JP2950574B2 - Immersion treatment method of carbon rod for manganese dry battery - Google Patents

Immersion treatment method of carbon rod for manganese dry battery

Info

Publication number
JP2950574B2
JP2950574B2 JP2097687A JP9768790A JP2950574B2 JP 2950574 B2 JP2950574 B2 JP 2950574B2 JP 2097687 A JP2097687 A JP 2097687A JP 9768790 A JP9768790 A JP 9768790A JP 2950574 B2 JP2950574 B2 JP 2950574B2
Authority
JP
Japan
Prior art keywords
carbon rod
impregnating agent
manganese dry
dry battery
melting point
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.)
Expired - Fee Related
Application number
JP2097687A
Other languages
Japanese (ja)
Other versions
JPH03297063A (en
Inventor
健一 篠田
彰英 泉
光良 村井
隆興 竹島
信昭 渡辺
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 Corp
Original Assignee
FDK Corp
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Filing date
Publication date
Application filed by FDK Corp filed Critical FDK Corp
Priority to JP2097687A priority Critical patent/JP2950574B2/en
Publication of JPH03297063A publication Critical patent/JPH03297063A/en
Application granted granted Critical
Publication of JP2950574B2 publication Critical patent/JP2950574B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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  • Sealing Battery Cases Or Jackets (AREA)
  • Inert Electrodes (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 《産業上の利用分野》 この発明は、高温貯蔵性を改良したマンガン乾電池用
炭素棒の浸漬処理方法に関する。
The present invention relates to a method of immersing a carbon rod for a manganese dry battery with improved high-temperature storability.

《従来の技術》 マンガン乾電池の集電体として用いられている炭素棒
は、それ自体が多孔質であるため、成形した炭素棒をそ
のまま電池に組込んだのでは炭素棒を通じて電池内への
空気の侵入や、電解液の滲出による正極端子板の腐蝕が
生ずる。
<Conventional technology> Since the carbon rod used as a current collector of a manganese dry battery is porous in itself, if the molded carbon rod is directly incorporated into the battery, air will flow into the battery through the carbon rod. And the corrosion of the positive electrode terminal plate due to the infiltration of the electrolyte solution.

このような不具合を防止するために、従来から、溶融
したパラフィンワックス浸漬槽内に炭素棒を浸漬するこ
とにより、パラフィンワックスからなる含浸剤を多孔質
内部に含浸させて隙間を塞いだ後に電池に組込んでい
る。
Conventionally, in order to prevent such problems, a carbon rod is immersed in a molten paraffin wax immersion tank to impregnate a porous impregnant made of paraffin wax into the inside of the porous material and close the gap. Incorporated.

ところで、近年ではマンガン乾電池にあっても電子部
品並みに高温貯蔵における耐久性が要求され、その目安
として従来の45℃貯蔵から60℃貯蔵における耐久性を評
価されるようになってきた。
By the way, in recent years, manganese dry batteries have been required to have durability in high-temperature storage similar to that of electronic components, and as a guideline, durability from conventional storage at 45 ° C. to storage at 60 ° C. has been evaluated.

また、このように高温貯蔵した場合には、前記炭素棒
に含浸されたパラフィンワックスの溶融による劣化が問
題となる。
In addition, when stored at such a high temperature, there is a problem that the paraffin wax impregnated in the carbon rod is deteriorated by melting.

この問題を解決するために、パラフィンワックスのう
ち、高温貯蔵に耐えられるものとして、市販されてい
る。例えば、融点が180゜F(84℃)のマイクロワックス
を含浸剤として用いれば、前述の高温貯蔵性能を満足す
るものと考えられていた。
In order to solve this problem, paraffin wax is commercially available as a paraffin wax that can withstand high-temperature storage. For example, it has been considered that the use of a microwax having a melting point of 180 ° F. (84 ° C.) as the impregnating agent satisfies the above-described high-temperature storage performance.

《発明が解決しようとする課題》 しかしながら、前記浸漬処理方法では、実際に前記高
融点マイクロワックスを使用して含浸処理したものを60
℃で貯蔵すると、初期状態に比べて内部抵抗が増加し、
また封口剤の劣化などが生じていた。
<< Problems to be Solved by the Invention >> However, in the above-mentioned immersion treatment method, what is actually impregnated using the high melting point microwax is 60%.
When stored at ℃, internal resistance increases compared to the initial state,
In addition, deterioration of the sealing agent and the like have occurred.

