Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPH0760782B2 - Method for manufacturing electrode foil for aluminum electrolytic capacitor - Google Patents
[go: Go Back, main page]

JPH0760782B2 - Method for manufacturing electrode foil for aluminum electrolytic capacitor - Google Patents

Method for manufacturing electrode foil for aluminum electrolytic capacitor

Info

Publication number
JPH0760782B2
JPH0760782B2 JP59243614A JP24361484A JPH0760782B2 JP H0760782 B2 JPH0760782 B2 JP H0760782B2 JP 59243614 A JP59243614 A JP 59243614A JP 24361484 A JP24361484 A JP 24361484A JP H0760782 B2 JPH0760782 B2 JP H0760782B2
Authority
JP
Japan
Prior art keywords
aluminum foil
aluminum
current
foil
counter 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.)
Expired - Lifetime
Application number
JP59243614A
Other languages
Japanese (ja)
Other versions
JPS61121318A (en
Inventor
弘 椚原
一男 岡村
涼一 島谷
健二 遠山
信義 神崎
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP59243614A priority Critical patent/JPH0760782B2/en
Publication of JPS61121318A publication Critical patent/JPS61121318A/en
Publication of JPH0760782B2 publication Critical patent/JPH0760782B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Fixed Capacitors And Capacitor Manufacturing Machines (AREA)
  • Oscillators With Electromechanical Resonators (AREA)
  • Diaphragms For Electromechanical Transducers (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は各種電子機器に用いられるアルミニウム電解コ
ンデンサ用電極箔の製造方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for producing an electrode foil for an aluminum electrolytic capacitor used in various electronic devices.

従来例の構成とその問題点 従来のこの種のアルミニウム電解コンデンサは通常塩素
イオンを含む電解液中で電解エッチングを行って実効表
面積を拡大させたアルミニウム箔と絶縁紙とを巻回し、
駆動用電解液を含漬させて構成していた。
Conventional example configuration and its problems Conventional aluminum electrolytic capacitors of this type are usually wound with an aluminum foil and an insulating paper whose effective surface area is expanded by performing electrolytic etching in an electrolytic solution containing chlorine ions,
It was constructed by impregnating the driving electrolyte.

電解エッチングによる電極箔の表面積拡大作用は、多数
の要因、例えばエッチング電流波形、電流密度、エッチ
ング液の種類、濃度、温度、そして添加剤の種類及び濃
度さらにエッチング前処理、中間処理、後処理、アルミ
ニウム生箔の種類等により影響を受ける。
The effect of increasing the surface area of the electrode foil by electrolytic etching is a number of factors, such as etching current waveform, current density, type of etching solution, concentration, temperature, and type and concentration of additives, as well as pretreatment, intermediate treatment, and posttreatment. It is affected by the type of aluminum foil.

電流波形に関する検討も、以前から行われており、矩形
波電流を用いる方法として、英国特許第1169234号明細
書、特開昭57−132322号公報等が知られている。
Studies on the current waveform have been conducted for some time, and as methods of using a rectangular wave current, British Patent No. 1169234, JP-A-57-132322 and the like are known.

これらの方法は、塩素イオンを含む水溶液中において、
矩形波電流を流し、電解エッチングを行う方法である。
These methods, in an aqueous solution containing chloride ions,
This is a method in which a rectangular wave current is passed and electrolytic etching is performed.

しかし、これらの方法では表面拡大率に限界があり、ア
ルミニウム電解コンデンサの小形化やコストダウンには
限界があるという欠点があった。
However, these methods have a drawback in that the surface expansion rate is limited, and there is a limitation in downsizing and cost reduction of the aluminum electrolytic capacitor.

発明の目的 本発明は上記した従来の欠点を除去するもので、従来よ
り高い拡面倍率が得られるアルミニウム箔を用いること
により小形化が図れるアルミニウム電解コンデンサ用電
極箔の製造方法を提供することを目的とするものであ
る。
An object of the present invention is to eliminate the above-mentioned conventional drawbacks, and to provide a method for manufacturing an electrode foil for an aluminum electrolytic capacitor, which can be miniaturized by using an aluminum foil which can obtain a higher surface expansion ratio than the conventional one. It is intended.

