。
Therefore, a structure in which hydrogen gas easily fills inside the battery after one assembly is a serious defect as a battery.

この発明は上記の事情に基づきなされたもので。This invention was made based on the above circumstances.

負極集電体の負極活性物質と接触する鋼または銅合金を
、過酸化水素、硫酸系の化学研摩液で研摩して清浄化し
た後、鋼または鋼合金の防錆剤を含む水溶液により防錆
処理をほどこすこさにより。
After cleaning the steel or copper alloy that comes into contact with the negative electrode active material of the negative electrode current collector with a hydrogen peroxide or sulfuric acid-based chemical polishing solution, it is rust-prevented with an aqueous solution containing a steel or steel alloy rust inhibitor. Depending on the level of processing.

水素ガスの発生、が少なくしたがって漏液、インピーダ
ンスの増加、破裂等がなく寿命を長期化することのでき
るアルカリ電池の製造方法を提供しようとするものであ
る。
It is an object of the present invention to provide a method for manufacturing an alkaline battery that generates less hydrogen gas and therefore has a longer life without leakage, increased impedance, bursting, etc.

すなわち、負極容器の鋼または鋼合金に付着した金属の
微細片等の異物は通常の洗滌法では除去が困難であるか
ら、これらの有害な異物を鋼または銅合金の表面をある
厚さまでけずり取ることにより解決したものである。
In other words, since it is difficult to remove foreign substances such as minute pieces of metal attached to the steel or steel alloy of the negative electrode container using normal cleaning methods, these harmful foreign substances are scraped off to a certain thickness on the surface of the steel or copper alloy. The problem was solved by this.

この研−により除去する厚さは1面の汚れや異ド板全体
の厚さの10%程度が標準的であり、したがってクラツ
ド板が薄い場合は鋼または鋼合金層もまた薄くなり、け
ずり取る厚さも制限される。
The standard thickness to be removed by this polishing is about 10% of the total thickness of the dirt or foreign plate on one side. Therefore, if the clad plate is thin, the steel or steel alloy layer will also be thinner and should be removed. Thickness is also limited.

クラツド板の厚さがQ、3mmの場合は、鋼または鋼合
金の厚さは30μ程度が一般的であり、10岸程度けず
り取っても内側のステンレススチール層が露出するおそ
れはないが、けずり取るための費用がかさみ実用的でな
い。負極容器の鋼または鋼合金面にステンレススチール
、ニッケル等の異物が付着したり打込まれている深さは
、深いものでも3〜5声程度であり、6μ程度けずり取
ることのできることが確認された。
When the thickness of the cladding plate is Q, 3mm, the thickness of the steel or steel alloy is generally about 30μ, and there is no risk of exposing the inner stainless steel layer even if it is scraped off by about 10 sides, but It is expensive and impractical to take. It has been confirmed that the depth at which foreign matter such as stainless steel, nickel, etc. is attached to or embedded in the steel or steel alloy surface of the negative electrode container is about 3 to 5 degrees deep, and that it is possible to scrape off about 6 μm. Ta.

この場合に銅または鋼合金面をけずり取る手段としては
、けずり取る厚さを比較的容易に管理できるという点で
化学研摩が適当である。さらに具体的には、過酸化水素
、硫酸系化学研摩剤を用いるの力?、過酸化水素と硫酸
の組成、処理温度右よび時間を選ぶことにより、けずり
敗る厚さを的確に管理できる特長がある。
In this case, chemical polishing is suitable as a means for scraping the copper or steel alloy surface, since the thickness of the scraping can be controlled relatively easily. More specifically, the power of using hydrogen peroxide, sulfuric acid-based chemical abrasives? By selecting the composition of hydrogen peroxide and sulfuric acid, treatment temperature and time, the thickness of the process can be precisely controlled.

