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JP2910080B2 - Manufacturing method of electrode foil for aluminum electrolytic capacitor - Google Patents
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JP2910080B2 - Manufacturing method of electrode foil for aluminum electrolytic capacitor - Google Patents

Manufacturing method of electrode foil for aluminum electrolytic capacitor

Info

Publication number
JP2910080B2
JP2910080B2 JP1216443A JP21644389A JP2910080B2 JP 2910080 B2 JP2910080 B2 JP 2910080B2 JP 1216443 A JP1216443 A JP 1216443A JP 21644389 A JP21644389 A JP 21644389A JP 2910080 B2 JP2910080 B2 JP 2910080B2
Authority
JP
Japan
Prior art keywords
power supply
formation
tank
foil
chemical conversion
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
JP1216443A
Other languages
Japanese (ja)
Other versions
JPH0379020A (en
Inventor
二三男 工藤
信義 神崎
涼一 島谷
悟 北村
弘 椚原
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 JP1216443A priority Critical patent/JP2910080B2/en
Publication of JPH0379020A publication Critical patent/JPH0379020A/en
Application granted granted Critical
Publication of JP2910080B2 publication Critical patent/JP2910080B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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 本発明はアルミ電解コンデンサ用電極箔の生産能力を
化成電流の供給量の増大により向上するためのアルミ電
解コンデンサ用電極箔の製造方法に関するものである。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing an electrode foil for an aluminum electrolytic capacitor for improving the production capacity of the electrode foil for an aluminum electrolytic capacitor by increasing the supply amount of a formation current. .

従来の技術 近年、電解コンデンサに対する市場の要求は、高信頼
性や軽薄短小化に加えて、低コスト化が望まれている。
2. Description of the Related Art In recent years, market demands for electrolytic capacitors have demanded cost reduction in addition to high reliability, lightness, and size reduction.

低コスト化については、電解コンデンサの主要材料で
ある電極箔の安価な提供が強く望まれている。
For cost reduction, it is strongly desired to provide an inexpensive electrode foil, which is a main material of an electrolytic capacitor.

以下に従来のアルミ電解コンデンサ用電極箔の製造方
法について説明する。
Hereinafter, a method for manufacturing a conventional electrode foil for an aluminum electrolytic capacitor will be described.

第3図は従来のアルミ電解コンデンサ用電極箔の製造
方法を説明するための製造装置の概念図である。第3図
において、1と4は化成槽、5は給電ローラ、6,7は直
流電源、8は化成箔、9はアルミニウム箔である。
FIG. 3 is a conceptual diagram of a manufacturing apparatus for explaining a conventional method of manufacturing an electrode foil for an aluminum electrolytic capacitor. In FIG. 3, reference numerals 1 and 4 denote a chemical tank, 5 denotes a feeding roller, 6 and 7 denote a DC power source, 8 denotes a conversion foil, and 9 denotes an aluminum foil.

化成槽1,4は、直流電源6,7の陰極に接続された複数の
化成電極と化成液を有する。給電ローラ5は、直流電源
6,7の陽極が接続され連続的に給電できるように回転す
る構造になっている。
The formation tanks 1, 4 have a plurality of formation electrodes connected to the cathodes of the DC power supplies 6, 7, and a formation solution. The power supply roller 5 is a DC power supply.
6, 7 anodes are connected and rotate so that power can be supplied continuously.

以上のように構成されたアルミ電解コンデンサ用電極
箔の製造装置について、以下その動作について説明す
る。
The operation of the apparatus for manufacturing an electrode foil for an aluminum electrolytic capacitor configured as described above will be described below.

