JPS58155655A - Manufacture of alkaline battery - Google Patents
Manufacture of alkaline batteryInfo
- Publication number
- JPS58155655A JPS58155655A JP57038575A JP3857582A JPS58155655A JP S58155655 A JPS58155655 A JP S58155655A JP 57038575 A JP57038575 A JP 57038575A JP 3857582 A JP3857582 A JP 3857582A JP S58155655 A JPS58155655 A JP S58155655A
- Authority
- JP
- Japan
- Prior art keywords
- sulfuric acid
- steel
- copper
- washed
- negative electrode
- 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
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/64—Carriers or collectors
- H01M4/66—Selection of materials
- H01M4/661—Metal or alloys, e.g. alloy coatings
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy 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
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
負極活物質お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1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。In general, alkaline batteries are made by filling a positive electrode active material in a metal positive electrode container that also serves as a positive electrode terminal, a negative electrode active material and an alkaline electrolyte in a metal negative electrode container that also serves as a negative electrode terminal, and then inserting a separator between the two. The two containers are fitted together via an insulating gasket, 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銅または銅合金との2層クラッド
板、あるいはニッケル、ステンレススチール、銅または
銅合金の三層クラツド板を銅または銅合金の側が容器の
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 copper or copper alloy, or a three-layer clad plate of nickel, stainless steel, copper, or copper alloy so that the copper or copper 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銅または鋼合金面に
はクラツド板の製造工程、スリット加工。The copper 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
が鋼または鋼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 steel or steel 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鋼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き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 steel alloy surface of the negative electrode container comes into contact with the frozen zinc of the negative electrode active material, thereby performing 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、m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 pond can be sealed tightly.
L、 カt、、 、ステンレススチール、ニッケル等の
異物が鋼または銅合金面に残っていると、これらの異物
には水化と亜鉛メッキとが行われにくいため。If foreign substances such as stainless steel, nickel, etc. remain on the steel or copper alloy surface, it is difficult for these foreign substances to be hydrated and galvanized.
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、組立て後電池内部に水素ガスが充満して電
池の内圧を高め、漏液の原因となりあるいは電池を破裂
させたりして、水素ガスを発生し易い構造は、電池とし
ての重大な欠陥である。Therefore, a structure that tends to generate hydrogen gas by filling the inside of the battery with hydrogen gas after assembly, increasing the internal pressure of the battery, causing leakage, or causing the battery to explode, is a serious defect in the 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at体の負極活性物質と接触する銅または銅合金の
表面をこれらの防錆剤を含む過酸化水素。Hydrogen peroxide containing these rust inhibitors is applied to the surface of copper or copper alloy that comes into contact with the negative electrode active material of the negative electrode at-body.
硫酸系の化学研摩液で清浄化しながら同時に防錆をほど
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
することができるとともに作業効率を向上することので
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。By cleaning with a sulfuric acid-based chemical polishing liquid and applying rust prevention at the same time, less hydrogen gas is generated, so there is no leakage, increased impedance, bursting, etc., extending the service life and improving work efficiency. The purpose of this invention is to provide a method for manufacturing an alkaline battery that can be used to produce alkaline batteries.
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浄法では除去が困難であるか
ヤ、これらの有害な異物を鋼または鋼合金の表面をある
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, it may be difficult to remove foreign substances such as fine metal particles attached to the steel or steel alloy of the negative electrode container using normal cleaning methods, or it may be difficult to remove these harmful foreign substances by scraping the surface of the steel or steel alloy to a certain thickness. This was solved by taking it.
この研摩により除去する厚さは、面の汚れや異物の付着
の程度と銅または鋼合金の厚さによって決定される。鋼
または鋼合金面の厚さは、クラツド板全体の厚さの10
襲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 thickness to be removed by this polishing is determined by the degree of dirt and foreign matter adhering to the surface and the thickness of the copper or steel alloy. The thickness of the steel or steel alloy surface is 10 times the thickness of the entire clad plate.
If the degree of attack is standard and therefore the clad plate is thin, the steel or steel alloy layer will also be thin and the thickness that can be scraped will be limited.
クラツド板の厚さが9.3mmの場合は、銅または鋼合
金の厚さは30μ程度が一般的であり、 10s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、けずり堆るための費用がかさみ実用的
でない。負極容器の銅または銅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3〜5μ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 clad plate is 9.3 mm, the thickness of the copper or steel alloy is generally about 30 μm, and there is no risk of exposing the inner stainless steel layer even if it is scraped for about 10 seconds, but It is expensive and impractical to do so. It was confirmed that the depth of foreign matter such as stainless steel, nickel, etc. attached to or embedded in the copper or copper alloy surface of the negative electrode container is approximately 3 to 5 μm at the deepest, and that it was possible to scrape off approximately 6 μm. .