異物を除去した後の銅または鋼合金面はそのま接触した
場合、汞化と亜鉛メッキが行なわれるtでに時間がかか
り、それ才での間は鋼または鋼合金面から水素ガスを発
生する。負極容器に汞化亜鉛およびアルカリ電解液を充
填後すぐに電池を組立てるので、水素ガスの発生は電池
組立後まで続くことになる。電池の内部で水素ガスが発
生するとそのインピーダンスを増加させあるいは内圧の
増加による漏液の原因となる。
If the copper or steel alloy surface is brought into contact with the surface after foreign matter has been removed, it will take time for the oxidation and galvanization to take place, and hydrogen gas will be generated from the steel or steel alloy surface. . Since the battery is assembled immediately after filling the negative electrode container with zinc chloride and alkaline electrolyte, hydrogen gas generation continues until after the battery is assembled. When hydrogen gas is generated inside the battery, it increases its impedance or causes leakage due to an increase in internal pressure.

そこで、この発明においては、化学研摩剤により研摩し
て洗浄化した後この清浄面に対し鋼または銅合金の防錆
剤を含む水溶液により防錆処理をほどこし防錆被膜を形
成した後水化亜鉛とアルカリ電解液きを充填することに
より水素ガスの発生を防止している。この場合に、防錆
剤としては。
Therefore, in this invention, after polishing and cleaning with a chemical abrasive, this clean surface is subjected to rust prevention treatment with an aqueous solution containing a steel or copper alloy rust preventive agent to form a rust preventive film, and then zinc hydrate The generation of hydrogen gas is prevented by filling the tank with alkaline electrolyte. In this case, as a rust inhibitor.

銅または鋼合金の防錆剤として一般に使用されているト
リアゾール誘導体を用いることができる。
Triazole derivatives commonly used as rust inhibitors for copper or steel alloys can be used.

なお、負極容器は一般に絞り加工によって周辺に折返し
部を設けた形状となっていて、この折返し部を形成する
際折り返し部付近は銅または鋼合金の加工度が大きいた
め引き延ばされて他の部分より薄くなっている。したが
ってこの部分を化学研摩液でけずり収るとステンレスス
チールが講出しこれが原因で水素ガスを発生するおそれ
がある。
In addition, the negative electrode container is generally shaped with a folded part around the periphery by drawing processing, and when forming this folded part, the copper or steel alloy around the folded part is stretched to a high degree of processing, and other parts are It is thinner than the other parts. Therefore, if this part is scraped with a chemical polishing solution, the stainless steel may become exposed, which may generate hydrogen gas.

しかしながら、この発明においては折り返し部を避けて
化学研摩を行なうものであるから、このような点におい
ても水素ガス発生防止に対する配慮がなされている。
However, in this invention, since chemical polishing is performed while avoiding the folded portion, consideration is given to prevention of hydrogen gas generation in this respect as well.

次に図面を参照してこの発明の一実施例を説明する。Next, an embodiment of the present invention will be described with reference to the drawings.

第1図に示すような、全体の厚さが0.3mmで鋼のI
lす、6(30μのニッケル1.ステンレススチール2
、@3よりなる三層クラツド板を使用し、これを絞り加
工して負極容器4を製作する。
As shown in Figure 1, the steel I
l, 6 (30μ nickel 1. stainless steel 2)
, @3 is used and drawn to produce the negative electrode container 4.

この負極容器4の周辺折返し部5に合成樹脂製の治具6
を当接して表面を覆った後、過酸化水素中和、水洗を繰
返して露出している鋼3の表面を化学的にけずり取り、
異物を除去して清浄にする。
A jig 6 made of synthetic resin is attached to the peripheral folded part 5 of this negative electrode container 4.
After contacting the steel 3 to cover the surface, the exposed surface of the steel 3 is chemically scraped off by repeating hydrogen peroxide neutralization and water washing.
Remove foreign objects and clean.

この洗浄面をたた゛ちに防錆剤としてのベンゾトリアゾ
ール0゜1慢を含む水溶液中に浸漬し80℃で約15秒
間処理し、防錆被膜を形成した後治具6を外して水洗乾
燥した。鋼面をけずり取る厚さは平均して約6声とする
The cleaned surface was then immersed in an aqueous solution containing 0.1% benzotriazole as a rust preventive agent and treated at 80°C for about 15 seconds to form a rust preventive film, after which the jig 6 was removed and washed with water and dried. The thickness of the steel surface to be scraped is approximately 6 tones on average.

