JPS58155653A - Manufacture of alkaline battery - Google Patents
Manufacture of alkaline batteryInfo
- Publication number
- JPS58155653A JPS58155653A JP57038573A JP3857382A JPS58155653A JP S58155653 A JPS58155653 A JP S58155653A JP 57038573 A JP57038573 A JP 57038573A JP 3857382 A JP3857382 A JP 3857382A JP S58155653 A JPS58155653 A JP S58155653A
- Authority
- JP
- Japan
- Prior art keywords
- steel
- copper
- sulfuric acid
- hydrogen peroxide
- chemical polishing
- 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
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 28
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000000126 substance Substances 0.000 claims abstract description 15
- 238000005498 polishing Methods 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 6
- 239000010959 steel Substances 0.000 claims description 25
- 229910000851 Alloy steel Inorganic materials 0.000 claims description 21
- 229910000831 Steel Inorganic materials 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 7
- 239000007773 negative electrode material Substances 0.000 claims description 5
- 229910052753 mercury Inorganic materials 0.000 claims description 3
- -1 mercury ions Chemical class 0.000 claims description 3
- 238000005267 amalgamation Methods 0.000 claims 1
- 229910000881 Cu alloy Inorganic materials 0.000 abstract description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 8
- 239000010949 copper Substances 0.000 abstract description 8
- 239000003792 electrolyte Substances 0.000 abstract description 8
- 238000004140 cleaning Methods 0.000 abstract description 7
- 229910052802 copper Inorganic materials 0.000 abstract description 5
- 229910001111 Fine metal Inorganic materials 0.000 abstract description 2
- 229960002523 mercuric chloride Drugs 0.000 abstract description 2
- LWJROJCJINYWOX-UHFFFAOYSA-L mercury dichloride Chemical compound Cl[Hg]Cl LWJROJCJINYWOX-UHFFFAOYSA-L 0.000 abstract description 2
- 229920003002 synthetic resin Polymers 0.000 abstract description 2
- 239000000057 synthetic resin Substances 0.000 abstract description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 abstract 3
- BQPIGGFYSBELGY-UHFFFAOYSA-N mercury(2+) Chemical compound [Hg+2] BQPIGGFYSBELGY-UHFFFAOYSA-N 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 14
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 12
- 239000010935 stainless steel Substances 0.000 description 9
- 229910001220 stainless steel Inorganic materials 0.000 description 8
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 6
- 229910052725 zinc Inorganic materials 0.000 description 6
- 239000011701 zinc Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- 229910052759 nickel Inorganic materials 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 5
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 description 4
- 238000005406 washing Methods 0.000 description 3
- 235000005074 zinc chloride Nutrition 0.000 description 3
- 239000011592 zinc chloride Substances 0.000 description 3
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 229910001923 silver oxide Inorganic materials 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 229910000990 Ni alloy Inorganic materials 0.000 description 1
- 239000003082 abrasive agent Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000009172 bursting Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 238000005253 cladding Methods 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000007772 electrode material Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 229910000474 mercury oxide Inorganic materials 0.000 description 1
- UKWHYYKOEPRTIC-UHFFFAOYSA-N mercury(ii) oxide Chemical compound [Hg]=O UKWHYYKOEPRTIC-UHFFFAOYSA-N 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000007774 positive electrode material Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 229910001256 stainless steel alloy Inorganic materials 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/10—Primary casings; Jackets or wrappings
- H01M50/147—Lids or covers
- H01M50/166—Lids or covers characterised by the methods of assembling casings with lids
- H01M50/171—Lids or covers characterised by the methods of assembling casings with lids using adhesives or sealing agents
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/10—Primary casings; Jackets or wrappings
- H01M50/147—Lids or covers
- H01M50/166—Lids or covers characterised by the methods of assembling casings with lids
- H01M50/167—Lids or covers characterised by the methods of assembling casings with lids by crimping
-
- 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)
- 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屡液を用いるアルカ
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 producing an alkaline battery using zinc or the like as a negative electrode active material and an alkaline electrolyte solution.