発明の構成 上記目的を達成するために本発明のアルミニウム電解コ
ンデンサ用電極箔の製造方法は、濃度が1〜4.5mol/
である塩素イオンを含む水溶液に、アルミニウム表面に
酸化皮膜を形成する作用を有するとともに、濃度が0.1
〜1mol/である硫酸イオンもしくは蓚酸イオンを添加
し、この水溶液中で、アルミニウム箔と対極との間に、
アルミニウム箔の対極に対する電位が正または負となる
ことを繰り返すような矩形波電流を通電してアルミニウ
ム箔の表面に酸化皮膜を形成すると同時にアルミニウム
箔を電解エッチングし、前記矩形波電流は、アルミニウ
ム箔から対極に流れる正電流密度が0.5〜2A/cm2で、そ
の流れる時間が2〜15msであり、一方、対極からアルミ
ニウム箔に流れる負電流密度が0.1〜0.5A/cm2で、その
流れる時間が2〜15msである矩形波電流を用いるように
したものである。
Structure of the invention In order to achieve the above object, a method for producing an electrode foil for an aluminum electrolytic capacitor of the present invention, the concentration is 1 ~ 4.5mol /
Aqueous solution containing chlorine ions, which has the effect of forming an oxide film on the aluminum surface, has a concentration of 0.1
~ 1mol / sulfate ion or oxalate ion is added, in this aqueous solution, between the aluminum foil and the counter electrode,
The aluminum foil is electrolytically etched at the same time as forming an oxide film on the surface of the aluminum foil by applying a rectangular wave current such that the potential with respect to the counter electrode of the aluminum foil is repeatedly positive or negative, and the rectangular wave current is the aluminum foil. The positive current density flowing from the counter electrode to the counter electrode is 0.5 to 2 A / cm 2 , and the flowing time is 2 to 15 ms, while the negative current density flowing from the counter electrode to the aluminum foil is 0.1 to 0.5 A / cm 2 , and the flowing time is Is a rectangular wave current of 2 to 15 ms.

この製造方法により、従来のものよりも、表面の酸化皮
膜量を増加させることができ、従来より高い拡面倍率を
得ることができるようになったものである。
With this manufacturing method, the amount of oxide film on the surface can be increased as compared with the conventional method, and a higher surface expansion ratio than that of the conventional method can be obtained.

その理由は以下に述べる通りである。The reason is as described below.

矩形波電流による電解エッチングは、アルミニウム箔か
ら対極に正電流が流れる時に溶解が生じ対極からアルミ
ニウム箔に負電流が流れる時に、表面に酸化皮膜が形成
され、それが繰り返される。なぜなら、正電流が流れる
時には、電解液中の塩素イオンがアルミニウムを攻撃
し、アルミニウムを溶解する。負電流が流れる時はアル
ミニウム箔と電解液との界面で電子がアルミニウム箔か
ら電解液に伝わる電気化学反応が生じるため、界面付近
のH+イオンが還元され水素ガスとして外部へ脱出する。
The electrolytic etching with a rectangular wave current is repeated when a positive current flows from the aluminum foil to the counter electrode to cause melting and a negative current flows from the counter electrode to the aluminum foil to form an oxide film on the surface. This is because, when a positive current flows, chlorine ions in the electrolytic solution attack aluminum and dissolve it. When a negative current flows, an electrochemical reaction occurs in which electrons are transferred from the aluminum foil to the electrolytic solution at the interface between the aluminum foil and the electrolytic solution, so that H + ions near the interface are reduced and escape to the outside as hydrogen gas.

その結果、アルミニウム箔界面での水素イオン濃度が減
少し、電解液のPHが上昇し、表面に酸化アルミニウム皮
膜が形成されるからである。
As a result, the hydrogen ion concentration at the aluminum foil interface decreases, the PH of the electrolytic solution increases, and an aluminum oxide film is formed on the surface.