まずアルミニウム箔9に給電ローラ5より化成電流が
供給され、化成槽1で直流電源6の電圧に応じた化成皮
膜が形成される。次に、化成槽4で直流電源7の電圧に
応じた化成皮膜が給電ローラ5より供給される化成電流
によって形成される。この時、直流電源6の電圧より
も、直流電源7の電圧を高くして行うようにしていた。
First, a formation current is supplied to the aluminum foil 9 from the power supply roller 5, and a formation film corresponding to the voltage of the DC power supply 6 is formed in the formation tank 1. Next, in the chemical conversion tank 4, a chemical conversion film corresponding to the voltage of the DC power supply 7 is formed by a chemical conversion current supplied from the power supply roller 5. At this time, the voltage of the DC power supply 7 is set to be higher than the voltage of the DC power supply 6.

発明が解決しようとする課題 しかしながら上記の従来の方法では、化成電流の供給
がアルミニウム箔9の段階で1ヶ所しか設けることがで
きないため、化成皮膜の生産性を向上するために化成電
流の増大を行うと、給電ローラ5とアルミニウム箔9の
間で火花放電を起こし、アルミニウム箔9が溶断して生
産できないという問題があった。
However, in the above-mentioned conventional method, the supply of the formation current can be provided at only one place at the stage of the aluminum foil 9, so that the formation current is increased in order to improve the productivity of the formation film. If this is done, a spark discharge occurs between the power supply roller 5 and the aluminum foil 9, and the aluminum foil 9 is melted and cannot be produced.

本発明は上記従来の問題点を解決するもので、生産性
の向上による低コスト化を図ることが可能なアルミ電解
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
したものである。
An object of the present invention is to solve the above-mentioned conventional problems, and an object of the present invention is to provide a method of manufacturing an electrode foil for an aluminum electrolytic capacitor, which can reduce the cost by improving the productivity.

課題を解決するための手段 この課題を解決するために本発明のアルミ電解コンデ
ンサ用電極箔の製造方法は、従来のアルミニウム箔に給
電する給電ローラに加え、化成皮膜が形成された化成箔
に、液体を用いて間接的に給電を行うようにしたもの
で、第1の直流電源の陽極に接続した給電ローラと、前
記第1の直流電源の陰極に接続した複数の化成電極と化
成液を有した第1の化成槽と、ホウ酸アンモニウム又は
ホウ酸ナトリウム又はリン酸を成分とする水溶液中でし
ゃ沸処理を行う水和処理槽及び/又は化成箔を折り曲げ
るためのφ30以下のローラと、第2の直流電源の陽極に
接続した複数の給電電極と給電液を有した給電槽と、前
記第2の直流電源の陰極に接続した複数の化成電極と化
成液を有した第2の化成槽とを設け、前記第1の直流電
源の電圧より第2の直流電源の電圧を高く設定して給電
ローラ及び給電槽から化成電流を供給し、この状態でア
ルミニウム箔を連続走行させて化成を行う製造方法とし
たものである。
Means for Solving the Problems In order to solve this problem, the method for manufacturing an electrode foil for an aluminum electrolytic capacitor of the present invention includes, in addition to a conventional power supply roller for supplying power to an aluminum foil, a chemical conversion film formed with a chemical conversion film, The power supply is indirectly performed by using a liquid, and includes a power supply roller connected to an anode of a first DC power supply, a plurality of formation electrodes connected to a cathode of the first DC power supply, and a formation liquid. A first chemical conversion tank, a hydration treatment tank for performing a boiling treatment in an aqueous solution containing ammonium borate, sodium borate, or phosphoric acid as a component and / or a roller of φ30 or less for bending a chemical conversion foil; A power supply tank having a plurality of power supply electrodes connected to the anode of the second DC power supply and a power supply liquid; and a second chemical formation tank having a plurality of formation electrodes connected to the cathode of the second DC power supply and the formation liquid. And the first straight line is provided. Than the power supply voltage of the second DC power supply voltage is set high to the supply anodizing current from the feeding roller and the feed tank, in which a manufacturing method of performing chemical conversion by an aluminum foil is continuously running in this state.

