JPS58169770A - Manufacturing method of alkaline battery - Google Patents
Manufacturing method of alkaline batteryInfo
- Publication number
- JPS58169770A JPS58169770A JP57038577A JP3857782A JPS58169770A JP S58169770 A JPS58169770 A JP S58169770A JP 57038577 A JP57038577 A JP 57038577A JP 3857782 A JP3857782 A JP 3857782A JP S58169770 A JPS58169770 A JP S58169770A
- Authority
- JP
- Japan
- Prior art keywords
- steel
- hydrogen gas
- amalgamation
- alkaline battery
- copper
- 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.)
- Granted
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鋼または鋼合金との2層クラッド
板、あるいは二!ケルステンレススチール、鋼または鋼
合金の三層クラツド板を鋼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
Two-layer clad plate of stainless steel and steel or steel alloy, or two! It is manufactured by drawing a three-layer clad plate of KEL stainless steel, steel or steel alloy so that the steel or steel alloy side becomes the inner surface of the container.
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檻、スリット加工打抜き絞り加工
等の工程で、#!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at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
困離である。The steel or steel alloy surface of the negative electrode container manufactured in this manner is subjected to processes such as cladding plate manufacturing, slitting, punching, drawing, etc. The formation of chemical substances, the adhesion of dirt and dust, and the adhesion of minute pieces of metal such as stainless steel and nickel cannot be avoided. Before assembling the battery, pretreatment such as degreasing and cleaning is performed, but if these foreign substances get into scratches on the AT 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 it.
負極容器の鋼または鋼合金面はアルカリ電解液のあるこ
とにより、負極活物質の水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 negative electrode active material, zinc hydride, to undergo amalgamation and galvanization.
このため、鋼または鋼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 steel alloy is more dangerous than zinc, hydrogen gas generation is suppressed even when 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
たは鋼合金面に残;でいる払これらの異物番こは氷化と
亜鉛メッキとが行われにくいため。However, foreign substances such as stainless steel and nickel remain on the copper or steel alloy surface; these foreign substances are difficult to freeze and galvanize.
そのまま露出した状態で残る。これらの金属は水車過電
圧が小さいので、負極容器にアルカリ溶液と亜鉛さが充
填された場合、水素ガスを発生する。It remains exposed. These metals have a small water turbine overvoltage, so when the negative electrode container is filled with alkaline solution and zinc, they generate hydrogen gas.
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物質と接する鋼または鋼合金の表面
を過酸化水素、硫酸系化学研摩液で研摩して清浄化した
後、水銀イオンを含む鋼または鋼合金の防錆剤溶液で処
理し、アマルガム化と防錆処理とを同時に行なうことに
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。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 treated with a steel or steel alloy rust preventive solution containing mercury ions. However, by performing amalgamation and rust prevention treatment at the same time, less hydrogen gas is generated, resulting in leakage and increased impedance.
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。It is an object of the present invention to provide a method for manufacturing alkaline batteries that is free from bursting, has a longer service life, and can improve work efficiency.
すなわち、負極容器の鋼または鋼合金に付着した金属の
微細片辱め異物は通常の洗滌法では除去が困噛であるか
ら、これらの有害な異物を鋼または鋼合金の表面をある
厚さまでけずり取ること番ζより解決したものである。In other words, it is difficult to remove fine particles of metal adhering to the steel or steel alloy of the negative electrode container using normal cleaning methods, so these harmful foreign particles are removed by scraping off the surface of the steel or steel alloy to a certain thickness. This is the solution from number ζ.
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
の程度と銅または銅合金の厚さ化よって決定される。鋼
または鋼合金面の厚さは、クラツド板全体の厚さのl0
I1111Fが標準的であり、したからでクラツド板が
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 copper alloy. The thickness of the steel or steel alloy surface is 10 of the total thickness of the clad plate.
I1111F is standard, so if the clad plate is thin, the steel or steel alloy layer will also be thin, limiting the thickness to which it will chip.
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30III41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、けずり散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鋼合金mK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機度
けずり填ることこののできることが確−された。When the thickness of the clad plate is Q, 3mm, the thickness of steel or steel alloy is generally 30III41 degrees, and 10s.
Although there is no risk of exposing the inner stainless steel layer even if it is chipped away, it is not practical because the cost of chipping away increases. The depth to which foreign matter such as copper or steel alloy mK stainless steel, nickel, etc. is attached or implanted in the negative electrode container is about 3 to 5 depths at most, and it is possible to fill it by cutting it by 6 μm. Confirmed.