この場合に銅または鋼合金面をけする取る手段としては
、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lこは、過酸化水
素、硫酸系化学研摩剤を用いるのが、過酸化水素と硫酸
の組成、処理温度および時間を選ぶことにより、けずり
取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 because the thickness to be scraped can be controlled relatively easily. More specifically, the use of hydrogen peroxide and sulfuric acid-based chemical abrasives has the advantage that the thickness to be scraped can be precisely controlled by selecting the composition of hydrogen peroxide and sulfuric acid, processing temperature, and time. .
異物を除去した後の鋼または銅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flでに時間がか
かり、それまでの間は鋼または鋼合金面から水素ガスを
発生する。負極容器に氷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 steel or copper alloy surface is brought into contact with the steel or copper alloy surface after the foreign matter has been removed, it will take time for the steel or copper alloy surface to undergo oxidation and zinc plating, and until then, 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 frozen zinc 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、鋼または銅合金の防錆剤
を含む過酸化水素、硫酸系の化学研摩剤を用いて表面を
研磨し清浄化しながら同時に防錆被膜を形成した後永化
亜鉛とアルカリ電解液と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、
鋼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。Therefore, in this invention, the surface is polished and cleaned using hydrogen peroxide and sulfuric acid-based chemical abrasives containing rust preventive agents for steel or copper alloy, and at the same time a rust preventive film is formed on the surface. The generation of hydrogen gas is prevented by filling with electrolyte. In this case, as a rust preventive agent,
Triazole derivatives commonly used as rust inhibitors for steel 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鋼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号
研摩液でけずり取るとステンレススケールが露出しこれ
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 steel or steel alloy in the vicinity of the folded part is stretched to a high degree of processing and other parts It is thinner than the other parts. Therefore, if this part is scraped off with a chemical polishing solution, the stainless steel scale will be exposed, which may generate hydrogen gas.
しかしながら、この発明に訪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9.3 mmで鋼ノ
厚さが30声のニッケルー、ステンレススチール2、銅
3よりなる三層クラシト板を使用し、これを絞り加工し
て負極容器4を製作する。As shown in Figure 1, a three-layer Crassito board made of nickel, stainless steel 2, and copper 3 with a total thickness of 9.3 mm and a steel thickness of 30 is used, and this is drawn. A negative electrode container 4 is manufactured.
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、防錆剤としてベンゾトリア
ゾール約0.21含むとともに、過酸化水素約10モル
、硫酸的0.45モルを含み過酸化水素に対する硫酸の
モル比が0.045の化学研摩液により常温で2分間程
度処理した後、゛水洗、硫酸洗い、水洗、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夢こすると同時に清浄面に防錆被
覆を形成する。鋼面をけずりとる厚さは平均して約6μ
とする。A jig 6 made of synthetic resin is attached to the peripheral folded part 5 of this negative electrode container 4.
After contacting and covering the surface, it contains about 0.21 moles of benzotriazole as a rust preventive agent, about 10 moles of hydrogen peroxide, and 0.45 moles of sulfuric acid, and the molar ratio of sulfuric acid to hydrogen peroxide is 0.045. After being treated with a chemical polishing solution for about 2 minutes at room temperature, the exposed surface of the steel 3 is chemically scraped by repeating water washing, sulfuric acid washing, water washing, neutralization, and water washing to remove foreign substances and clean it. At the same time as rubbing, a rust-preventing coating is formed on the clean surface. The average thickness of the steel surface is approximately 6μ
shall be.
はニッケルメッキした鋼板よりなる有底短円筒状の正極
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、1G
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汞化亜鉛であ
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
1の開口部を内側に彎曲させてこれを締着している。is a short cylindrical cathode container with a bottom made of nickel-plated steel plate, 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, 1G
1 is an electrolyte holding material made of a porous fiber material impregnated with an alkaline electrolyte, and 11 is zinc chloride as a negative electrode active material. An insulating backing 12 insulates and seals the gap between the positive electrode container 7 and the negative electrode container 4, and the opening of the positive electrode container 1 is curved inward to fasten the backing.
図中13は環体である。In the figure, 13 is a ring.
このようにして作った電池0を含む各種の処理液組成の
電池内〜聞と比較のために同じ負極容器をトリクレン洗
滌後アルカリ洗滌して水洗乾燥しただけのものを用いて
組立てた従来の電池(ト)とを漏液の点について対比し
た。すなわち第1表は。For comparison, the interior of batteries with various treatment solution compositions, including the battery 0, made in this way, and a conventional battery assembled using the same negative electrode container that had been washed with trichlene, alkaline, washed with water, and dried. (G) was compared with respect to leakage. In other words, Table 1 is.
これらの電池を温度60℃、湿度90チの試験槽中lζ
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。These batteries were placed in a test tank at a temperature of 60°C and a humidity of 90°C.
The figure shows the number of leaked samples for each 1000 samples stored using a 10x microscope.