一般にアルカリ電池は正極端子を兼ねる金属製正極容量
内〈正極活物質、負極端子を兼ねる金属m電極容器内に
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ゲット
を介して両容器を嵌合し、正極容量の開口部を内方〈彎
−させて密封口している。In general, alkaline batteries have a metal positive electrode capacity that also serves as the positive electrode terminal. After filling the negative electrode active material and alkaline electrolyte into a metal electrode container that also serves as the positive electrode terminal, a separator is interposed, and one synthetic polymer, etc. The two containers are fitted together via an insulating gas get, and the opening of the positive electrode capacitor is curved inward to seal the 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銅合金との2層りラV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鋼また鋼合金の側が容器の内
面になるように紋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
A two-layer V-clad plate of stainless steel and steel or copper alloy, or a three-layer V-clad plate of nickel, stainless steel, steel, or copper alloy is processed so that the steel or steel alloy side becomes the inner surface of the container. It was manufactured by
このようにして製造した負極容器の銅または鋼合金WK
−はクラッド坂の製造工程、スリット加工打抜II/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つたり、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−である。Copper or steel alloy WK of the negative electrode container manufactured in this way
- is to avoid the formation of oxides, the adhesion of dirt and dust, or the adhesion of minute pieces of metal such as stainless steel and nickel during the cladding slope manufacturing process, slit processing punching II/drawing process, etc. I can't. 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, it is impossible to completely remove them with normal cleaning or other means. It is difficult to remove.
負極容器の鋼才たは鋼合金面はアルカリ電解液のあるこ
とにより、jlL極活物質の汞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 steel or steel alloy surface of the negative electrode container comes into contact with the zinc chloride of the JIL electrode active material, and is amalgamated and galvanized.
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.
Lかり、ステンレススチール、ニッケル等の異物が鋼ま
たは鋼合金面に残っていると、これらの異物ζこは汞化
と亜鉛メッキとが行われにくいため。If foreign matter such as steel, stainless steel, or nickel remains on the steel or steel alloy surface, it will be difficult for these foreign matter to undergo galvanization and galvanization.
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a<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 capacity a is filled with 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満して電
池の内圧を高め、ll液の原因となりあるいは電池を破
裂させたりして、水素ガスを発生し鳥い構造は、電池と
しての重大な欠陥である。Therefore, after one assembly, the inside of the battery is filled with hydrogen gas, which increases the internal pressure of the battery, causing ll liquid or causing the battery to explode, producing hydrogen gas. be.
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銅または銅合金の
s面を過酸化水素、硫酸系の化学研摩液で清浄化した後
、水銀イオンを含む溶液でアマルガム化することにより
、水素ガスの発生が少なくしたがって漏液や破裂等がな
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
法を提供することを目的としている。After cleaning the s-plane of copper or copper alloy that comes into contact with the negative electrode active material of the negative electrode current collector with hydrogen peroxide and sulfuric acid-based chemical polishing liquid, the hydrogen gas is removed by amalgamating with a solution containing mercury ions. It is an object of the present invention to provide a method for manufacturing an alkaline battery which can have a long lifespan without the occurrence of leakage or bursting.
すなわち、負極容器の鋼または鋼合金には付着した金属
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
から、これらの有害な異物を鋼または鋼合金の表面をあ
る厚さまでけずり壜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 fine metal particles attached to the steel or steel alloy of the negative electrode container using normal cleaning methods, it is necessary to scrape the surface of the steel or steel alloy to a certain thickness to remove these harmful foreign substances. This was solved by bottling it.
この研摩により除去する厚さは1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、ブラッド板金体の厚さの10
−程度が標準的であり、したがってクラvWIKが薄い
場合は鋼または鋼合金層もまた薄くなり、けずり堆る厚
さも制限される。The thickness to be removed by this polishing is determined by the degree of dirt or foreign matter adhering to one 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 brad sheet metal body.
- If the degree is standard and therefore the crack vWIK is thin, the steel or steel alloy layer will also be thin and the thickness that can be chipped will also be limited.
クラツド板の厚さが9.3mmの場合は、鍋または鋼合
金の厚さは30J1程度が一般的であり、lG#1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詔
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S
さは、深いものでも3〜5μS度であり、6s@度けず
り取ることこののできることが確gされた。If the thickness of the clad plate is 9.3 mm, the thickness of the pot or steel alloy is generally about 30J1, and even if it is scraped off by 1 degree, the inner stainless steel layer will not be exposed. It is impractical and impractical due to the high cost of shaving. Foreign matter such as stainless steel or nickel is attached to or has been implanted into the steel or steel alloy surface of the negative electrode container S.
It was confirmed that the depth was 3 to 5 μS degrees even at deep depths, and that it was possible to remove 6 seconds of scratches.
この場合に鋼または鋼合金間をけする取る手段としては
、けずり敗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。さらに異体的には、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 leveling the gap between the steels or steel alloys, since the thickness of the steel or steel alloy can be controlled relatively easily. Furthermore, 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, treatment temperature, and time.