この原因として含浸剤として用いられるパラフィンワ
ックス,マイクロワックスは仮にその融点を80℃とする
と、その約20℃の低い値が軟化点となり、60℃で貯蔵す
ると前記高融点パラフィンワックス中に含まれている低
分子量成分が溶融して炭素棒の表面に滲み出し、正極合
剤と炭素棒との接触抵抗を増加させ、また、炭素棒に塗
布されている封口剤を劣化させるからであると推定され
る。
The reason for this is that if the melting point of paraffin wax or microwax used as an impregnating agent is assumed to be 80 ° C., its low value of about 20 ° C. becomes the softening point, and when stored at 60 ° C., it is contained in the high melting point paraffin wax. It is presumed that the low molecular weight component melts and oozes out on the surface of the carbon rod, increasing the contact resistance between the positive electrode mixture and the carbon rod and deteriorating the sealing agent applied to the carbon rod. You.

この発明は、少なくとも含浸剤の融点を90℃以上に設
定すれば、高温貯蔵による含浸剤成分の滲み出しを防止
できることに着目してなされたものであり、高温貯蔵性
を向上したマンガン乾電池用炭素棒の浸漬処理方法を提
供することを目的とする。
The present invention has been made in view of the fact that, if the melting point of the impregnating agent is set to at least 90 ° C., it is possible to prevent the exudation of the impregnating agent components due to high-temperature storage, and the carbon for manganese dry batteries with improved high-temperature storage properties has been made. An object of the present invention is to provide a method of immersing a rod.

《課題を解決するための手段》 前記目的を達成するため、この発明方法では、含浸剤
として、ノルマルパラフィンを主成分とする分子量300
〜500の炭化水素化合物からなるパラフィンワックス,
もしくは分子量35〜60のイソパラフィンおよびシクロパ
ラフィン系炭化水素混合物からなるマイクロワックスを
主成分とし、これに結合性ポリオレフィン系樹脂を添加
し、少なくともその融点を90℃以上とした含浸剤組成物
を用いたことを特徴とする。
<< Means for Solving the Problems >> In order to achieve the above object, in the method of the present invention, as an impregnating agent, a molecular weight of 300 having normal paraffin as a main component is used.
Paraffin wax consisting of ~ 500 hydrocarbon compounds,
Alternatively, an impregnating composition comprising microwax consisting of a mixture of isoparaffin and cycloparaffinic hydrocarbon having a molecular weight of 35 to 60 as a main component, a binding polyolefin resin added thereto, and having a melting point of at least 90 ° C. or more was used. It is characterized by the following.

含浸に用いられる含浸剤組成物中の結晶性ポリオレフ
ィン系樹脂としては、融点107℃の結晶性ポリエチレ
ン,または軟化点145℃の結晶性ポリプロピレン等が用
いられる。
As the crystalline polyolefin-based resin in the impregnating composition used for the impregnation, crystalline polyethylene having a melting point of 107 ° C. or crystalline polypropylene having a softening point of 145 ° C. is used.

そしてこれを主成分である前記組成のパラフィンワッ
クス,もしくはマイクロワックスに温度150〜160℃で混
合分散することで、少なくとも融点90℃以上の含浸剤組
成物が得られる。
Then, this is mixed and dispersed in paraffin wax or microwax having the above-mentioned composition as a main component at a temperature of 150 to 160 ° C. to obtain an impregnating composition having a melting point of 90 ° C. or more.

なお、融点が90℃以上という値は、前述のように一般
に前記ワックスの軟化点は、その融点に対して約20℃低
く、60℃における貯蔵性を考慮すると、その軟化点を少
なくても70℃程度に設定すれば良いことに着目して設定
された値である。
The value of the melting point of 90 ° C. or higher generally means that the softening point of the wax is about 20 ° C. lower than the melting point as described above, and considering the storability at 60 ° C., the softening point is at least 70 ° C. It is a value set by paying attention to the fact that it should be set to about ° C.

