JP3309176B2 - Method of forming electrode foil for medium and high pressure aluminum electrolytic capacitors - Google Patents

Method of forming electrode foil for medium and high pressure aluminum electrolytic capacitors

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Publication number
JP3309176B2
JP3309176B2 JP10207096A JP10207096A JP3309176B2 JP 3309176 B2 JP3309176 B2 JP 3309176B2 JP 10207096 A JP10207096 A JP 10207096A JP 10207096 A JP10207096 A JP 10207096A JP 3309176 B2 JP3309176 B2 JP 3309176B2
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JP
Japan
Prior art keywords
treatment
minutes
hydration
pure water
acid
Prior art date
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Expired - Fee Related
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JP10207096A
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Japanese (ja)
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JPH09275040A (en
Inventor
健 海老原
隆 梶山
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.)
Nippon Light Metal Co Ltd
Japan Capacitor Industrial Co Ltd
Original Assignee
Nippon Light Metal Co Ltd
Japan Capacitor Industrial Co Ltd
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、特に中高圧用のア
ルミニウム電解コンデンサ用電極箔に有効な化成方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for forming an electrode foil for an aluminum electrolytic capacitor for medium and high pressures.

【0002】[0002]

【従来の技術】従来、アルミニウム電解コンデンサの陽
極アルミニウム箔は拡面処理を施した高純度のアルミニ
ウム箔に水和処理を行なったのち、陽極酸化処理を行な
って結晶性の酸化アルミニウムを表面に生成し、これを
誘電体皮膜として利用している。ところで上記におい
て、陽極酸化により結晶性の酸化アルミニウムを形成す
る際に必然的に空孔欠陥が発生する。この空孔欠陥は、
水和処理により生成した水酸化アルミニウムが脱水する
際に起こる体積収縮により発生し、その内部には酸素ガ
スが封じ込められる。この空孔欠陥が誘電体皮膜に存在
すると、電解コンデンサとして使用したときに、空孔欠
陥が露出して皮膜の劣化をきたすので、通常は陽極酸化
処理後に熱処理・化学的処理・機械的処理を施して結晶
性の酸化アルミニウムの生成時に発生する皮膜内部及び
厚さ方向の空孔欠陥を露出させ、再度陽極酸化処理を施
して露出した空孔欠陥の修復を行なって空孔欠陥の少な
い誘電体皮膜を形成している。
2. Description of the Related Art Conventionally, the anode aluminum foil of an aluminum electrolytic capacitor has been subjected to a hydration treatment on a high-purity aluminum foil having been subjected to a surface enlargement treatment and then anodized to produce crystalline aluminum oxide on the surface. This is used as a dielectric film. By the way, in the above, when forming crystalline aluminum oxide by anodic oxidation, vacancy defects inevitably occur. This vacancy defect is
The aluminum hydroxide generated by the hydration treatment is generated by volume shrinkage that occurs when dehydration occurs, and oxygen gas is sealed inside. If these vacancies are present in the dielectric film, the porosity defects are exposed and deteriorate the film when used as an electrolytic capacitor, so heat treatment, chemical treatment, and mechanical treatment are usually performed after anodizing. To expose vacancies in the film and in the thickness direction generated during the formation of crystalline aluminum oxide, and then perform anodic oxidation treatment to repair the exposed vacancies, thereby reducing the vacancies in the dielectric. A film is formed.

【0003】[0003]

【発明が解決しようとする課題】しかし、熱処理後の減
極処理において、1回の熱処理と再陽極酸化処理によ
り、空孔欠陥を充分に露出・修復することは困難であ
り、そのため一般的にはこれらの処理を複数回繰り返し
行なっている。しかしながら、上記した処理を何度繰り
返し行なっても、すべての空孔欠陥を露出・修復させる
ことは困難であると共に、製造設備の面や生産効率の面
などからも自から制約を受け、空孔欠陥を露出・修復す
る方策として必ずしも有効な手段ではなかった。そこで
本発明は、上記した空孔欠陥を軽度の減極処理により効
率的に露出・修復させて耐久性に優れた特に中高圧陽極
用に有効な電極箔の化成方法を提供することを目的とし
たものである。
However, in the depolarization treatment after the heat treatment, it is difficult to sufficiently expose and repair the vacancy defects by one heat treatment and re-anodization treatment. Repeats these processes a plurality of times. However, it is difficult to expose and repair all vacancy defects even if the above process is repeated many times, and the vacancy is restricted by the production equipment and production efficiency. It was not always an effective means for exposing and repairing defects. Therefore, an object of the present invention is to provide a method for forming an electrode foil, which is effective for a medium-to-high-pressure anode, and is particularly durable by efficiently exposing and repairing the above-described vacancy defects by mild depolarization. It was done.