第 1 表
また第2表は温度45℃、湿度90チで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・り
を調べ、それぞれ試験電池1000個中膨らんでQ、5
mm以上高くなった電池の個数を示したものである。Table 1 and Table 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°C.
This shows the number of batteries whose height has increased by mm or more.
第 2 表
第1表によると、従来品η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内〜(ト)の場合には貯蔵
日数30日で少ない個数の漏液が始まり1日数が増加し
ても従来品(ト)の場合に比して漏液するものの数は著
しく少ない。Table 2 According to Table 1, in the case of the conventional product η, leakage starts after 20 days of storage and rapidly increases as the number of days increases, whereas in the case of the battery of the present invention (g) A small number of leaks started after 30 days of storage, and even if the number of days increased, the number of leaks was significantly smaller than in the case of the conventional product (G).
また第2表によれば、従来品ηの場合の不良の数に比し
てこの発明による電池囚〜(至)の場合−こは約V7以
下に抑えることができる。Further, according to Table 2, the number of defects in the battery according to the present invention can be suppressed to about V7 or less compared to the number of defects in the case of the conventional product η.
なお、@1表および第2表を通じ過酸化水素8〜10モ
ル、硫#0.25〜0.6モル、過酸化水素に対する硫
酸のモル比がQ、03〜0.06の@囲に含まれる(口
)−〇の場合が特く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 is 8 to 10 moles, sulfur # is 0.25 to 0.6 mole, and the molar ratio of sulfuric acid to hydrogen peroxide is included in the @circle of Q, 03 to 0.06. It can be seen that particularly good test results can be obtained in the case of -○.
以上述べたようにこの発明によれば、aii集電体の負
極活性物質と接触する銅または鋼合金の表面を、これら
の防錆剤を含む過酸化水素、硫酸系の化学研摩液で清浄
化しながら同時−こ防錆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することができるととも
に作業効率を向上することが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, the surface of the copper or steel alloy that comes into contact with the negative electrode active material of the AII current collector is cleaned with a chemical polishing solution based on hydrogen peroxide or sulfuric acid containing these rust preventive agents. At the same time, by applying rust prevention, the generation of hydrogen gas is reduced, so there is no leakage, impedance increase, explosion, etc., and the lifespan of alkaline batteries can be extended, and work efficiency can be improved. A manufacturing method can be provided.
なお、この発明は上記実施例に限定されるものではなく
要旨を変艇しない範囲において種々変形して実施するこ
とができる。上記実施例においで防錆剤としてマアゾー
ル誘導体を用いる場合を示しているか6.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-mentioned embodiments, and can be implemented with various modifications without departing from the gist. 6. Does the above example show the case where a maazole derivative is used as a rust preventive agent? Rust inhibitors are not limited to these.
第1図はこの発明の一実施例の製造工程の#i、BA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・・・銅 4・・・負極容器5・・・周
辺折返し部 6・・・治具7・・・正極容器
8・・・陽極合剤9・・・セパレータ 1o・・・電
解液保持材11・・・氷化亜鉛 12・・・絶縁バ
ッキング13・・・項体FIG. 1 is a #i, BA diagram of the manufacturing process of an embodiment of the present invention, and FIG. 2 is a longitudinal cross-sectional view showing a mercury oxide battery obtained by the same embodiment. 1... Nickel 2... Stainless steel 3... Copper 4... Negative electrode container 5... Peripheral folded part 6... Jig 7... Positive electrode container
8... Anode mixture 9... Separator 1o... Electrolyte holding material 11... Zinc oxide 12... Insulating backing 13... Nectar body
Claims (4)
合金の表面を、鋼または鋼合金の防錆剤を含む過酸化水
素、硫酸系の化学研摩液で研摩して清浄化と防錆とを同
時に行なうことを特徴とするアルカリ電池の製造方法。(1) The surface of the steel or copper alloy that is in contact with the negative electrode active material of the negative electrode current collector is cleaned and rust-prevented by polishing it with hydrogen peroxide or sulfuric acid-based chemical polishing liquid that contains a steel or steel alloy rust inhibitor. A method for producing an alkaline battery, characterized by carrying out the following at the same time.
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.
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.
とを特徴とする特許請求の範囲第1項ないし第3項のい
ずれかに記載されたアルカリ電池の製造方法。(4) The method for manufacturing an alkaline battery according to any one of claims 1 to 3, characterized in that a triazole derivative is used as the rust preventive agent.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57038575A JPS58155655A (en) | 1982-03-11 | 1982-03-11 | Manufacture of alkaline battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57038575A JPS58155655A (en) | 1982-03-11 | 1982-03-11 | Manufacture of alkaline battery |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58155655A true JPS58155655A (en) | 1983-09-16 |
Family
ID=12529081
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57038575A Pending JPS58155655A (en) | 1982-03-11 | 1982-03-11 | Manufacture of alkaline battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58155655A (en) |
-
1982
- 1982-03-11 JP JP57038575A patent/JPS58155655A/en active Pending
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