の正極容器、8は酸化銀活物質に電導剤として黒鉛を添
加し形成した陽極合剤、9はイオン透過性のセパレータ
、10はアルカリ電解液を含浸させた多孔性繊維物質か
らなる電解液保持材、11は負極活物質としての氷化亜
鉛である。12は正極容器7と負極容器4との間を絶縁
するとともにその間隙を密封する絶縁バッキングで、正
極容器lの開口部を内側に彎曲させてこれを締着してい
る。
8 is an anode mixture formed by adding graphite as a conductive agent to a silver oxide active material, 9 is an ion-permeable separator, and 10 is an electrolyte holder made of a porous fiber material impregnated with an alkaline electrolyte. Material 11 is frozen zinc as a negative electrode active material. Reference numeral 12 denotes an insulating backing that insulates the space between the positive electrode container 7 and the negative electrode container 4 and seals the gap therebetween, and the opening of the positive electrode container 1 is curved inward to fasten the backing.

図中13は頃体である。13 in the figure is the body.

このようにして作った電池0を含む各種の処理ただけの
ものを用いて組立てた従来の電池ηとをマ漏液の点につ
いて対比した。すなわち第1表は、これらの電池を温度
60℃、湿度90嗟の試験槽中ζこ貯蔵し、10倍の顕
微鏡を用いてそれぞれ1000個について漏液したもの
の個数を示したものである。
The battery 0 produced in this way was compared with a conventional battery η assembled using only various treatments in terms of leakage. That is, Table 1 shows the number of cells that leaked out of each 1000 cells stored in a test tank at a temperature of 60.degree. C. and a humidity of 90 minutes using a 10x microscope.

以下余白 第  1  表 また第2表は、温度45℃、湿度90%で3ケ月貯蔵し
た電池の水素ガス発生等に基づく高さの変化を調べ、そ
れぞれ試験電池1,000個中膨らんで0.5mm以と
高くなった電池の個数を示したものである。
Tables 1 and 2 show changes in height due to hydrogen gas generation, etc. of batteries stored for 3 months at a temperature of 45°C and humidity of 90%, and swelled to 0.0% among 1,000 test batteries. This figure shows the number of batteries whose height is 5 mm or more.

以下余白 第  2  表 第1表によると、従来品萌の場合には貯蔵日数20日で
漏洩が始まり日数の増加とともに急激に増加して行くの
に対し、この発明による電池囚〜閲の場合には貯蔵日数
30日で少ない価数の漏液が始まり1日数が増加しても
従来品ηの場合に比して漏液するものの数は著しく少な
い。
According to Table 1, in the case of the conventional product Moe, leakage begins after 20 days of storage and rapidly increases as the number of days increases, whereas in the case of the battery cell battery according to the present invention, The leakage of a small number of liquids started after 30 days of storage, and even if the number of days increased, the number of liquids leaking was significantly smaller than in the case of the conventional product η.

また第2表によれば、従来品(ト)の場合の不良の数に
比してこの発明−こよる電池四〜(6)の場合には約1
/9以下に抑えることができる。
Also, according to Table 2, compared to the number of defects in the case of the conventional product (G), the number of defects in the case of batteries 4 to (6) according to the present invention is about 1.
/9 or less.

なお、第1表および@2表を通じ、過酸化水素8〜10
モル、硫酸0.25〜0.6モル、過酸化水素に対る一
硫酸のモル比が0.03〜0.06の範囲に含まれる(
ハ)〜0の場合が特に良好な試験結果が得られることを
知ることができる。
In addition, through Table 1 and @Table 2, hydrogen peroxide 8 to 10
mol, sulfuric acid 0.25 to 0.6 mol, the molar ratio of monosulfuric acid to hydrogen peroxide is in the range of 0.03 to 0.06 (
It can be seen that particularly good test results can be obtained in the case of c) ~0.