【0004】[0004]

【課題を解決するための手段】本発明は、上記した目的
を達成するために、拡面処理を施した高純度のアルミニ
ウム箔を、純水中に浸漬して水和処理を行なう第一工程
と、直鎖ジカルボン酸を含む水溶液中で浸漬処理する第
二工程と、純水中に浸漬して水和処理を行なう第三工程
と、陽極酸化処理後に熱処理を含む減極処理工程とから
成ることを特徴としたものであり、好ましくは第一工程
及び第三工程における水和処理温度をそれぞれ摂氏70
度以上とするものである。
SUMMARY OF THE INVENTION In order to achieve the above-mentioned object, the present invention provides a first step of immersing a high-purity aluminum foil subjected to a surface enlargement treatment in pure water to perform a hydration treatment. And a second step of immersion in an aqueous solution containing a linear dicarboxylic acid, a third step of immersion in pure water to perform hydration, and a depolarization step including heat treatment after anodization. Preferably, the hydration temperature in the first step and the third step is 70 degrees Celsius, respectively.
Degrees or more.

【0005】[0005]

【作用】しかして、上記において、陽極酸化処理により
結晶性の酸化アルミニウムを形成させる際に発生した空
孔欠陥は、熱処理を含む減極処理工程において、空孔欠
陥内に封じ込められた酸素ガスが加熱されることにより
体積膨脹して、空孔欠陥の表層にある酸化物層を破壊し
て空孔欠陥が露出する。上記における体積膨脹は、高温
度ほど著しくなり、空孔欠陥の露出効果は大きくなる
が、下地の金属アルミニウムの融点を超えて高温度にす
ることはできないからその温度には自から限界がある。
しかるに本発明によれば、化成処理工程における水和処
理工程を二回に分けて、その間に直鎖ジカルボン酸水溶
液中に浸漬する処理を挿入したので、前段の水和処理に
よって生成した水和皮膜の表面に直鎖ジカルボン酸が吸
着し、後段の水和処理によってこの吸着層の表側に新た
な水和皮膜が生成する。すなわち、水和皮膜の中間部に
直鎖ジカルボン酸を含む水和皮膜が生じ、この水和皮膜
に陽極酸化処理を行なうことにより、中間部に直鎖ジカ
ルボン酸を含む結晶性酸化物が生成される。
Thus, in the above, the vacancy defects generated when the crystalline aluminum oxide is formed by the anodic oxidation treatment are caused by the oxygen gas sealed in the vacancy defects in the depolarization treatment step including the heat treatment. The volume expansion due to the heating causes the oxide layer on the surface of the vacancy defect to be broken, thereby exposing the vacancy defect. The volume expansion in the above becomes remarkable as the temperature increases, and the effect of exposing the vacancy defects increases. However, since the temperature cannot be raised to a temperature higher than the melting point of the underlying metallic aluminum, the temperature has its own limit.
However, according to the present invention, the hydration treatment step in the chemical conversion treatment step is divided into two steps, and a treatment of immersion in a linear dicarboxylic acid aqueous solution is inserted between them, so that the hydration film formed by the preceding hydration treatment The linear dicarboxylic acid is adsorbed on the surface of the substrate, and a new hydration film is formed on the front side of the adsorbed layer by the hydration treatment in the later stage. That is, a hydrated film containing linear dicarboxylic acid is formed in the middle part of the hydrated film, and by performing anodizing treatment on the hydrated film, a crystalline oxide containing linear dicarboxylic acid is generated in the middle part. You.