表面の酸化皮膜は、エッチングが進行し、腐食孔が深
く、かつ細くなった時、腐食孔が途中で欠け落ちたり溶
解消失されてしまうのを防ぐ効果を有する。
The oxide film on the surface has an effect of preventing the corrosion hole from chipping off or being dissolved and disappeared in the middle when etching progresses and the corrosion hole becomes deep and thin.

ところが、従来の方法によると、負電流が流れ酸化皮膜
が形成される反応は、電解液中のH+イオンとアルミニウ
ム箔との界面での電気化学反応に限られ、エッチング後
表面に形成される酸化皮膜量は、0.1mg/cm2程度であ
る。その結果、腐食孔の溶解・欠落を十分に止めること
ができず、目標とする高い拡面倍率を得ることができな
かった。
However, according to the conventional method, the reaction in which a negative current flows and an oxide film is formed is limited to the electrochemical reaction at the interface between the H + ion in the electrolytic solution and the aluminum foil, and is formed on the surface after etching. The amount of oxide film is about 0.1 mg / cm 2 . As a result, it was not possible to sufficiently stop the dissolution and lack of corrosion holes, and it was not possible to obtain the target high surface expansion ratio.

本発明の製造方法によれば、負電流が流れて酸化皮膜が
形成される時、酸化皮膜を形成する作用を有する添加剤
の硫酸イオンもしくは蓚酸イオンの効果により、表面の
酸化皮膜量が従来方法より多く、0.3〜0.6mg/cm2に達す
る。
According to the production method of the present invention, when a negative current flows to form an oxide film, the amount of the oxide film on the surface is reduced by the conventional method due to the effect of the sulfate ion or oxalate ion of the additive having the action of forming the oxide film. More, reaching 0.3-0.6 mg / cm 2 .

その結果、腐食孔溶解・欠落が防止され、高い拡面倍率
が得られるのである。
As a result, dissolution and loss of corrosion holes are prevented, and a high surface expansion ratio can be obtained.

実施例の説明 次に具体的な実施例について、図面を用いて説明する。Description of Embodiments Next, specific embodiments will be described with reference to the drawings.

〔実施例1〕 塩素イオン濃度についての検討結果を第1図に示す。た
だし塩素イオンとして、食塩水溶液を用いた。第1図か
らも明らかなように塩素イオン濃度が1〜4.5mol/の
範囲において、高い拡面倍率が得られていることがわか
る。
[Example 1] Fig. 1 shows the results of studies on the chlorine ion concentration. However, a saline solution was used as the chlorine ions. As is clear from FIG. 1, it is understood that a high surface expansion ratio is obtained in the range of chlorine ion concentration of 1 to 4.5 mol /.

〔実施例2〕 添加剤濃度と、表面の酸化皮膜量および拡面倍率との関
係についての検討結果を第2図,第3図に示す。添加剤
濃度が0.1〜1.0mol/の範囲において効果が高いことが
明らかであり、添加剤濃度が1mol/を越えると逆に拡
面倍率が低下するのは表面の酸化皮膜量がある程度以上
になると、かえって表面の活性度を減少させ、腐食孔の
発生頻度を減少させるためと考えられている。
[Example 2] Fig. 2 and Fig. 3 show the results of studies on the relationship between the additive concentration, the amount of oxide film on the surface, and the surface expansion ratio. It is clear that the effect is high in the additive concentration range of 0.1 to 1.0 mol /, and when the additive concentration exceeds 1 mol /, on the contrary, the surface expansion ratio decreases when the amount of oxide film on the surface exceeds a certain amount. On the contrary, it is considered that the activity of the surface is reduced and the frequency of occurrence of corrosion holes is reduced.

〔実施例3〕 電流密度についての検討結果を第4図,第5図に示す。
ただし塩素イオンとして、食塩を用い添加剤として芒硝
を用いた。
[Embodiment 3] The examination results of the current density are shown in FIG. 4 and FIG.
However, salt was used as the chlorine ion, and Glauber's salt was used as the additive.