このように融点を90℃以上に設定することにより前記
結晶性ポリオレフィン系樹脂の添加量が定まる。
By setting the melting point to 90 ° C. or higher, the amount of the crystalline polyolefin resin to be added is determined.

例えば前記樹脂がポリエチレンの場合、その添加量は
5〜10%、多くても15%(重量、以下同じ)になる。
For example, when the resin is polyethylene, the added amount is 5 to 10%, and at most 15% (weight, the same applies hereinafter).

つまり、この限定理由としては、添加量が下限値の5
%を下回った場合には、融点が90℃以下になり、所期の
効果が得られなくなる。
In other words, the reason for this limitation is that the amount of addition is lower than the lower limit of 5%.
%, The melting point becomes 90 ° C. or less, and the desired effect cannot be obtained.

逆に上限値の15%を上回った場合には、溶融粘度が上
がりすぎ、含浸処理温度を相当高く設定するか、あるい
は時間を長くしないと炭素棒に対する含浸性が低下する
からである。
Conversely, if it exceeds 15% of the upper limit, the melt viscosity becomes too high, and the impregnating property to the carbon rod decreases unless the impregnation temperature is set to a considerably high value or the time is not prolonged.

なお、他の結晶性ポリオレフィン樹脂を用いた場合に
も、融点を90℃以上に設定することおよび含浸時におけ
る粘度を考慮することでその添加量が定まることにな
る。
In the case where another crystalline polyolefin resin is used, the amount to be added is determined by setting the melting point to 90 ° C. or higher and considering the viscosity at the time of impregnation.

前記炭素棒は、黒鉛にバインダとしてピッチ,タール
等を混練し、棒状に押出成形し、次いで焼成した後、所
定寸法に裁断したものが用いられる。
As the carbon rod, one obtained by kneading graphite, pitch, tar, or the like as a binder, extruding into a rod shape, firing, and then cutting to a predetermined size is used.

この炭素棒の含浸処理方法は、前記組成物からなる含
浸剤が満たされ、真空状態に保たれ、かつ含浸剤の溶融
粘度に応じて150℃に保たれた浸漬槽内に炭素棒を投入
し、飽和状態まで含浸させ、その後引上げ、加熱によっ
て表面の含浸剤を除去すれば、含浸処理済みの炭素棒が
得られる。
In this method of impregnating a carbon rod, the carbon rod is charged into an immersion tank filled with an impregnating agent comprising the composition, kept in a vacuum state, and kept at 150 ° C. in accordance with the melt viscosity of the impregnating agent. If the impregnating agent is impregnated to a saturated state, then it is pulled up, and the impregnating agent on the surface is removed by heating to obtain an impregnated carbon rod.

その後前述の処理を終えた炭素棒を常法により電池に
組み込めばマンガン乾電池が完成する。
Thereafter, the manganese dry battery is completed by incorporating the carbon rod, which has been subjected to the above-described treatment, into the battery by a conventional method.

《作 用》 上記処理により得られた炭素棒を用いたマンガン乾電
池は、60℃で貯蔵した場合でも、含浸剤の融点は少なく
とも90℃以上であるから、その軟化点は70℃以上であ
り、したがってこの貯蔵温度における低分子量成分の炭
素棒表面への滲出は防止されるものと推定できる。
<< Operation >> Since the melting point of the impregnating agent is at least 90 ° C or more even when the manganese dry battery using the carbon rod obtained by the above treatment is stored at 60 ° C, its softening point is 70 ° C or more, Therefore, it can be presumed that the leaching of the low molecular weight component to the carbon rod surface at this storage temperature is prevented.

《発明の効果》 以上のように、この発明のマンガン乾電池用炭素棒の
浸漬処理方法にあっては、上述の含浸剤組成物を炭素棒
に含浸することにより60℃での高温貯蔵下における炭素
棒表面への含浸剤の滲出に伴う内部抵抗の増加や封口剤
の劣化などを防止し、高温貯蔵性能を向上できる。
<< Effects of the Invention >> As described above, in the method of immersing a carbon rod for a manganese dry battery of the present invention, the carbon rod is impregnated with the above-described impregnating composition into a carbon rod under high-temperature storage at 60 ° C. It is possible to prevent an increase in internal resistance due to leaching of the impregnating agent onto the rod surface, deterioration of the sealing agent, and the like, and improve high-temperature storage performance.