この場合番こ鋼または銅合金面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。さらに具体的には、過酸化水
素、硫酸系化学型−剤を用いるのが、過酸化水素と流酸
の組成、処理温度および時間を選ぶことにより、けずり
職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 sharpening the steel or copper alloy surface, since the thickness of the surface to be scratched can be controlled relatively easily. More specifically, the advantage of using hydrogen peroxide and sulfuric acid type chemical molding agents is that the thickness of the scratch can be precisely controlled by selecting the composition of hydrogen peroxide and hydrochloric acid, treatment temperature and time. There is.
異物を除去した後の綱または銅合金面はそのま接触した
場合、氷化と亜鉛メッキが行なわれる蟲でに時間がかか
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。負極容器に水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 some time for the steel or copper alloy surface to freeze and galvanize, and in the meantime 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 hydrate 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、化学研摩により清浄化し
た後この清浄面を水銀イオンを含む銅または銅合金の防
錆剤溶液で処理し、アマルガム化と防錆処理とを同時に
行なった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。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, after cleaning by chemical polishing, this clean surface is treated with a rust preventive solution of copper or copper alloy containing mercury ions, and amalgamation and rust prevention treatment are simultaneously performed. The generation of hydrogen gas is prevented by filling the tank with an alkaline electrolyte. In this case, triazole derivatives commonly used as rust preventive agents for steel or steel alloys can be used as the rust preventive agent.
なお、負極容器は一般に絞り加工によって周辺ζこ折返
し部を設けた形状化なっていて、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堆るとステンレス
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。In addition, the negative electrode container is generally formed into a shape with a folded part around the periphery by drawing processing, and when forming this folded part, the area near the folded part is stretched due to the high degree of processing of the copper or steel alloy. It is thinner than the . 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!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, chemical polishing is performed while avoiding the folded portion, so this is a problem! Consideration has been given to preventing the generation of hydrogen gas.
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Q、3mmで鋼の厚
さが30μのニッケルl、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, the overall thickness is Q, nickel l, stainless steel 2, steel 3 with a steel thickness of 3 mm and 30 μm.
The negative electrode container 4 is manufactured by drawing a three-layer clad plate made of the following materials.
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、過酸化水素約10モル、硫
酸約α45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−こより常温で2分間程度処
理した後、水洗、硫酸洗い。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 with a chemical polishing solution containing about 10 moles of hydrogen peroxide and about 45 moles of sulfuric acid and a molar ratio of sulfuric acid to hydrogen peroxide of 0.045, the polishing solution was treated at room temperature for about 2 minutes. Wash with water and sulfuric acid.
水洗、中和、水洗を繰返して露出している銅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。この
清浄面に対し、直ち1こ負極容51個当り約o、tmg
の水銀イオンと防錆剤としてベンゾトリアゾール0.2
11Gとを含む水溶液中に浸漬し。Water washing, neutralization, and water washing are repeated to chemically scrape off the exposed surface of the copper 3 to remove foreign matter and clean it. Approximately 0, tmg per 51 negative electrodes is applied to this clean surface.
of mercury ion and benzotriazole as a rust inhibitor 0.2
Immerse it in an aqueous solution containing 11G.
80℃で約1s秒間処理し、アマルガム化と防錆破膜の
形成を同時に行なった後、治具6を外して水洗乾燥した
。鋼面をけずり喉る厚さは平均して約6μとする。After processing at 80° C. for about 1 second to simultaneously form amalgam and form a rust-preventing broken film, the jig 6 was removed and washed with water and dried. The average thickness of the steel surface is about 6μ.
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
容易、8は酸化−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、lO
はγ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57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パフキングで、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 a short cylindrical positive electrode with a bottom made of a nickel-plated steel plate, 8 is an anode mixture formed by adding graphite as a conductive agent to an oxidized active material, 9 is an ion-permeable separator, IO
1 is an electrolyte holding material made of a porous fibrous material impregnated with a γ-alkaline electrolyte, and 11 is zinc chloride as a negative electrode active material. Reference numeral 12 denotes an insulating puffing for insulating and sealing the gap between the positive electrode container 57 and the negative electrode container 4, and the opening of the positive electrode container 1 is bent inward and fastened.
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とを漏液の点につい
て対比した。すなわち第1表は。A conventional battery η assembled using only various treatments, including the battery 0 produced in this way, was compared with respect to leakage. In other words, Table 1 is.
これらの電池を温度6011:、 51度90−の試験
槽中に貯蔵し、10倍の顕微鏡を用いてそれぞれ100
0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 stored in a test chamber at a temperature of 6011:, 51 degrees and 90 degrees, and each 100
The number of leaked samples is shown for 0 samples.
以下余白
第 l 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を調べ、そ
れぞれ試験電池1,000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 2 also shows the 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 5 mm or more.
以下余白
第 2 表
増加して行くのに対し、この発明による電池囚〜(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ηの場合に比して漏液するも
のの数は著しく少ない。Table 2 below is a blank space.