作用 この製造方法により、化成電流を複数のところより供
給することが可能となり、このために化成箔全体に電流
が分散され、局部的に電流集中するということがなくな
って部分的な発熱によるアルミニウムの水素ぜい性を防
止することができるものである。
Function This production method makes it possible to supply the formation current from a plurality of places, so that the current is dispersed throughout the formation foil, the current is not locally concentrated, and the aluminum is partially heated due to heat generation. It can prevent hydrogen embrittlement.

さらに、給電液を介して給電槽で間接的に化成箔に給
電する場合、その前工程で化成箔をホウ酸アンモニウム
又はホウ酸ナトリウム又はリン酸を成分とする水溶液中
でしゃ沸処理することにより化成皮膜が水和され、化成
皮膜中に電気を運ぶイオンが注入されるために化成皮膜
の電気抵抗を小さくすることができる。
Further, in the case of indirectly supplying power to the chemical conversion foil in the power supply tank via the power supply solution, the chemical conversion foil is subjected to boiling treatment in an aqueous solution containing ammonium borate, sodium borate, or phosphoric acid as a component in the preceding step. Since the chemical conversion film is hydrated and ions that carry electricity are implanted into the chemical conversion film, the electrical resistance of the chemical conversion film can be reduced.

また同じく、前工程で化成箔に折り曲げ負荷を加える
ことにより化成皮膜にクラックが生じ、このクラックを
通して給電用電解液が内部の金属(アルミ)と直接接触
するために化成皮膜の電気抵抗を小さくすることができ
る。これらの作用により給電槽の浴電圧を低下させ、給
電時の電力損失が極めて小さくなるために化成電流の供
給量を大幅に増大させることが可能となり、生産速度の
向上によるコストダウンが実現できる。
Similarly, a crack is generated in the chemical conversion film by applying a bending load to the chemical conversion foil in the previous process, and the electrolytic solution for power supply comes into direct contact with the internal metal (aluminum) through the crack, thereby reducing the electrical resistance of the chemical conversion film. be able to. By these effects, the bath voltage of the power supply tank is reduced, and the power loss at the time of power supply is extremely small, so that the supply amount of the formation current can be greatly increased, and the cost can be reduced by improving the production speed.

実施例 以下、本発明の一実施例について、図面を参照しなが
ら説明する。第1図は本発明の第1の実施例における、
アルミ電解コンデンサ用電極箔の製造方法を説明するた
めの製造装置の概念図である。
Embodiment Hereinafter, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a first embodiment of the present invention.
It is a conceptual diagram of the manufacturing apparatus for demonstrating the manufacturing method of the electrode foil for aluminum electrolytic capacitors.

第1図において、1,4は化成槽で、2は水和処理槽で
ある。3は給電槽で、5は給電ローラである。6,7は直
流電源で、8は化成箔で、9はアルミニウム箔である。
In FIG. 1, reference numerals 1 and 4 denote a chemical conversion tank and 2 denotes a hydration treatment tank. Reference numeral 3 denotes a power supply tank, and reference numeral 5 denotes a power supply roller. Reference numerals 6 and 7 denote DC power supplies, 8 denotes a conversion foil, and 9 denotes an aluminum foil.

化成槽1,4は、直流電源の陰極と接続された複数の化
成電極と化成液を有する。水和処理槽2は、ホウ酸アン
モニウム、又はホウ酸ナトリウム、又はリン酸を成分と
する高温の水溶液を有する。給電槽3は、直流電源の陽
極が接続された複数の給電電極と給電液を有し、給電ロ
ーラ5には直流電源の陽極が接続されている。
The formation tanks 1 and 4 have a plurality of formation electrodes connected to a cathode of a DC power supply and a formation solution. The hydration treatment tank 2 has a high-temperature aqueous solution containing ammonium borate, sodium borate, or phosphoric acid as a component. The power supply tank 3 has a plurality of power supply electrodes to which an anode of a DC power supply is connected and a power supply liquid. The power supply roller 5 is connected to an anode of a DC power supply.