《実 施 例》 次に本発明の実施例を説明する。但し本発明は以下の
実施例に限定されるものではない。
<< Embodiment >> Next, an embodiment of the present invention will be described. However, the present invention is not limited to the following embodiments.

実施例 融点180゜F(84℃)のマイクロワックス(分子35〜60
のイソパラフィンおよびシクロパラフィン系炭化水素混
合物)が入っている150℃に保たれた浸漬槽内に、マイ
クロワックス95%に対し融点130℃の結晶性ポリエチレ
ン5%を投入し均一に分散混合することにより含浸剤組
成物を得た。得られた含浸剤組成物の融点は105℃であ
った。
Examples Microwax with melting point 180 ° F (84 ° C) (molecules 35-60)
5% of crystalline polyethylene having a melting point of 130 ° C with respect to 95% of microwax in an immersion tank maintained at 150 ° C containing a mixture of isoparaffins and cycloparaffinic hydrocarbons) and uniformly dispersed and mixed. An impregnating composition was obtained. The melting point of the obtained impregnating composition was 105 ° C.

この浸漬槽内を真空にした状態で、最適溶融粘度とな
る温度150℃に保ち、成形処理された炭素棒を投入し、
数分間浸漬しすることにより飽和状態まで含浸させ、そ
の後引上げ、140〜150℃で加熱して表面に付着している
余剰の含浸剤を除去し、含浸処理済みの炭素棒を得た。
With the inside of this immersion tank evacuated, keep the temperature at 150 ° C, which is the optimum melt viscosity, and put the molded carbon rod,
It was impregnated to a saturated state by immersing for several minutes, then pulled up and heated at 140 to 150 ° C. to remove the excess impregnating agent adhering to the surface, thereby obtaining an impregnated carbon rod.

その後常法によりこれを電池に組み込んでR20型(単
一)マンガン乾電池を完成した。
Thereafter, this was assembled into a battery by a conventional method to complete an R20 type (single) manganese dry battery.

比較例 従来タイプの最高の融点である融点180゜F(84℃)の
マイクロワックスが入っている150℃に保たれた真空状
態の浸漬槽内に炭素棒を投入し、飽和状態まで含浸さ
せ、その後引上げ、加熱によって表面の含浸剤を除去
し、含浸処理済みの炭素棒を得た。
Comparative Example A carbon rod was put into a vacuum immersion tank maintained at 150 ° C. containing microwax having a melting point of 180 ° F. (84 ° C.), which is the highest melting point of the conventional type, and impregnated to a saturated state. Thereafter, the impregnating agent on the surface was removed by pulling up and heating to obtain an impregnated carbon rod.

その後常法によりこれを電池に組み込んでR20型(単
一)マンガン乾電池を完成した。
Thereafter, this was assembled into a battery by a conventional method to complete an R20 type (single) manganese dry battery.

次に以上の実施例および比較例の各乾電池を5ケずつ
60℃で20日貯蔵した後の連続放電性能(負荷抵抗2Ω,
終止電圧0.9V)を比較したところ、実施例の電池の平均
放電時間が310分であったのに対し、比較例(従来品)
の平均放電時間は270分と大巾に下回っていた。
Next, each of the dry batteries of the above Examples and Comparative Examples was 5
Continuous discharge performance after storage at 60 ° C for 20 days (load resistance 2Ω,
Comparing the cutoff voltage (0.9V), the average discharge time of the battery of the example was 310 minutes, while the comparative example (conventional product)
Had an average discharge time of 270 minutes, which was significantly lower.

したがって、本発明方法では従来方法に比べて直接的
には推定できないものの、含浸剤の炭素棒表面に対する
滲出がなく、これにより内部抵抗増加が少なくなるもの
と推定できる。
Therefore, although the method of the present invention cannot be directly estimated as compared with the conventional method, it can be estimated that there is no seepage of the impregnating agent on the surface of the carbon rod, thereby reducing the increase in internal resistance.