In the case of , a small number of liquids start leaking after 30 days of storage, and even if the number of days increases, the number of liquids leaking is significantly smaller than in the case of the conventional product η.
また第2表によれば、従来品ηの場合の不良の数基こ比
してこの発明による電池囚〜(6)の場合には約1/7
以下に抑えるととグできる。Also, according to Table 2, compared to the number of defective units in the case of the conventional product η, the number of defective units in the case of the battery capacitor (6) according to the present invention is approximately 1/7
You can do it by keeping it below.
なお、第1表射よび第2表を通じ過酸化水素8〜lOモ
ル、硫酸0.25〜0.6モル、過酸化水素に対する硫
酸のモル比が0.03〜0.06の範囲に含まれる(6
)〜0の場合が特に喪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 the first expression and Table 2, hydrogen peroxide is 8 to 10 mol, sulfuric acid is 0.25 to 0.6 mol, and the molar ratio of sulfuric acid to hydrogen peroxide is in the range of 0.03 to 0.06. (6
) to 0, it can be seen that particularly favorable test results are obtained.
以上述べたようにこの発明によれば、電極集電体の負極
活物質と接する鋼鵞たは鋼合金の表面を過酸化水素、硫
酸系化学研摩液で研摩して清浄化した後、水銀イオンを
含む鋼または鋼合金の防錆剤溶液で処理し、アマルガム
化と防錆処理とを同時に行なうことにより、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, after polishing and cleaning the surface of the steel or steel alloy in contact with the negative electrode active material of the electrode current collector with hydrogen peroxide and sulfuric acid-based chemical polishing liquid, mercury ions are removed. By treating the steel or steel alloy with a rust preventive solution that contains amalgamation and rust prevention treatment at the same time, less hydrogen gas is generated, resulting in less leakage, increased impedance, and
It is possible to provide a method for manufacturing an alkaline battery that can prolong its life without bursting, and can improve work efficiency.
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。Note that the present invention is not limited to the above-mentioned embodiments, and various modifications have been made without changing the gist thereof, but the rust preventive agent is not limited to these.
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1116・・・治具7・・・正極容器
8・−陽極合剤9・・・セパレータ 1G−・・電解
液保′持材11・・・汞化亜鉛 12−絶縁パッキ
ング!3・・・環体
、計
14里・
二重−
第1図
$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 folding 1116... Jig 7... Positive electrode container
8.-Anode mixture 9...Separator 1G--Electrolyte holding material 11...Zinc chloride 12-Insulating packing! 3...Ring, total of 14 ri/double - Figure 1 $2 Figure
Claims (4)
合金の表面を、過酸化水素、硫酸系化学研摩液で研摩し
て清浄化した後、水銀イオンを含む鋼または鋼合金の防
錆剤溶液で処理し、アマルガム化と防錆処理とを同時に
行なう王権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 end of the negative electrode current collector in contact with the electrode active material or the surface of the steel alloy with a chemical polishing solution based on hydrogen peroxide or sulfuric acid, rust prevention of steel or steel alloy containing mercury ions is performed. 1. A method for producing an alkaline battery characterized by having the right to perform amalgamation and rust prevention treatment at the same time by treating it with a chemical solution.
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 above chemical polishing liquid contains 8 to 10 moles of hydrogen peroxide,
2. The method for producing an alkaline battery according to claim 1, wherein the alkaline battery contains 0.25 to 0.6 moles of sulfuric acid.
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.
とを特徴とする特許請求の範囲@1項ないし第3項のい
ずれか番c記愼されたアルカリ電池の製造方法。(4) A method for producing an alkaline battery as set forth in 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 |
---|---|---|---|
JP57038577A JPS58169770A (en) | 1982-03-11 | 1982-03-11 | Manufacturing method of alkaline battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57038577A JPS58169770A (en) | 1982-03-11 | 1982-03-11 | Manufacturing method of alkaline battery |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58169770A true JPS58169770A (en) | 1983-10-06 |
JPS6348394B2 JPS6348394B2 (en) | 1988-09-28 |
Family
ID=12529135
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57038577A Granted JPS58169770A (en) | 1982-03-11 | 1982-03-11 | Manufacturing method of alkaline battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58169770A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4780623A (en) * | 1987-02-06 | 1988-10-25 | Pioneer Electronic Corporation | Contour compensating circuit |
-
1982
- 1982-03-11 JP JP57038577A patent/JPS58169770A/en active Granted
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4780623A (en) * | 1987-02-06 | 1988-10-25 | Pioneer Electronic Corporation | Contour compensating circuit |
Also Published As
Publication number | Publication date |
---|---|
JPS6348394B2 (en) | 1988-09-28 |
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