以上のように構成されたアルミ電解コンデンサ用電極
箔の製造装置について、以下その動作を説明する。
The operation of the apparatus for manufacturing an electrode foil for an aluminum electrolytic capacitor configured as described above will be described below.

まず、アルミニウム箔9に給電ローラ5より化成電流
が供給され、化成槽1で直流電源6の電圧に応じた化成
皮膜が形成される。次に、水和処理槽2で化成皮膜がし
ゃ沸され、化成皮膜中に電気を運ぶイオンが注入され
る。次に、給電槽3でイオン電流により給電電極から化
成箔8に電流が供給される。次に、化成槽4で直流電源
7の電圧に応じた化成皮膜が形成される。この時、直流
電源6の電圧よりも、直流電源7の電圧を高く設定して
行う。次に、本実施例の条件について説明する。
First, a formation current is supplied to the aluminum foil 9 from the power supply roller 5, and a formation film corresponding to the voltage of the DC power supply 6 is formed in the formation tank 1. Next, the chemical conversion film is boiled in the hydration treatment tank 2, and ions that carry electricity are injected into the chemical conversion film. Next, a current is supplied to the chemical conversion foil 8 from the power supply electrode by the ion current in the power supply tank 3. Next, a chemical conversion film corresponding to the voltage of the DC power supply 7 is formed in the chemical conversion tank 4. At this time, the voltage of the DC power supply 7 is set higher than the voltage of the DC power supply 6. Next, conditions of the present embodiment will be described.

(1) 給電槽3の条件 給電液組成:アジピン酸アンモニウム50g/ 電 気 量:1A/10cm2×4分 給電液温度:30℃ (2) 直流電源6の電圧:300V (3) 直流電源7の電圧:450V (4) 水和処理槽2の条件 ホウ酸アンモニウム…0.01g/、0.1g/、1.0g/ 処理液組成:ホウ酸ナトリウム…0.01g/、0.1g/
、1.0g/ リン酸…0.1g/、1g/、10g/ 処理液温度:95℃ 処理時間 :3分 上記の内容で実施した時の給電槽3の浴電圧と化成箔
8の耐折強度を表−1に示す。
(1) Power supply tank 3 conditions Power supply composition: Ammonium adipate 50g / Electricity: 1A / 10cm 2 × 4 minutes Power supply liquid temperature: 30 ° C (2) Voltage of DC power supply 6: 300V (3) DC power supply 7 (4) Conditions for hydration treatment tank 2 Ammonium borate: 0.01 g /, 0.1 g /, 1.0 g / Treatment liquid composition: sodium borate: 0.01 g /, 0.1 g /
, 1.0 g / phosphoric acid ... 0.1 g /, 1 g /, 10 g / Treatment temperature: 95 ° C Treatment time: 3 minutes The bath voltage of the power supply tank 3 and the bending strength of the conversion foil 8 when the above contents were carried out. It is shown in Table 1.

以上のように、本実施例によれば、化成皮膜が形成さ
れた後、ホウ酸アンモニウム0.01g/〜1g/水溶液、
又はホウ酸ナトリウム0.01g/〜1g/水溶液、又はリ
ン酸1g/〜10g/水溶液中でしゃ沸処理する水和処理
槽を設けることによって、給電槽3の浴電圧が水和処理
しない場合の約1/6に低減された。このことは、液体を
用いて給電する時の電力損失が、水和処理することによ
って約1/6に低減することを示している。また、水和処
理によって化成箔8の強度低下を防ぐことができる。
As described above, according to this example, after the formation of the chemical conversion film, ammonium borate 0.01 g / ~ 1 g / aqueous solution,
Alternatively, by providing a hydration treatment tank that performs boiling treatment in 0.01 g / -1 g / aqueous solution of sodium borate or 1 g / -10 g / aqueous solution of phosphoric acid, the bath voltage of the power supply tank 3 is reduced when the hydration treatment is not performed. Reduced to 1/6. This indicates that the power loss when supplying power using liquid is reduced to about 1/6 by the hydration treatment. Further, the hydration treatment can prevent the strength of the chemical conversion foil 8 from decreasing.

