JPH0665208B2 - Aluminum electrolytic capacitor - Google Patents

Aluminum electrolytic capacitor

Info

Publication number
JPH0665208B2
JPH0665208B2 JP59117011A JP11701184A JPH0665208B2 JP H0665208 B2 JPH0665208 B2 JP H0665208B2 JP 59117011 A JP59117011 A JP 59117011A JP 11701184 A JP11701184 A JP 11701184A JP H0665208 B2 JPH0665208 B2 JP H0665208B2
Authority
JP
Japan
Prior art keywords
aluminum foil
aluminum
current density
time
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
JP59117011A
Other languages
Japanese (ja)
Other versions
JPS60260123A (en
Inventor
弘 椚原
一男 岡村
涼一 島谷
健一 遠山
信義 神崎
浩一 小島
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 JP59117011A priority Critical patent/JPH0665208B2/en
Publication of JPS60260123A publication Critical patent/JPS60260123A/en
Publication of JPH0665208B2 publication Critical patent/JPH0665208B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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利用されるアルミニウム電解コ
ンデンサに関するものである。
TECHNICAL FIELD The present invention relates to 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い実効表面
積を拡大したアルミニウム箔と絶縁紙とを巻回し、駆動
用電解液を含浸したコンデンサ素子をケースに封入して
構成していた。
Conventional example configuration and its problems Conventional aluminum electrolytic capacitors of this type are usually formed by electrolytically etching in an electrolytic solution containing chlorine ions, winding an aluminum foil with an expanded effective surface area, and insulating paper to form a driving electrolytic solution. The impregnated capacitor element was enclosed in a case.

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
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1,169,234号明
細書、特開昭57−132322号公報等が知られている。これ
らの方法は、塩素イオンとして食塩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。
Studies on the current waveform have been conducted for some time, and as methods of using a rectangular wave current, British Patent No. 1,169,234, JP-A-57-132322 and the like are known. These methods are methods in which a rectangular wave current is passed in an aqueous solution containing chloride as chlorine ions to carry out electrolytic etching.

しかしながら、これらの方法では、中性の食塩水を利用
しているため、電解エッチング中に溶出したアルミニウ
ムイオンが水酸化アルミニウムの沈澱物を生成し、生産
装置や配管等に付着し、その除去のために、定期的に設
備を停止しなければならず、設備の稼動率を低下させる
という欠点があった。
However, in these methods, since neutral salt solution is used, aluminum ions eluted during electrolytic etching produce aluminum hydroxide precipitates, which adhere to production equipment and pipes, etc. Therefore, there is a drawback in that the equipment must be regularly stopped, and the operating rate of the equipment is reduced.

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、水酸化
アルミニウムの沈澱物が生じない液組成において、高倍
率の電極箔を生産し、生産設備の稼動率を向上させるこ
とにより、アルミニウム電解コンデンサのコストダウン
を図ることを目的とするものである。
The object of the present invention is to eliminate the above-mentioned conventional drawbacks, by producing a high-magnification electrode foil in a liquid composition that does not cause precipitation of aluminum hydroxide, by improving the operating rate of production equipment, The purpose is to reduce the cost of the aluminum electrolytic capacitor.

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
ンデンサは、塩素イオンとして塩酸と塩化アルミニウム
を含む水溶液中で、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又は負となること
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
を電解エッチングするとともに、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/c
m2で、その流れる時間が1〜15msであり、一方、対極か
らアルミニウム箔に流れる負極電流密度が0.1〜0.5A/c
m2で、その流れる時間が1〜5msである矩形波電流を用
いて構成したアルミニウム箔を陽極箔として用いたもの
である。
In order to achieve the above object, the aluminum electrolytic capacitor of the present invention, in an aqueous solution containing hydrochloric acid and aluminum chloride as chlorine ions, between the aluminum foil and the counter electrode, the potential of the aluminum foil to the counter electrode is positive or negative. The rectangular wave current has a positive current density of 0.5 to 2 A / c flowing from the aluminum foil to the counter electrode while the aluminum foil is electrolytically etched by applying a rectangular wave current.
m 2 and the flowing time is 1 to 15 ms, while the negative electrode current density flowing from the counter electrode to the aluminum foil is 0.1 to 0.5 A / c.
An aluminum foil configured by using a square wave current having a flowing time of 1 to 5 ms at m 2 was used as an anode foil.