第4図,第5図からも明らかなように正電流密度が0.5
〜2.0A/cm2、負電流密度0.1〜0.5A/cm2の範囲におい
て、高い拡面倍率が得られていることがわかる。
As is clear from FIGS. 4 and 5, the positive current density is 0.5
It can be seen that a high surface expansion ratio is obtained in the range of up to 2.0 A / cm 2 and negative current density of 0.1 to 0.5 A / cm 2 .

〔実施例4〕 正電流時間と負電流時間についての検討結果を第6図,
第7図に示す。この第6図,第7図からも明らかなよう
に正電流時間が2〜15ms、負電流時間が2〜15msの範囲
において高い拡面倍率が得られていることがわかる。
[Embodiment 4] FIG. 6 shows the results of study on positive current time and negative current time.
It is shown in FIG. As is clear from FIGS. 6 and 7, it is understood that a high surface expansion ratio is obtained in the range of the positive current time of 2 to 15 ms and the negative current time of 2 to 15 ms.

〔実施例5〕 正電流と負電流との過渡時間についての検討結果を第8
図に示す。この第8図からも明らかなように過渡時間が
長くなると、拡面倍率が減少するが、2ms以下だと高い
拡面倍率が得られていることがわかる。過渡時間が増加
すると、不適当な電流密度でエッチングする割合が相対
的に増加するためと考えられている。
[Embodiment 5] The results of the examination of the transient time between the positive current and the negative current are shown in Section 8.
Shown in the figure. As is clear from FIG. 8, the surface expansion ratio decreases as the transition time becomes longer, but it can be seen that a high surface expansion ratio is obtained at 2 ms or less. It is considered that the proportion of etching at an inappropriate current density relatively increases as the transition time increases.

発明の効果 以上のように本発明のアルミニウム電解コンデンサ用電
極箔の製造方法によれば、濃度が1〜4.5mol/である
塩素イオンを含む水溶液に、アルミニウム表面に酸化皮
膜を形成する作用を有するとともに、濃度が0.1〜1mol/
である硫酸イオンもしくは蓚酸イオンを添加し、この
水溶液中で、アルミニウム箔と対極との間に、アルミニ
ウム箔の対極に対する電位が正または負となることを繰
り返すような矩形波電流を通電してアルミニウム箔の表
面に酸化皮膜を形成すると同時にアルミニウム箔を電解
エッチングするようにしているため、エッチング後にア
ルミニウム箔の表面に形成される酸化皮膜量を従来方法
に比べて多くすることができ、これにより、腐食孔の溶
解・欠落を十分に止めることができるため、従来より高
い拡面倍率が得られる。また、アルミニウム箔に通電さ
れる矩形波電流は、アルミニウム箔から対極に流れる正
電流密度を0.5〜2A/cm2とし、かつその流れる時間を2
〜15msとし、さらに対極からアルミニウム箔に流れる負
電流密度を0.1〜0.5A/cm2とし、かつその流れる時間を
2〜15msとしているため、この範囲規定によりさらに高
い拡面倍率が得られることになり、そしてこのようなア
ルミニウム箔を陽極箔として用いることによりアルミニ
ウム電解コンデンサの小形化とコストダウンが図れるも
のである。
EFFECTS OF THE INVENTION As described above, according to the method for producing an electrode foil for an aluminum electrolytic capacitor of the present invention, an aqueous solution containing chlorine ions having a concentration of 1 to 4.5 mol / has the action of forming an oxide film on the aluminum surface. Together with the concentration of 0.1-1 mol /
Sulfate ion or oxalate ion is added, and in this aqueous solution, a rectangular wave current is repeatedly applied between the aluminum foil and the counter electrode so that the potential with respect to the counter electrode of the aluminum foil becomes positive or negative. Since the aluminum foil is electrolytically etched at the same time that the oxide film is formed on the surface of the foil, the amount of the oxide film formed on the surface of the aluminum foil after etching can be increased as compared with the conventional method. Since it is possible to sufficiently prevent the dissolution and loss of the corrosion holes, it is possible to obtain a surface expansion ratio higher than before. In addition, the rectangular wave current applied to the aluminum foil has a positive current density of 0.5 to 2 A / cm 2 flowing from the aluminum foil to the counter electrode and a flowing time of 2 seconds.
-15 ms, the negative current density flowing from the counter electrode to the aluminum foil is 0.1-0.5 A / cm 2 , and the flowing time is 2-15 ms. By using such an aluminum foil as the anode foil, the aluminum electrolytic capacitor can be downsized and the cost can be reduced.