【0006】次いでこの結晶性酸化物に熱処理を行なう
と、中間部に取り込まれた直鎖ジカルボン酸が熱分解し
て、主に二酸化炭素ガスを発生する。この熱分解は、直
鎖ジカルボン酸が結晶中に取り込まれている場合には起
こりにくく、空孔表面に存在する場合には起こり易く、
従って、熱処理により、空孔欠陥内の酸素ガスの膨脹と
同時に直鎖ジカルボン酸の分解反応による二酸化炭素ガ
スの発生により著しく効率的に空孔欠陥の露出を実現す
ることができる。
Next, when the crystalline oxide is subjected to a heat treatment, the linear dicarboxylic acid incorporated in the intermediate portion is thermally decomposed to generate mainly carbon dioxide gas. This thermal decomposition is unlikely to occur when the linear dicarboxylic acid is incorporated in the crystal, and tends to occur when the linear dicarboxylic acid is present on the pore surface.
Therefore, by the heat treatment, the expansion of the oxygen gas in the vacancy defect and the generation of carbon dioxide gas by the decomposition reaction of the linear dicarboxylic acid simultaneously with the expansion of the vacancy defect can be realized extremely efficiently.

【0007】特に本発明において、中間層に直鎖ジカル
ボン酸を含む酸化物を生成したのは、空孔欠陥の位置が
この部分に集中しているためであり、この部分において
熱分解と体積膨脹が発生しないとその効果が充分に発揮
できないこと、また、直鎖ジカルボン酸を含む水溶液に
浸漬処理することは、比較的低温で熱分解して二酸化炭
素となり、体積膨脹が著しい点と、陽極酸化工程で電気
化学的反応を妨害しない点から選択したものである。
Particularly, in the present invention, the oxide containing linear dicarboxylic acid was formed in the intermediate layer because the position of vacancy defects was concentrated in this portion, and thermal decomposition and volume expansion in this portion were performed. In addition, immersion treatment in an aqueous solution containing a linear dicarboxylic acid requires thermal decomposition at a relatively low temperature to form carbon dioxide, resulting in significant volume expansion and anodic oxidation. It is selected because it does not interfere with the electrochemical reaction in the process.

【0008】なお使用可能な直鎖ジカルボン酸として
は、シュウ酸、マロン酸、コハク酸、グルタル酸、アジ
ピン酸、フマル酸、マレイン酸、酒石酸が好ましく、こ
のほかに、ピメリン酸、シベリン酸等の直鎖飽和ジカル
ボン酸が使用でき、またシトラコン酸、アコニット酸、
リンゴ酸、クエン酸等の直鎖不飽和ジカルボン酸も使用
することができる。
Preferred linear dicarboxylic acids that can be used are oxalic acid, malonic acid, succinic acid, glutaric acid, adipic acid, fumaric acid, maleic acid, and tartaric acid. Linear saturated dicarboxylic acids can be used, and citraconic acid, aconitic acid,
Linear unsaturated dicarboxylic acids such as malic acid and citric acid can also be used.

【0009】また使用可能な高純度アルミニウム箔とし
ては、通常使用される99.99%以上のものが好まし
いが、中高圧電解コンデンサ用に拡面処理できるもので
あれば、99.9%以上のアルミニウム純度のものであ
っても、充分所期の目的を達成することが可能である。
[0009] The usable high-purity aluminum foil is preferably 99.99% or more, which is usually used. However, if it can be expanded for medium-to-high pressure electrolytic capacitors, it should be 99.9% or more. Even with aluminum purity, the intended purpose can be sufficiently achieved.

【0010】[0010]