上記構成によれば、アルミニウム箔を電解エッチングす
る場合、塩素イオンとして塩酸と塩化アルミニウムを含
む水溶液中で行っているため、水酸化アルミニウムの沈
澱物が生じることはなく、またアルミニウム箔に通電さ
れる矩形波電流は正電流密度を0.5〜2A/cm2とし、かつ
その流れる時間を1〜15msとし、さらに負電流密度を0.
1〜0.5A/cm2とし、かつその流れる時間を1〜5msとし
ているため、アルミニウム箔の表面に酸化皮膜がつきす
ぎることもなくなって、溶解を均一に行え、これによ
り、高い拡面倍率を得ることができるとともに、水酸化
アルミニウムの沈殿物が生産装置や配管等に付着するこ
ともなくなるため、生産設備の稼動率の向上が図れてア
ルミニウム電解コンデンサのコストダウンに大きく寄与
するものである。
According to the above configuration, when the aluminum foil is electrolytically etched, since it is performed in an aqueous solution containing hydrochloric acid and aluminum chloride as chlorine ions, no aluminum hydroxide precipitate is generated, and the aluminum foil is energized. The square wave current has a positive current density of 0.5 to 2 A / cm 2 , a flowing time of 1 to 15 ms, and a negative current density of 0.
Since it is set to 1 to 0.5 A / cm 2 and the flowing time is set to 1 to 5 ms, there is no excessive oxide film on the surface of the aluminum foil, and the melting can be performed uniformly, which results in a high surface expansion ratio. In addition to being able to obtain the same, the precipitation of aluminum hydroxide is prevented from adhering to the production equipment, pipes, etc., so that the operating rate of the production equipment can be improved and the cost of the aluminum electrolytic capacitor can be greatly reduced.

実施例の説明 以下、本発明の実施例について図面を用いて説明する。Description of Embodiments Embodiments of the present invention will be described below with reference to the drawings.

実施例1 第1図は正電流時間を変化させた場合における拡面倍率
の検討結果を示し、また第2図は負電流時間を変化させ
た場合における拡面倍率の検討結果を示したものであ
る。
Example 1 FIG. 1 shows the examination result of the surface enlargement magnification when the positive current time was changed, and FIG. 2 shows the examination result of the surface enlargement magnification when the negative current time was changed. is there.

なお、実験条件は以下の通りである。The experimental conditions are as follows.

第1図の実験条件 正電流時間 :1〜21ms(2msステップ) 正電流密度 :1.0A/cm2 負電流時間 :1.0ms 負電流密度 :0.2A/cm2 エッチング時間 :1分 エッチング温度 :90℃ 液組成 :HCl5%,AlCl35% 第2図の実験条件 正電流時間 :15ms 正電流密度 :1.0A/cm2 負電流時間 :1〜15ms(2msステップ) 負電流密度 :0.2A/cm2 エッチング時間 :1分 エッチング温度:90℃ 液組成:HCl5%,AlCl3 5%第1図,第2図から明らかなように正電流の流れる
時間が1〜15ms、負電流の流れる時間が1〜5msの範囲
において高い拡面倍率が得られている。
Experimental conditions positive current time in the first view: 1~21ms (2ms step) the positive current density: 1.0A / cm 2 negative current time: 1.0 ms negative current density: 0.2 A / cm 2 Etching time: 1 minute etching temperature: 90 ° C Liquid composition: HCl 5%, AlCl 3 5% Experimental conditions in Fig. 2 Positive current time: 15ms Positive current density: 1.0A / cm 2 Negative current time: 1 to 15ms (2ms step) Negative current density: 0.2A / cm 2 Etching time: 1 minute Etching temperature: 90 ° C. Liquid composition: HCl 5%, AlCl 3 5% As can be seen from FIGS. 1 and 2, positive current flow time is 1 to 15 ms, negative current flow time is 1 High surface expansion ratio is obtained in the range of ~ 5ms.