以下、本発明の第2の実施例について図面を参照しな
がら説明する。
Hereinafter, a second embodiment of the present invention will be described with reference to the drawings.

第2図(a),(b)は本発明の第2の実施例を示す
アルミ電解コンデンサ用電極箔と製造装置の概念図であ
る。同図において、10は化成箔8の折り曲げローラで、
第2図(b)に示すように複数本のローラ10aをリング
状に配置することにより構成されている。本実施例にお
いて、第1図に示す第1の実施例と異なるのは、折り曲
げローラ10を水和処理槽2の代りに設けた点である。
FIGS. 2 (a) and 2 (b) are conceptual diagrams of an aluminum electrolytic capacitor electrode foil and a manufacturing apparatus according to a second embodiment of the present invention. In the figure, reference numeral 10 denotes a folding roller for forming foil 8;
As shown in FIG. 2 (b), it is constituted by arranging a plurality of rollers 10a in a ring shape. This embodiment differs from the first embodiment shown in FIG. 1 in that a folding roller 10 is provided instead of the hydration treatment tank 2.

上記のように構成されたアルミ電解コンデンサ用電極
箔の製造装置について、以下その動作を説明する。
The operation of the apparatus for manufacturing an electrode foil for an aluminum electrolytic capacitor configured as described above will be described below.

まず、アルミニウム箔9に給電ローラ5より化成電流
が供給され、化成槽1で直流電源6の電圧に応じた化成
皮膜が形成される。次に、折り曲げローラ10で化成箔8
が折り曲げられて、化成箔8の表面に形成された化成皮
膜にクラックが生ずる。次に、給電槽3で、イオン電流
により給電電極から化成箔8に電流が供給される。次
に、化成槽4で直流電源7の電圧に応じた化成皮膜が形
成される。この時、直流電源6の電圧よりも、直流電源
7の電圧を高く設定して行う。
First, a formation current is supplied to the aluminum foil 9 from the power supply roller 5, and a formation film corresponding to the voltage of the DC power supply 6 is formed in the formation tank 1. Next, the forming roller 8 is
Is bent, and cracks occur in the chemical conversion film formed on the surface of the chemical conversion foil 8. Next, in the power supply tank 3, a current is supplied from the power supply electrode to the chemical conversion foil 8 by an ionic current. Next, a chemical conversion film corresponding to the voltage of the DC power supply 7 is formed in the chemical conversion tank 4. At this time, the voltage of the DC power supply 7 is set higher than the voltage of the DC power supply 6.

次に、本実施例の条件について説明する。 Next, conditions of the present embodiment will be described.

折り曲げローラ10の径 ローラ径:φ10、φ20、φ30 給電槽3の条件と直流電源6,7の電圧は実施例1と同
じである。
Diameter of folding roller 10 Roller diameter: φ10, φ20, φ30 The conditions of the power supply tank 3 and the voltages of the DC power supplies 6 and 7 are the same as those in the first embodiment.

上記の内容で実施した時の給電槽3の浴電圧と化成箔
8の耐折強度を表−2に示す。
Table 2 shows the bath voltage of the power supply tank 3 and the bending strength of the chemical conversion foil 8 when the above operation was performed.

以上のように本実施例によれば、化成箔8を折り曲げ
るためのφ20以下のローラを設けることにより、給電槽
の浴電圧が約1/3に低下された。このことは、液体を用
いて給電する時の電力損失が、折り曲げローラを設ける
ことにより約1/3に低下できることになる。また、化成
箔8の強度についても低下を防ぐことができた。
As described above, according to the present embodiment, the bath voltage of the power supply tank was reduced to about 1/3 by providing a roller of φ20 or less for bending the chemical conversion foil 8. This means that the power loss when supplying power using the liquid can be reduced to about 1/3 by providing the folding roller. Also, the strength of the chemical conversion foil 8 was able to be prevented from lowering.