【実施の態様】以下本発明の実施例を比較例との関係に
おいて詳述する。 (実施例1)拡面処理を施した99.99%以上の高純
度アルミニウム箔を95℃の純水中に5分間浸漬した
後、85℃、5%のシュウ酸水溶液中に5分間浸漬処理
を施し、再度95℃の純水中に5分間浸漬処理を施した
後、85℃の7wt%ホウ酸水溶液中で20mA/cm
2 の化成電圧400Vの陽極酸化を行い、400Vに上
昇した後、15分間定電圧保持を行い、漏洩電流を減少
させた後520℃、5分間の熱処理を大気雰囲気下で行
い、再度同条件で陽極酸化を施し、この時の電気量と耐
電圧特性とを測定した。次いでこの化成箔を、純水中で
2時間沸騰煮沸して促進劣化試験を行なった後、耐電圧
特性を測定して促進劣化試験前の値と比較した。
Embodiments of the present invention will be described in detail below in relation to comparative examples. (Example 1) A 99.99% or more high-purity aluminum foil subjected to a surface enlargement treatment was immersed in pure water at 95 ° C for 5 minutes, and then immersed in 85 ° C, 5% oxalic acid aqueous solution for 5 minutes. And immersion treatment again in pure water at 95 ° C. for 5 minutes, followed by 20 mA / cm 2 in a 7 wt% aqueous solution of boric acid at 85 ° C.
Perform anodic oxidation of the second formation voltage 400V, after rising to 400V, it performed 15 minutes constant voltage holding, 520 ° C. after reducing the leakage current, a heat treatment for 5 minutes in an air atmosphere, again under the same conditions Anodization was performed, and the quantity of electricity and withstand voltage characteristics at this time were measured. Next, the formed foil was boiled in pure water for 2 hours to perform an accelerated deterioration test, and then the withstand voltage characteristics were measured and compared with the values before the accelerated deterioration test.

【0011】(実施例2)拡面処理を施した高純度アル
ミニウム箔を、95℃の純水中に2分間浸漬した後、6
0℃、5%のコハク酸水溶液中に5分間浸漬処理を施
し、再度95℃の純水中に5分間浸漬処理を行なった
後、85℃の7wt%ホウ酸水溶液中で20mA/cm
2 の化成電圧400Vの陽極酸化を行い、400Vに上
昇した後、15分間定電圧保持を行い、漏洩電流を減少
させた後、520℃、5分間の熱処理を大気雰囲気下で
行い、再度同条件で陽極酸化を施し、この時の電気量と
耐電圧特性とを測定した。次いでこの化成箔を、純水中
で2時間沸騰煮沸して促進劣化試験を行なった後、耐電
圧特性を測定して促進劣化試験前の値と比較した。
(Example 2) A high-purity aluminum foil subjected to a surface enlargement treatment was immersed in pure water at 95 ° C for 2 minutes.
After immersion treatment in a 5% aqueous succinic acid solution at 0 ° C. for 5 minutes, immersion treatment in pure water at 95 ° C. for 5 minutes, and then 20 mA / cm in a 7 wt% boric acid aqueous solution at 85 ° C.
Anodizing at a formation voltage of 400 V in Step 2 and raising the voltage to 400 V, holding a constant voltage for 15 minutes, reducing the leakage current, performing a heat treatment at 520 ° C. for 5 minutes in an air atmosphere, and again under the same conditions Anodizing was performed, and the quantity of electricity and withstand voltage characteristics at this time were measured. Next, the formed foil was boiled in pure water for 2 hours to perform an accelerated deterioration test, and then the withstand voltage characteristics were measured and compared with the values before the accelerated deterioration test.

【0012】(比較例1)比較例1は、実施例1におけ
る水和処理を1回のみとして「85℃、5%のシュウ酸
水溶液中に5分間浸漬処理する工程」を省略した場合を
例示している。すなわち、拡面処理を施した高純度アル
ミニウム箔を、95℃の純水中に10分間浸漬した後、
85℃の7wt%ホウ酸水溶液中で20mA/cm2
化成電圧400Vの陽極酸化を行い、400Vに上昇し
た後、15分間定電圧保持を行い、漏洩電流を減少させ
た後、520℃、5分間の熱処理を大気雰囲気下で行い
再度同条件で陽極酸化を施し、この時の電気量と耐電圧
特性とを測定した。次いでこの化成箔を純水中で2時間
沸騰煮沸して促進劣化試験を行なった後、耐電圧特性を
測定して促進劣化試験前の値と比較した。
(Comparative Example 1) Comparative Example 1 is an example in which the hydration treatment in Example 1 is performed only once, and the “step of immersing in oxalic acid aqueous solution at 85 ° C. and 5% for 5 minutes” is omitted. are doing. That is, after immersing the high-purity aluminum foil subjected to the surface enlargement treatment in pure water at 95 ° C. for 10 minutes,
Anodizing is performed at a formation voltage of 400 mA at 20 mA / cm 2 in a 7 wt% aqueous solution of boric acid at 85 ° C., and after raising the voltage to 400 V, a constant voltage is maintained for 15 minutes to reduce the leakage current. A minute heat treatment was performed in an air atmosphere, anodization was performed again under the same conditions, and the quantity of electricity and withstand voltage characteristics at this time were measured. Next, the formed foil was boiled in pure water for 2 hours to perform an accelerated deterioration test, and then the withstand voltage characteristics were measured and compared with the values before the accelerated deterioration test.