また、以上の各乾電池を20ケずつを60℃で20日貯蔵
し、次いで常温で3ケ月放置した後の短絡電流を調べた
結果、実施例の平均短絡電流は8.5A,またその範囲は7.8
〜8.8Aであったのに対し、比較例の平均短絡電流は7.3A
で、またその範囲は7.0〜7.5Aであった。
Further, as a result of examining the short-circuit current after storing each of the above dry batteries at 20 ° C. for 20 days at 60 ° C. and then standing at room temperature for 3 months, the average short-circuit current of the example was 8.5 A, and the range was 7.8.
8.8 A, whereas the average short-circuit current of the comparative example was 7.3 A.
And the range was 7.0-7.5A.

したがって、本発明方法における短絡電流値は従来に
比べて大きく、またこのことは含浸剤の滲出を原因とす
る封口剤の劣化の程度も小さくなるものと推定できる。
Therefore, the short-circuit current value in the method of the present invention is larger than that of the conventional method, and it can be estimated that the degree of deterioration of the sealing agent due to leaching of the impregnating agent is reduced.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 竹島 隆興 東京都港区新橋5丁目36番11号 富士電 気化学株式会社内 (72)発明者 渡辺 信昭 東京都港区新橋5丁目36番11号 富士電 気化学株式会社内 (56)参考文献 特開 昭56−59452(JP,A) (58)調査した分野(Int.Cl.6,DB名) H01M 4/06 H01M 2/06 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takahide Takeshima 5-36-11 Shimbashi, Minato-ku, Tokyo Inside Fuji Electric Chemical Co., Ltd. (72) Inventor Nobuaki Watanabe 5-36-11 Shimbashi, Minato-ku, Tokyo (56) References JP-A-56-59452 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) H01M 4/06 H01M 2/06

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】正極集電体を構成する炭素棒を、溶融した
含浸剤を収容した浸漬槽内に浸漬し、前記炭素棒の多孔
質内部に前記含浸剤をを含浸した後引き上げ、次いで前
記炭素棒の表面に付着した余剰の含浸剤を除去する工程
からなるマンガン乾電池用炭素棒の浸漬処理方法におい
て、 前記含浸剤は、ノルマルパラフィンを主成分とする分子
量300〜500の炭化水素化合物からなるパラフィンワック
ス,もしくは分子量35〜60のイソパラフィンおよびシク
ロパラフィン系炭化水素混合物からなるマイクロワック
スを主成分とし、これに結晶性ポリオレフィン系樹脂を
添加し、少なくともその融点を90℃以上に設定した含浸
剤組成物からなることを特徴とするマンガン乾電池用炭
素棒の浸漬処理方法。
1. A carbon rod constituting a positive electrode current collector is immersed in an immersion tank containing a molten impregnating agent, and the porous interior of the carbon rod is impregnated with the impregnating agent and then pulled up. A method for immersing a carbon rod for a manganese dry battery, comprising the step of removing an excess impregnating agent attached to the surface of the carbon rod, wherein the impregnating agent is composed of a hydrocarbon compound having a molecular weight of 300 to 500 and having normal paraffin as a main component. An impregnating composition consisting mainly of paraffin wax or microwax consisting of a mixture of isoparaffins and cycloparaffinic hydrocarbons having a molecular weight of 35 to 60, to which a crystalline polyolefin resin is added and whose melting point is set to at least 90 ° C. A method of immersing a carbon rod for a manganese dry battery, comprising:
JP2097687A 1990-04-16 1990-04-16 Immersion treatment method of carbon rod for manganese dry battery Expired - Fee Related JP2950574B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2097687A JP2950574B2 (en) 1990-04-16 1990-04-16 Immersion treatment method of carbon rod for manganese dry battery

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Application Number Priority Date Filing Date Title
JP2097687A JP2950574B2 (en) 1990-04-16 1990-04-16 Immersion treatment method of carbon rod for manganese dry battery

Publications (2)

Publication Number Publication Date
JPH03297063A JPH03297063A (en) 1991-12-27
JP2950574B2 true JP2950574B2 (en) 1999-09-20

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JP (1) JP2950574B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003297370A (en) * 2002-04-01 2003-10-17 Matsushita Electric Ind Co Ltd Positive electrode electricity collector for manganese dry cell
JP2005026151A (en) * 2003-07-04 2005-01-27 Matsushita Electric Ind Co Ltd Positive current collector for manganese dry battery and manganese dry battery using it

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