化学研磨の処理は場合により50’C付近で行なうこと
もあるが、上記範囲の場合の処理作業は常温(20〜3
0℃)で充分であり、省エネルギーの利点があるばかり
でなく処理の速度が迅速でしかも均一な面を得られる特
長がある。
Chemical polishing may be carried out at around 50'C depending on the case, but in the case of the above range, the processing work is carried out at room temperature (20 to 30°C).
0° C.) is sufficient, and it not only has the advantage of energy saving, but also has the advantage that the processing speed is quick and a uniform surface can be obtained.

このようにして洗浄にした面を銅または鋼合金の防錆剤
0.5〜0.31を含む水溶液中で60〜90Cで処理
すると1強固で安定した防錆膜を得ることができる。
When the thus cleaned surface is treated at 60 to 90C in an aqueous solution containing 0.5 to 0.31 of a copper or steel alloy rust preventive agent, a strong and stable rust preventive film can be obtained.

以上述べたようにこの発明によれば負極集電体の負極活
性物質と接触する鋼または鋼合金を、過酸化水素、硫酸
系の化学研摩液で研摩して清浄化した後、銅または鋼合
金の防錆剤を含む水溶液により防錆処理をほどこすこと
により、水素ガスの発生が少なくしたがって漏液、イン
ピーダンスの増加、破裂等がなく寿命を長期化できるア
ルカリ電池の製造方法を提供することができる。
As described above, according to the present invention, after polishing and cleaning the steel or steel alloy that comes into contact with the negative electrode active material of the negative electrode current collector with a hydrogen peroxide or sulfuric acid based chemical polishing liquid, the copper or steel alloy It is an object of the present invention to provide a method for producing an alkaline battery that can prolong its life without causing leakage, impedance increase, rupture, etc., by applying rust prevention treatment with an aqueous solution containing a rust preventive agent. can.

なお、この発明は上記実施例に限定されるものではなく
要旨を変更しない範囲において種々変形しているが防錆
剤はこれのみに限定されるものではない。
It should be noted that the present invention is not limited to the above embodiments, and various modifications may be made without changing the gist thereof, but the rust preventive agent is not limited to these.

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

第1図はこの発明の一実施例の製造工程の説明図、第2
図は同実施例によって得られた酸化水銀電池を示す縦断
面図である。 1・・・ニッケル    2・・・ステンレススチール
3・・・鋼       4・・・負極容器5・・・周
辺折返し部  6・・・治具9・・・セパレータ  1
0・・・電解液保持剤11・・・水化亜鉛   12・
−・絶縁バッキング13・・・環体 vE1図 第2図
Fig. 1 is an explanatory diagram of the manufacturing process of one embodiment of the present invention;
The figure is a longitudinal cross-sectional view showing a mercury oxide battery obtained in the same example. 1...Nickel 2...Stainless steel 3...Steel 4...Negative electrode container 5...Peripheral folded part 6...Jig 9...Separator 1
0... Electrolyte holding agent 11... Zinc hydrate 12.
-・Insulating backing 13... Ring body vE1 Figure 2

Claims (5)