【0013】(比較例2)比較例2は、実施例1におけ
る後段の水和処理を省略した場合を例示している。すな
わち、拡面処理を施した高純度アルミニウム箔を95℃
の純水中に10分間浸漬した後、85℃、5%のシュウ
酸水溶液中に5分間浸漬処理を施し、85℃の7wt%
ホウ酸水溶液中で20mA/cm2 の化成電圧400V
の陽極酸化を行い、400Vに上昇した後、15分間定
電圧保持を行い、漏洩電流を減少させた後、520℃、
5分間の熱処理を大気雰囲気下で行い、再度同条件で陽
極酸化を施し、この時の電気量と耐電圧特性とを測定し
た。次いでこの化成箔を、純水中で2時間沸騰煮沸して
促進劣化試験を行なった後、耐電圧特性を測定して促進
劣化前の値と比較した。
Comparative Example 2 Comparative Example 2 exemplifies a case in which the subsequent hydration treatment in Example 1 is omitted. That is, the high-purity aluminum foil subjected to the surface enlargement process
Immersed in pure water at 85 ° C for 5 minutes, and then immersed in 5% oxalic acid aqueous solution at 85 ° C for 7 minutes.
Formation voltage of 20 mA / cm 2 in boric acid solution at 400 V
Anodic oxidation, after raising to 400V, holding a constant voltage for 15 minutes, reducing the leakage current, 520 ℃
A heat treatment for 5 minutes was performed in an air atmosphere, anodization was performed again under the same conditions, and the quantity of electricity and withstand voltage characteristics at this time were measured. Next, the formed foil was boiled and boiled in pure water for 2 hours to perform an accelerated deterioration test, and then the withstand voltage characteristics were measured and compared with the values before the accelerated deterioration.

【0014】(比較例3)比較例3は、実施例2におけ
る「60℃、5%のコハク酸水溶液中に5分間浸漬処
理」する工程を、「85℃、8%のホウ酸水溶液中に5
分間浸漬処理」する工程に代えた場合を例示している。
すなわち、拡面処理を施した高純度アルミニウム箔を、
95℃の純水中に2分間浸漬した後、85℃、8%のホ
ウ酸水溶液中に5分間浸漬処理を施し、再度95℃の純
水中に5分間浸漬処理を行なった後、85℃の7wt%
ホウ酸水溶液中で20mA/cm2 の化成電圧400V
の陽極酸化を行い、400Vに上昇した後、15分間定
電圧保持を行い、漏洩電流を減少させた後、520℃、
5分間の熱処理を大気雰囲気下で行い、再度同条件で陽
極酸化を施し、この時の電気量と耐電圧特性とを測定し
た。次いでこの化成箔を、純水中で2時間沸騰煮沸して
促進劣化試験を行なった後、耐電圧特性を測定して促進
劣化試験前の値と比較した。
(Comparative Example 3) In Comparative Example 3, the step of “immersing in a 5% aqueous succinic acid solution at 60 ° C. for 5 minutes” in Example 2 was carried out in the same manner as in “2. 5
For example, a case in which the step of “immersion for a minute” is replaced is shown.
In other words, a high-purity aluminum foil that has been
After immersion in pure water at 95 ° C. for 2 minutes, immersion treatment in 85% aqueous 8% boric acid for 5 minutes, immersion in pure water at 95 ° C. for 5 minutes again, 7wt% of
Formation voltage of 20 mA / cm 2 in boric acid solution at 400 V
Anodic oxidation, after raising to 400V, holding a constant voltage for 15 minutes, reducing the leakage current, 520 ℃
A heat treatment for 5 minutes was performed in an air atmosphere, anodization was performed again under the same conditions, and the quantity of electricity and withstand voltage characteristics at this time were measured. Next, the formed foil was boiled in pure water for 2 hours to perform an accelerated deterioration test, and then the withstand voltage characteristics were measured and compared with the values before the accelerated deterioration test.