異物を除去した後の銅または銅合金面はそのまでに時間
がかかり、それまでの間は鋼または鋼合金間から水素ガ
スを発生する。負極容器に氷化亜鉛肴よびアルカリ電解
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くなる。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mj(よる漏液の原因となる。It takes time for the copper or copper alloy surface to remove foreign matter, and until then, hydrogen gas is generated from between the steel or steel alloy. Since the battery is assembled immediately after filling the negative electrode container with frozen zinc platter and alkaline electrolyte, the generation of hydrogen gas continues until after the battery is assembled. When hydrogen gas is generated inside the battery, it increases its impedance or increases the internal pressure (mj), causing leakage.
そこでこの発lidおいては、鋼または銅合金面を清浄
にした後、電池組立前にこの面をアマルガム化しその後
汞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。Therefore, in this generation lid, after cleaning the steel or copper alloy surface, this surface is amalgamated before battery assembly, and then filled with zinc chloride and alkaline electrolyte to prevent the generation of hydrogen gas. There is.
なn、*a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、この折返し部を影成する
際祈り返し部付近は銅t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壜るとステンレスス
チ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。*a Containers generally have a shape with a folded part around the periphery by drawing processing, and when forming this folded part, the area around the folded part has to be drawn because the copper or steel alloy is highly processed. It has been stretched out and is thinner than the other parts. Therefore, if this part is scraped with a chemical polishing solution, the stainless steel will be 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
ても水素ガス発生肪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 hydrogen gas generation and fat stop in this respect as well.
次に図画を参照してこの発明の一実施例を説明する。Next, one 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Q、3 mmで鋼の
厚さが30声のニッケル1.ステンレススチール2、鋼
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, a nickel 1. A three-layer clad plate made of stainless steel 2 and steel 3 is used and drawn to produce a negative electrode container 4.
との負極容器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分関糧度処
理した後、水洗、硫酸洗い。A synthetic resin jig 6 is attached to the peripheral folded part 5 of the negative electrode container 4.
After the surface was covered with a chemical polishing solution containing about 10 moles of hydrogen peroxide and 0.45 moles of sulfuric acid, and the molar ratio of sulfuric acid to hydrogen peroxide was 0.045, it was treated at room temperature for 2 minutes. After that, wash with water and sulfuric acid.
水洗、中和、水洗を繰返して露出している鋼3の表面を
化学的にけずり堰る。鋼面のけずり散る厚さを平均して
約6μとする。The exposed surface of the steel 3 is chemically dammed by repeating water washing, neutralization, and water washing. The average thickness of the scraped steel surface is approximately 6μ.
次いで、治具6を堰外し酢酸酸性の塩化第二水銀溶液に
浸漬して鋼面をアマルガム化した後水洗乾燥した。Next, the jig 6 was removed from the weir and immersed in an acetic acidic mercuric chloride solution to amalgamate the steel surface, followed by washing with water and drying.
この負性容器4を用いて第2図に示すような酸はニッケ
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ζこ電導剤として島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。1
2は正極容器7と負極容器4との間を絶縁するととも番
こ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。Using this negative container 4, the acid as shown in FIG.
9 is an ion-permeable separator; 10 is an electrolyte holding material made of a porous fibrous material impregnated with an alkaline electrolyte; 11 is frozen zinc as a negative electrode active material. 1
Reference numeral 2 denotes an insulating backing that insulates the gap 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を含む各種缶処理液組成の
電池囚〜(6)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4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ηとを漏液の点−こついて対比
した。すなわち第1表は。For comparison with the batteries made in this manner (6) with various can treatment solution compositions, including the battery 0, the same negative electrode containers were assembled using the same negative electrode containers that had been washed with trichlene, washed with alkali 4 times, washed with water, and dried. A comparison was made with a conventional battery η in terms of leakage. In other words, Table 1 is.
これらの電池を温度6011:、湿[901の試験槽中
に貯蔵し、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O
第 1 表
またM2flは、ii度45T:、@変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1000個中膨らんでQ、5mm
以上高くなつた電池の個数を示したものである。These batteries were stored in a test tank at a temperature of 6011: and a humidity of 901, and the number of leaked cells for each 1000 cells was measured using a 10x microscope. The changes in height due to hydrogen gas generation, etc. of batteries stored for 3 months at 45T: @ 90- were investigated, and each of the 1000 test batteries swelled to Q, 5mm.
This shows the number of batteries that have increased in price.
以下余白
第2表
第19によると、従来品(ト)の場合には貯蔵日数20
日て漏洩が始まり日数の増加とともに急激憂ζ増加して
行くのに対し、この発1jHcよる電池因〜(至)の場
合〈は貯翼日数30日で少ない個数の漏液が始まり5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 2, No. 19 in the margin below, in the case of the conventional product (G), the storage period is 20 days.