なお、第1の実施例の水和処理槽2と第2の実施例の
折り曲げローラ10を併用してもよいことは言うまでもな
い。また、限定されたスペースでアルミ電解コンデンサ
用電極箔の製造装置を設ける時、比較的化成皮膜の薄い
200V以下では、折り曲げローラ10を給電槽3の前に設
け、化成皮膜が厚くなる(300V以上)場合は、水和処理
槽2を給電槽3の前に設ける方法が有効である。
It goes without saying that the hydration tank 2 of the first embodiment and the bending roller 10 of the second embodiment may be used in combination. Also, when installing equipment for manufacturing electrode foil for aluminum electrolytic capacitors in a limited space, the conversion film is relatively thin.
At 200 V or less, it is effective to provide the bending roller 10 in front of the power supply tank 3 and to provide the hydration treatment tank 2 in front of the power supply tank 3 when the chemical conversion film becomes thick (300 V or more).

発明の効果 以上のように本発明は、第1の直流電源の陽極に接続
した給電ローラと、前記第1の直流電源の陰極に接続し
た複数の化成電極と化成液を有する化成槽と、ホウ酸ア
ンモニウム又はホウ酸ナトリウム又はリン酸を成分とす
る水溶液中でしゃ沸処理を行う水和処理槽及び/又は化
成箔を折り曲げるためのローラと、第2の直流電源の陽
極に接続した複数の給電電極と給電液を有する給電槽
と、前記第2の直流電源の陰極に接続した複数の化成電
極と化成液を有する化成槽とを設け、前記第1の直流電
源の電圧より第2の直流電源の電圧を高く設定して給電
ローラ及び給電槽から化成電流を供給し、この状態でア
ルミニウム箔を連続走行させて化成を行うようにするこ
とにより、生産速度の向上と、低コスト化を図ることが
できるものである。
Effect of the Invention As described above, the present invention provides a power supply roller connected to the anode of the first DC power supply, a plurality of formation electrodes connected to the cathode of the first DC power supply, and a formation tank having a formation liquid. A hydration tank for performing a boiling treatment in an aqueous solution containing ammonium acid, sodium borate, or phosphoric acid as a component and / or a roller for bending a chemical conversion foil, and a plurality of power supplies connected to an anode of a second DC power supply A power supply tank having an electrode and a power supply liquid; and a plurality of formation electrodes connected to the cathode of the second DC power supply and a formation tank having a formation liquid, wherein a second DC power supply is provided based on the voltage of the first DC power supply. To increase the production speed and reduce the cost by forming a high voltage to supply the formation current from the power supply roller and the power supply tank and continuously running the aluminum foil in this state to perform the formation. What can be It is.

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

第1図は本発明の第1の実施例におけるアルミ電解コン
デンサ用電極箔の製造方法を説明するための製造装置の
概念図、第2図(a),(b)は本発明の第2の実施例
におけるアルミ電解コンデンサ用電極箔の製造方法を説
明するための製造装置の概念図、第3図は従来のアルミ
電解コンデンサ用電極箔の製造方法を説明するための製
造装置の概念図である。 1,4……化成槽、2……水和処理槽、3……給電槽、5
……給電ローラ、6,7……直流電源、8……化成箔、9
……アルミニウム箔、10……折り曲げローラ。
FIG. 1 is a conceptual view of a manufacturing apparatus for explaining a method of manufacturing an electrode foil for an aluminum electrolytic capacitor in a first embodiment of the present invention, and FIGS. 2 (a) and (b) are second views of the present invention. FIG. 3 is a conceptual diagram of a manufacturing apparatus for explaining a method for manufacturing an electrode foil for an aluminum electrolytic capacitor in an embodiment, and FIG. 3 is a conceptual diagram of a manufacturing apparatus for explaining a conventional method for manufacturing an electrode foil for an aluminum electrolytic capacitor. . 1,4 ... Chemical tank, 2 ... Hydration tank, 3 ... Power supply tank, 5
…… Power supply roller, 6,7… DC power supply, 8… Formation foil, 9
…… Aluminum foil, 10 …… Bending roller.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 北村 悟 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 椚原 弘 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59−215716(JP,A) 特開 昭61−37977(JP,A) 特開 昭62−134919(JP,A) (58)調査した分野(Int.Cl.6,DB名) H01G 9/04 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Satoru Kitamura 1006 Kazuma Kadoma, Osaka Prefecture Inside Matsushita Electric Industrial Co., Ltd. In-company (56) References JP-A-59-215716 (JP, A) JP-A-61-37977 (JP, A) JP-A-62-134919 (JP, A) (58) Fields studied (Int. . 6 , DB name) H01G 9/04