【図面の簡単な説明】[Brief description of drawings]

第1図は電解液中の塩素イオン濃度と拡面倍率との関係
を示す特性図、第2図は添加剤濃度と拡面倍率との関係
を示す特性図、第3図は添加剤濃度と表面皮膜量との関
係を示す特性図、第4図は正電流密度と拡面倍率との関
係を示す特性図、第5図は負電流密度と拡面倍率との関
係を示す特性図、第6図は正電流時間と拡面倍率との関
係を示す特性図、第7図は負電流時間と拡面倍率との関
係を示す特性図、第8図は正電流と負電流との間の過渡
電流時間と拡面倍率との関係を示す特性図である。
FIG. 1 is a characteristic diagram showing the relationship between the chlorine ion concentration in the electrolytic solution and the surface expansion ratio, FIG. 2 is a characteristic diagram showing the relationship between the additive concentration and the surface expansion ratio, and FIG. 3 is the additive concentration. FIG. 4 is a characteristic diagram showing the relationship between the surface coating amount, FIG. 4 is a characteristic diagram showing the relationship between the positive current density and the surface expansion ratio, and FIG. 5 is a characteristic diagram showing the relationship between the negative current density and the surface expansion ratio. 6 is a characteristic diagram showing the relationship between the positive current time and the surface expansion ratio, FIG. 7 is a characteristic diagram showing the relationship between the negative current time and the surface expansion ratio, and FIG. 8 is a graph showing the relationship between the positive current and the negative current. It is a characteristic view which shows the relationship between transient current time and surface expansion ratio.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 遠山 健二 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 神崎 信義 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (56)参考文献 特開 昭58−223311(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Kenji Toyama, 1006 Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Nobuyoshi Kanzaki, 1006, Kadoma, Kadoma City, Osaka Matsushita Electric Industrial Co., Ltd. 56) References JP-A-58-223311 (JP, A)

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】濃度が1〜4.5mol/である塩素イオンを
含む水溶液に、アルミニウム表面に酸化皮膜を形成する
作用を有するとともに、濃度が0.1〜1mol/である硫酸
イオンもしくは蓚酸イオンを添加し、この水溶液中で、
アルミニウム箔と対極との間に、アルミニウム箔の対極
に対する電位が正または負となることを繰り返すような
矩形波電流を通電してアルミニウム箔の表面に酸化皮膜
を形成すると同時にアルミニウム箔を電解エッチング
し、前記矩形波電流は、アルミニウム箔から対極に流れ
る正電流密度が0.5〜2A/cm2で、その流れる時間が2〜1
5msであり、一方、対極からアルミニウム箔に流れる負
電流密度が0.1〜0.5A/cm2で、その流れる時間が2〜15m
sである矩形波電流を用いるようにしたことを特徴とす
るアルミニウム電解コンデンサ用電極箔の製造方法。
1. An aqueous solution containing chloride ions having a concentration of 1 to 4.5 mol /, which has a function of forming an oxide film on the aluminum surface and is added with a sulfate ion or an oxalate ion having a concentration of 0.1 to 1 mol /. , In this aqueous solution,
Between the aluminum foil and the counter electrode, a rectangular wave current that repeatedly causes the potential of the counter electrode of the aluminum foil to become positive or negative is applied to form an oxide film on the surface of the aluminum foil and at the same time electrolytically etch the aluminum foil. The square wave current has a positive current density of 0.5 to 2 A / cm 2 flowing from the aluminum foil to the counter electrode and a flowing time of 2 to 1
5 ms, while the negative current density flowing from the counter electrode to the aluminum foil is 0.1 to 0.5 A / cm 2 , and the flowing time is 2 to 15 m.
A method of manufacturing an electrode foil for an aluminum electrolytic capacitor, characterized in that a rectangular wave current of s is used.
【請求項2】矩形波電流は、正電流から負電流に、もし
くは負電流から正電流に変わる過渡時間が2ms以下であ
ることを特徴とする特許請求の範囲第1項記載のアルミ
ニウム電解コンデンサ用電極箔の製造方法。
2. The aluminum electrolytic capacitor according to claim 1, wherein the rectangular wave current has a transition time of 2 ms or less at which it changes from a positive current to a negative current or from a negative current to a positive current. Method for manufacturing electrode foil.
JP59243614A 1984-11-19 1984-11-19 Method for manufacturing electrode foil for aluminum electrolytic capacitor Expired - Lifetime JPH0760782B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59243614A JPH0760782B2 (en) 1984-11-19 1984-11-19 Method for manufacturing electrode foil for aluminum electrolytic capacitor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59243614A JPH0760782B2 (en) 1984-11-19 1984-11-19 Method for manufacturing electrode foil for aluminum electrolytic capacitor