【0015】その結果を表1で示す。The results are shown in Table 1.

【表1】 [Table 1]

【0016】以上の結果から明らかなように、いずれの
実施例においても、再陽極酸化を施した時の電気量は、
比較例1乃至3のいずれと比較しても極めて大きく、こ
のことから熱処理による空孔欠陥の露出効果が顕著であ
ることが理解できる。また純水中での2時間の沸騰煮沸
による促進劣化試験後においても、耐電圧特性の低下は
全く見られなかった。また直鎖ジカルボン酸であるシュ
ウ酸水溶液で浸漬処理を行なっても、後段の水和処理を
行なわない比較例2の場合にはその効果は小さく、さら
にまた熱分解しないホウ酸水溶液処理を、前後に区分し
た水和処理の中間に挿入した比較例3の場合も全く効果
が得られなかった。
As is evident from the above results, in each of the examples, the amount of electricity when re-anodizing is performed is as follows:
Compared to any of Comparative Examples 1 to 3, it is extremely large, and it can be understood from this that the effect of exposing vacancy defects by the heat treatment is remarkable. Further, even after the accelerated deterioration test by boiling for 2 hours in pure water, no decrease in withstand voltage characteristics was observed at all. Further, even when immersion treatment is performed with an aqueous solution of oxalic acid, which is a linear dicarboxylic acid, the effect is small in the case of Comparative Example 2 in which the subsequent hydration treatment is not performed. No effect was obtained even in the case of Comparative Example 3 inserted in the middle of the hydration treatment classified into.

【0017】なお上記した実施例1及び2における処理
温度、処理時間及び液濃度は、当該使用した直鎖ジカル
ボン酸においてそれぞれ最も好ましい条件であり、これ
らの条件は、直鎖ジカルボン酸の種類によって異なる。
また水和処理の温度として、第一工程及び第三工程にお
いて70℃以下で行なった場合には、水和物の生成に時
間を要し、作業性を欠く。従って水和処理の温度として
第一工程においても、また第三工程にいても少なくとも
70℃以上が好ましい。また陽極酸化処理における電流
密度と化成電圧及び空孔欠陥を露出処理するための52
0℃、5分間の熱処理条件は、いずれも従来から実施さ
れている公知の条件を適用したものである。
The treatment temperature, treatment time and solution concentration in Examples 1 and 2 are the most preferable conditions for the used linear dicarboxylic acid, and these conditions differ depending on the type of the linear dicarboxylic acid. .
When the hydration treatment is performed at 70 ° C. or less in the first step and the third step, it takes a long time to produce a hydrate and lacks workability. Therefore, the temperature of the hydration treatment is preferably at least 70 ° C. in both the first step and the third step. In addition, the current density and the formation voltage in the anodic oxidation treatment and 52 for exposing the vacancy defect.
As the heat treatment conditions at 0 ° C. for 5 minutes, well-known conditions conventionally applied are applied.

【0018】[0018]

【発明の効果】以上のように、本発明によれば前後の水
和処理工程の中間に、直鎖ジカルボン酸水溶液による浸
漬処理工程を挿入したので、熱処理による減極工程にお
いて、空孔欠陥の露出を著しく促進し、かつその空孔欠
陥の露出は、再陽極酸化処理によって修復されて、残存
する空孔欠陥を著しく低減することができて耐久性に優
れ、かつ、再陽極酸化時の電気量も著しく向上する中高
圧用のアルミニウム電極箔を提供することができる。
As described above, according to the present invention, the immersion treatment step with the aqueous solution of linear dicarboxylic acid is inserted between the hydration treatment steps before and after, so that the porosity defect is eliminated in the depolarization step by heat treatment. Exposure is remarkably accelerated, and the exposure of the vacancy defects is repaired by the re-anodizing treatment, so that the remaining vacancy defects can be significantly reduced, and the durability is excellent. It is possible to provide an aluminum electrode foil for medium and high pressures whose amount is significantly improved.