On the other hand, in the case of battery cause due to 1jHc, a small number of leaks start after 30 days of blade storage and rapidly increase as the number of days increases. Even if the number of leaks increases, the number of leaks is significantly smaller than that of the conventional product η.
また第2表によれば、従来品ηの場合の不良のな諭、第
1表および嬉2表を通じ、過酸化水素8〜10モル、硫
酸0L25〜0.6モル、過酸化水素に対する硫酸のそ
ル比が0.08−(LO6の範囲に含まれる@〜0の場
合が特に爽好な試験結果が得られることを知ることがで
きる。In addition, according to Table 2, there are 8 to 10 moles of hydrogen peroxide, 25 to 0.6 moles of sulfuric acid, and sulfuric acid to hydrogen peroxide. It can be seen that especially refreshing test results are obtained when the solenoid ratio is between 0.08 and 0, which is included in the range of 0.08-(LO6).
以上述べたようにこの発明によれば、負@集電体の員極
活性物質と接触する鋼または鋼金金の表面を過酸化水素
、硫酸系の化学研摩液で清浄化した後、水銀イオンを含
む嬉液てアマルガム化することにより、水素ガスの発生
が少なくしたがって漏液や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すること
ができる。As described above, according to the present invention, after cleaning the surface of steel or steel gold that comes into contact with the active material of the negative current collector with hydrogen peroxide and sulfuric acid based chemical polishing liquid, mercury ions are removed. It is possible to provide a method for producing an alkaline battery that generates less hydrogen gas and can prolong its life without leakage or rupture by amalgamating the liquid containing the alkaline liquid.
なお、この発明は上記実施例化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実施するこ
とができる。Note that the present invention is not limited to the above-mentioned embodiments, and can be implemented with various modifications without changing the gist.
第1図はくの発明の一実施例の製造工場の説明図、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rル3
・・・鋼 4・−負極容器5・・・周辺折返
し部 6−@^
9−−セパレータ 1G・・・電解液保持材11・−
汞化亜鉛 12・・・絶縁バッキング!3−・一体Fig. 1 is an explanatory diagram of a manufacturing factory according to an embodiment of the invention; Fig. 2
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-@^ 9--Separator 1G...Electrolyte holding material 11.-
Zinc chloride 12...Insulating backing! 3-・One body
Claims (1)
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、水銀イオンを含む溶液でアマルガム化す
る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。 (2)上記化学研摩液は過酸化水素8〜10モル、硫酸
(LL!5〜α6モルを含むものであることを特徴とす
る特許請求の範l![第1項記機のアルカリ電池の製造
方法。 (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iwgz項記載のアルカリ電池の製
造方法。[Scope of Claims] (The surface of the steel or steel alloy in contact with the negative electrode active material of the negative electrode current collector is polished and cleaned with a chemical polishing solution based on hydrogen peroxide or sulfuric acid, and then polished with a solution containing mercury ions. A method for producing an alkaline battery, characterized by comprising a step of amalgamation. (2) A patent characterized in that the chemical polishing liquid contains 8 to 10 moles of hydrogen peroxide and sulfuric acid (LL!5 to α6 moles) Claim 1! [Method for manufacturing an alkaline battery according to the machine set forth in paragraph 1. (3) The chemical polishing liquid has a molar ratio of sulfuric acid to hydrogen peroxide in a range of 0.03 to 0.06. A method for manufacturing an alkaline battery according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57038573A JPS58155653A (en) | 1982-03-11 | 1982-03-11 | Manufacture of alkaline battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57038573A JPS58155653A (en) | 1982-03-11 | 1982-03-11 | Manufacture of alkaline battery |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58155653A true JPS58155653A (en) | 1983-09-16 |
Family
ID=12529028
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57038573A Pending JPS58155653A (en) | 1982-03-11 | 1982-03-11 | Manufacture of alkaline battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58155653A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5445908A (en) * | 1991-10-17 | 1995-08-29 | Matsushita Electric Industrial Co., Ltd. | Alkaline dry cell |
EP0935300A4 (en) * | 1996-10-23 | 2000-03-01 | Tdk Corp | Method for manufacturing electrode for battery |
-
1982
- 1982-03-11 JP JP57038573A patent/JPS58155653A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5445908A (en) * | 1991-10-17 | 1995-08-29 | Matsushita Electric Industrial Co., Ltd. | Alkaline dry cell |
EP0935300A4 (en) * | 1996-10-23 | 2000-03-01 | Tdk Corp | Method for manufacturing electrode for battery |
US6423105B1 (en) | 1996-10-23 | 2002-07-23 | Tdk Corporation | Process for producing an electrode for a battery |
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