負電流時間の最適値の幅が正電流時間の最適値の幅より
短いのは負電流時間が5ms以上になると表面に酸化皮膜
がつきすぎるために、溶解が不均一になるためと考えら
れる。
The reason why the width of the optimum value of the negative current time is shorter than the width of the optimum value of the positive current time is considered to be that the oxide film is excessively attached to the surface when the negative current time is 5 ms or more, so that the dissolution becomes nonuniform.

実施例2 第3図(a)は正電流密度を変化させた場合における拡
面倍率の検討結果を示し、また第3図(b)は負電流密
度を変化させた場合における拡面倍率の検討結果を示し
たものである。
Example 2 FIG. 3 (a) shows the examination result of the surface expansion ratio when the positive current density was changed, and FIG. 3 (b) shows the examination of the surface expansion ratio when the negative current density was changed. The results are shown.

なお、実験条件は以下の通りである。The experimental conditions are as follows.

第3図(a)の実験条件 正電流時間 :15ms 正電流密度 :0.3〜2.3A/cm2 電流時間 :1.0ms 負電流密度 :0.2A/cm2 エッチング時間 :1分 エッチング温度 :90℃ 液組成 :HCl5%,AlCl35% 第3図(b)の実験条件 正電流時間 :15ms 正電流密度 :1.0A/cm2 負電流時間 :1.0ms 負電流密度 :0.1〜1.3A/cm2 エッチング時間 :1分 エッチング温度 :90℃ 液組成 :HCl5%,AlCl35% 第3図(a),(b)から明らかなように正電流密度が
0.5〜2A/cm2、負電流密度が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。
Figure 3 (a) experimental conditions positive current time: 15 ms positive current density: 0.3~2.3A / cm 2 Current Time: 1.0 ms negative current density: 0.2 A / cm 2 Etching time: 1 minute etching temperature: 90 ° C. solution Composition: HCl 5%, AlCl 3 5% Experimental conditions in Fig. 3 (b) Positive current time: 15ms Positive current density: 1.0A / cm 2 Negative current time: 1.0ms Negative current density: 0.1 to 1.3A / cm 2 Etching Time: 1 minute Etching temperature: 90 ° C Liquid composition: HCl 5%, AlCl 3 5% As shown in Figs. 3 (a) and 3 (b), the positive current density is
In the range of 0.5 to 2 A / cm 2 and the negative current density of 0.1 to 0.5 A / cm 2 , high surface expansion ratio is obtained.

実施例3 本発明の条件によるエッチング拡面倍率と従来条件との
比較を下の表に示す。
Example 3 The table below shows a comparison between the etching surface enlargement ratio under the conditions of the present invention and the conventional conditions.

方法1は従来例による方法である。方法3は本発明例で
ある。方法2は本発明でHCl濃度がゼロになった場合で
ある。この方法でも沈澱は生じないが、液の電導度が低
くなるため、同一溶解減量を得るため、より多くの電力
消費を必要とする。
Method 1 is a conventional method. Method 3 is an example of the present invention. Method 2 is a case where the HCl concentration becomes zero in the present invention. This method also does not cause precipitation, but since the conductivity of the liquid is low, more power consumption is required to obtain the same loss on dissolution.