フロントページの続き (72)発明者 梶山 隆 静岡県庵原郡蒲原町蒲原1丁目34番1号 日本軽金属株式会社グループ技術セン ター内 (56)参考文献 特開 平6−275473(JP,A) 特開 平5−335186(JP,A) 特開 昭60−65517(JP,A) 特開 平8−64480(JP,A) 特開 昭62−186514(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01G 9/04 301 Continuation of the front page (72) Inventor Takashi Kajiyama 1-34-1 Kambara, Kambara-cho, Anbara-gun, Shizuoka Prefecture Inside the Nippon Light Metal Co., Ltd. Group Technology Center (56) References JP-A-6-275473 (JP, A) JP-A-5-335186 (JP, A) JP-A-60-65517 (JP, A) JP-A-8-64480 (JP, A) JP-A-62-186514 (JP, A) (58) Int.Cl. 7 , DB name) H01G 9/04 301

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 拡面処理を施した高純度のアルミニウム
箔を、純水中に浸漬して水和処理を行なう第一工程と、
直鎖ジカルボン酸を含む水溶液中で浸漬処理する第二工
程と、純水中に浸漬して水和処理を行なう第三工程と、
陽極酸化処理後に熱処理を含む減極処理工程とから成る
ことを特徴とした中高圧アルミニウム電解コンデンサ用
電極箔の化成方法。
A first step of immersing a high-purity aluminum foil having been subjected to a surface enlargement treatment in pure water to perform a hydration treatment;
A second step of immersion treatment in an aqueous solution containing a linear dicarboxylic acid, and a third step of immersion in pure water to perform hydration treatment,
A method for forming an electrode foil for a medium-to-high pressure aluminum electrolytic capacitor, comprising a depolarization step including a heat treatment after anodizing treatment.
【請求項2】 第一工程及び第三工程における水和処理
温度をそれぞれ摂氏70度以上とした請求項1記載の中
高圧アルミニウム電解コンデンサ用電極箔の化成方法。
2. The method according to claim 1, wherein the hydration temperature in the first step and the third step is 70 ° C. or higher, respectively.
JP10207096A 1996-04-02 1996-04-02 Method of forming electrode foil for medium and high pressure aluminum electrolytic capacitors Expired - Fee Related JP3309176B2 (en)

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JP3309176B2 true JP3309176B2 (en) 2002-07-29

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* Cited by examiner, † Cited by third party
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JP2005347681A (en) * 2004-06-07 2005-12-15 Nichicon Corp Method of manufacturing anode foil for aluminum electrolytic capacitor
JP4572649B2 (en) * 2004-10-12 2010-11-04 パナソニック株式会社 Method for producing electrode foil for electrolytic capacitor
JP2007036048A (en) * 2005-07-28 2007-02-08 Nichicon Corp Manufacturing method of electrode foil for aluminum electrolytic capacitor
JP5490446B2 (en) 2009-06-18 2014-05-14 パナソニック株式会社 Method for producing anode foil for aluminum electrolytic capacitor
US8345409B2 (en) * 2010-03-31 2013-01-01 Nippon Chemi-Con Corporation Solid electrolytic capacitor
JP6650298B2 (en) * 2015-06-29 2020-02-19 日本軽金属株式会社 Method for manufacturing electrode for aluminum electrolytic capacitor
JP6990974B2 (en) 2017-02-09 2022-01-12 日本軽金属株式会社 Manufacturing method of electrodes for aluminum electrolytic capacitors
JP6675996B2 (en) 2017-02-09 2020-04-08 日本軽金属株式会社 Method for manufacturing electrode for aluminum electrolytic capacitor
JP6933931B2 (en) * 2017-07-28 2021-09-08 日本軽金属株式会社 Electrodes for Aluminum Electrolytic Capacitors and Their Manufacturing Methods
KR102625388B1 (en) * 2019-03-01 2024-01-17 이너 몽골리아 우란차부 동양광 폼드 포일 컴퍼니 리미티드 Electrode structure and method of manufacturing the same

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