Publications (2)

Publication Number Publication Date
JPS61121318A JPS61121318A (en) 1986-06-09
JPH0760782B2 true JPH0760782B2 (en) 1995-06-28

Family

ID=17106436

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59243614A Expired - Lifetime JPH0760782B2 (en) 1984-11-19 1984-11-19 Method for manufacturing electrode foil for aluminum electrolytic capacitor

Country Status (1)

Country Link
JP (1) JPH0760782B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4793957B2 (en) * 2007-01-31 2011-10-12 ニチコン株式会社 Method for producing aluminum electrode foil for electrolytic capacitor

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58223311A (en) * 1982-06-22 1983-12-24 エルナ−株式会社 Method of etching aluminum foil for electrolytic condenser

Also Published As

Publication number Publication date
JPS61121318A (en) 1986-06-09

Similar Documents

Publication Publication Date Title
JPH0235443B2 (en)
US6440288B1 (en) Method for preparing anode electrode for high voltage electrolytic capacitor
US3190822A (en) Process for electrolytically etching valve metal surfaces
JPH0760782B2 (en) Method for manufacturing electrode foil for aluminum electrolytic capacitor
JP3252313B2 (en) Etching method of aluminum foil for electrolytic capacitor
JP2000077275A (en) Manufacturing method of electrode foil for aluminum electrolytic capacitor
KR940013301A (en) Method of manufacturing metal foil by electrolysis
JP2000068159A (en) Solid electrolytic capacitor electrode foil therefor and its manufacture
JPS61210191A (en) Etching method for aluminum electrolytic capacitor foil
KR940011667A (en) Metal foil manufacturing method by electrolysis
JPH0353099A (en) Method for processing ta base material
JP3269818B2 (en) Surface roughened copper, method for producing the same, and printed circuit board using the same
US11230794B2 (en) Use of nonafluorobutanesulfonic acid in a low PH etch solution to increase aluminum foil capacitance
JP2002246274A (en) Electrode foil for aluminum electrolytic capacitor and method of manufacturing the same
JP2001244153A (en) Manufacturing method of electrode foil for aluminum electrolytic capacitor
JPH0665208B2 (en) Aluminum electrolytic capacitor
JPS60169131A (en) Method of producing electrode foil for aluminum electrolytic condenser
JP2638038B2 (en) Manufacturing method of electrode foil for aluminum electrolytic capacitor
JPH1187186A (en) Etching method of electrode foil for aluminum electrolytic capacitor
JP2002260969A (en) Manufacturing method of anode foil for aluminum electrolytic capacitor
JPH0620030B2 (en) Method for manufacturing electrode foil for aluminum electrolytic capacitor
JP2745520B2 (en) Manufacturing method of electrode foil for aluminum electrolytic capacitor
SU833421A1 (en) Electrolyte for electrochemical treatment
JP2765105B2 (en) Method for producing electrode foil for aluminum electrolytic capacitor
KR930003433B1 (en) Etching liquid of aluminium foil