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は、
アルミニウム箔を電解エッチングする場合、塩素イオン
として塩酸と塩化アルミニウムを含む水溶液中で行って
いるため、水酸化アルミニウムの沈澱物が生じることは
なく、またアルミニウム箔に通電される矩形波電流は正
電流密度を0.5〜2A/cm2とし、かつその流れる時間を1
〜15msとし、さらに負電流密度を0.1〜0.5A/cm2とし、
かつその流れる時間を1〜5msとしているため、アルミ
ニウム箔の表面に酸化皮膜がつきすぎることもなくなっ
て、溶解を均一に行え、これにより、高い拡面倍率を得
ることができるとともに、水酸化アルミニウムの沈澱物
が生産装置や配管等に付着することもなくなるため、生
産設備の稼動率の向上が図れてアルミニウム電解コンデ
ンサのコストダウンに大きく寄与するものである。
As described above, the aluminum electrolytic capacitor of the present invention is
When electrolytically etching aluminum foil, since it is performed in an aqueous solution containing hydrochloric acid and aluminum chloride as chlorine ions, aluminum hydroxide precipitates do not occur, and the square wave current applied to the aluminum foil is a positive current. The density is 0.5 to 2 A / cm 2 and the flowing time is 1
And ~15Ms, further negative current density was 0.1~0.5A / cm 2,
Moreover, since the flowing time is set to 1 to 5 ms, the surface of the aluminum foil will not be overly coated with an oxide film, and the dissolution can be carried out uniformly, whereby a high surface expansion ratio can be obtained and aluminum hydroxide can be obtained. Since the deposit of No. 1 does not adhere to the production equipment, piping, etc., the operating rate of the production equipment can be improved and the cost of the aluminum electrolytic capacitor can be greatly reduced.

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

第1図は正電流時間と拡面倍率との関係を示す特性図、
第2図は負電流時間と拡面倍率との関係を示す特性図、
第3図(a),(b)は正電流密度及び負電流密度と拡
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 positive current time and the surface expansion ratio,
FIG. 2 is a characteristic diagram showing the relationship between the negative current time and the surface expansion ratio,
3 (a) and 3 (b) are characteristic diagrams showing the relationship between the positive current density and the negative current density and the surface expansion ratio.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 遠山 健一 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 (72)発明者 小島 浩一 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) 特開 昭59−70800(JP,A) ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Kenichi Toyama 1006 Kadoma, Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Nobuyoshi Kanzaki 1006, Kadoma, Kadoma City, Osaka Matsushita Electric Industrial Co., Ltd. 72) Inventor Koichi Kojima, Kadoma City, Osaka Prefecture 1006 Kadoma, Matsushita Electric Industrial Co., Ltd. (56) References JP-A-58-223311 (JP, A) JP-A-59-70800 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】塩素イオンとして塩酸と塩化アルミニウム
を含む水溶液中で、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又は負となること
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
を電解エッチングするとともに、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/c
m2で、その流れる時間が1〜15ms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1〜5msである矩形波電流を用い
て構成したアルミニウム箔を陽極箔として用いたアルミ
ニウム電解コンデンサ。
1. A rectangular wave current is repeatedly applied between an aluminum foil and a counter electrode in an aqueous solution containing hydrochloric acid and aluminum chloride as chlorine ions so that the potential of the aluminum foil with respect to the counter electrode becomes positive or negative. And electrolytically etching the aluminum foil, the square wave current has a positive current density of 0.5 to 2 A / c flowing from the aluminum foil to the counter electrode.
m 2 and the flowing time is 1 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
Then, an aluminum electrolytic capacitor using an aluminum foil, which is formed by using a rectangular wave current having a flowing time of 1 to 5 ms, as an anode foil.
JP59117011A 1984-06-07 1984-06-07 Aluminum electrolytic capacitor Expired - Lifetime JPH0665208B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59117011A JPH0665208B2 (en) 1984-06-07 1984-06-07 Aluminum electrolytic capacitor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59117011A JPH0665208B2 (en) 1984-06-07 1984-06-07 Aluminum electrolytic capacitor

Publications (2)

Publication Number Publication Date
JPS60260123A JPS60260123A (en) 1985-12-23
JPH0665208B2 true JPH0665208B2 (en) 1994-08-22

Family

ID=14701241

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59117011A Expired - Lifetime JPH0665208B2 (en) 1984-06-07 1984-06-07 Aluminum electrolytic capacitor

Country Status (1)

Country Link
JP (1) JPH0665208B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6288315A (en) * 1985-10-15 1987-04-22 長井電子工業協同組合 Etching of aluminum foil for electrolytic capacitor

Family Cites Families (2)

* 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
US4427506A (en) * 1982-09-24 1984-01-24 Sprague Electric Company AC Etching of aluminum capacitor foil

Also Published As

Publication number Publication date
JPS60260123A (en) 1985-12-23

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