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】第1の直流電源の陽極に接続した給電ロー
ラと、前記第1の直流電源の陰極に接続した複数の化成
電極と化成液を有した第1の化成槽と、ホウ酸アンモニ
ウム水溶液又はホウ酸ナトリウム水溶液又はリン酸水溶
液中でしゃ沸処理を行う水和処理槽及び/又は化成箔を
折り曲げるためのφ30以下のローラと、第2の直流電源
の陽極に接続した複数の給電電極と給電液を配した給電
槽と、前記第2の直流電源の陰極に接続した複数の化成
電極と化成液を有した第2の化成槽とを設け、前記第1
の直流電源の電圧より第2の直流電源の電圧を高く設定
して給電ローラ及び給電槽から化成電流を供給し、この
状態でアルミニウム箔を連続走行させて化成することを
特徴とするアルミ電解コンデンサ用電極箔の製造方法。
1. A power supply roller connected to an anode of a first DC power supply, a first chemical conversion tank having a plurality of formation electrodes and a formation liquid connected to a cathode of the first DC power supply, and ammonium borate. A hydration treatment tank for performing a boiling treatment in an aqueous solution, a sodium borate aqueous solution, or a phosphoric acid aqueous solution and / or a roller having a diameter of 30 or less for bending a conversion foil, and a plurality of power supply electrodes connected to an anode of a second DC power supply A power supply tank provided with a power supply solution and a plurality of formation electrodes connected to a cathode of the second DC power supply and a second formation tank having a formation solution;
An aluminum electrolytic capacitor characterized in that the voltage of the second DC power supply is set higher than the voltage of the DC power supply to supply a formation current from the power supply roller and the power supply tank, and the aluminum foil is continuously run in this state to form the aluminum electrolytic capacitor. Of manufacturing electrode foil for use.
JP1216443A 1989-08-22 1989-08-22 Manufacturing method of electrode foil for aluminum electrolytic capacitor Expired - Fee Related JP2910080B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1216443A JP2910080B2 (en) 1989-08-22 1989-08-22 Manufacturing method of electrode foil for aluminum electrolytic capacitor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1216443A JP2910080B2 (en) 1989-08-22 1989-08-22 Manufacturing method of electrode foil for aluminum electrolytic capacitor

Publications (2)

Publication Number Publication Date
JPH0379020A JPH0379020A (en) 1991-04-04
JP2910080B2 true JP2910080B2 (en) 1999-06-23

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP1216443A Expired - Fee Related JP2910080B2 (en) 1989-08-22 1989-08-22 Manufacturing method of electrode foil for aluminum electrolytic capacitor

Country Status (1)

Country Link
JP (1) JP2910080B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0715034U (en) * 1993-08-23 1995-03-14 浩之 大井 Sucker tool for health promotion
CN106245086B (en) * 2016-08-31 2019-03-01 四川石棉华瑞电子有限公司 Aluminium foil second level formation system and method

Also Published As

Publication number Publication date
JPH0379020A (en) 1991-04-04

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