【特許請求の範囲】[Claims] (1)負極集電体の負極活物質と接する鋼または銅合金
の表面を、過酸化水素、硫酸系の化学研摩液で研摩して
清浄化した後、鋼または鋼合金の防錆剤を含む水溶液に
より防錆処理をほどこす工程を有することを特徴とする
アルカリ電池の製造方法。
(1) After polishing and cleaning the surface of the steel or copper alloy that is in contact with the negative electrode active material of the negative electrode current collector with a hydrogen peroxide or sulfuric acid-based chemical polishing liquid, a rust preventive agent for the steel or steel alloy is added. A method for producing an alkaline battery, comprising the step of applying rust prevention treatment using an aqueous solution.
(2)上記化学研摩液は過酸化水素8〜10モル、硫酸
0.25〜0,6モルを含むものであることを特徴とす
る特許請求の範囲第1項記載のアルカリ電池の製造方法
(2) The method for manufacturing an alkaline battery according to claim 1, wherein the chemical polishing liquid contains 8 to 10 moles of hydrogen peroxide and 0.25 to 0.6 moles of sulfuric acid.
(3)上記化学研摩液は過酸化水素に対する硫酸のモル
比が0.03〜0.06の範囲のものであることを特徴
とする特許請求の範囲第2項記載のアルカリ電池の製造
方法。
(3) The method for manufacturing an alkaline battery according to claim 2, wherein the chemical polishing liquid has a molar ratio of sulfuric acid to hydrogen peroxide in a range of 0.03 to 0.06.
(4)上記防錆処理は鋼または鋼合金の防錆剤0.05
〜0.301を含む水溶液中で60〜90℃の温度で行
なわれることを特徴とする特許請求の範囲ta1項ない
し第3項のいずれかに記載のアルカリ電池の製造方法。
(4) The above rust preventive treatment is a rust preventive agent for steel or steel alloys with 0.05
The method for producing an alkaline battery according to any one of claims ta1 to 3, characterized in that the process is carried out in an aqueous solution containing 0.301 to 60 to 90°C.
(5)上記防錆剤としてトリアゾール誘導体を用いるこ
とを特徴とする特許請求の範囲第1項ないし第4項のい
ずれかに記載されたアルカリ電池の製造方法。
(5) The method for manufacturing an alkaline battery according to any one of claims 1 to 4, characterized in that a triazole derivative is used as the rust preventive agent.
JP57038578A 1982-03-11 1982-03-11 Manufacture of alkaline battery Pending JPS58155657A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57038578A JPS58155657A (en) 1982-03-11 1982-03-11 Manufacture of alkaline battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57038578A JPS58155657A (en) 1982-03-11 1982-03-11 Manufacture of alkaline battery

Publications (1)

Publication Number Publication Date
JPS58155657A true JPS58155657A (en) 1983-09-16

Family

ID=12529166

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57038578A Pending JPS58155657A (en) 1982-03-11 1982-03-11 Manufacture of alkaline battery

Country Status (1)

Country Link
JP (1) JPS58155657A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60221957A (en) * 1984-03-22 1985-11-06 Toshiba Battery Co Ltd Alkaline battery with no added mercury
US6602629B1 (en) 2000-05-24 2003-08-05 Eveready Battery Company, Inc. Zero mercury air cell

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60221957A (en) * 1984-03-22 1985-11-06 Toshiba Battery Co Ltd Alkaline battery with no added mercury
US6602629B1 (en) 2000-05-24 2003-08-05 Eveready Battery Company, Inc. Zero mercury air cell

Similar Documents

Publication Publication Date Title
FR2611988A1 (en) PROCESS FOR MANUFACTURING A NICKEL HYDROXIDE ELECTRODE
US20090220861A1 (en) Method for producing alkaline battery, and alkaline battery
JPS58155657A (en) Manufacture of alkaline battery
US4364800A (en) Situ metal plating of the cathode terminal surface of an electrochemical cell
JPS58155653A (en) Manufacture of alkaline battery
JPS58155655A (en) Manufacture of alkaline battery
JPH06338327A (en) Negative electrode collector and button-shaped alkaline battery using same
JPS58169770A (en) Manufacturing method of alkaline battery
JPS58155656A (en) Manufacture of alkaline battery
JPS6156285A (en) Alkali battery
JPS58155654A (en) Manufacture of alkaline battery
JPH07302581A (en) Alkaline battery
JPH0955193A (en) Alkaline cell
JPS6156286A (en) Alkali battery
JPS6151378B2 (en)
JPH10334903A (en) Substrate for alkaline storage battery, its manufacture, and alkaline storage battery
JP2003272636A (en) Alkaline battery
JP4618771B2 (en) Button-type alkaline battery
JPH0620694A (en) Alkaline dry battery
JPS61267264A (en) Alkaline battery
JPH05109411A (en) Alkaline dry battery
JPS61267265A (en) Alkaline battery
JPS59119673A (en) Battery
JPS6313306B2 (en)
JPH08130021A (en) Alkaline battery