JP2007299916A - Manufacturing method of electrode foil for electrolytic capacitor - Google Patents

Manufacturing method of electrode foil for electrolytic capacitor Download PDF

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JP2007299916A
JP2007299916A JP2006126369A JP2006126369A JP2007299916A JP 2007299916 A JP2007299916 A JP 2007299916A JP 2006126369 A JP2006126369 A JP 2006126369A JP 2006126369 A JP2006126369 A JP 2006126369A JP 2007299916 A JP2007299916 A JP 2007299916A
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electrode foil
phosphoric acid
foil
electrolytic capacitor
condensed
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Fumikazu Daimon
史和 大門
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Nichicon Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a manufacturing method of an electrode foil for an aluminum electrolytic capacitor which improves water resistance of the electrode foil. <P>SOLUTION: In the manufacturing method of the electrode foil for the electrolytic capacitor including an anodic oxidation process which forms an oxide film on an etched aluminum foil by anodic oxidation, the aluminum foil is immersed in phosphorus processing liquid including condensed phosphoric acid and/or condensed phosphate after or in the course of the anodic oxidation process, wherein in the phosphorus processing liquid, only the condensed phosphoric acid and/or the condensed phosphate may be blended, but moreover, orthophosphoric acid and/or orthophosphate may be blended. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は、電解コンデンサ用電極箔の製造方法に関するものであり、特に、低圧用電極箔に関するものである。   The present invention relates to a method for producing an electrode foil for electrolytic capacitors, and particularly relates to a low-pressure electrode foil.

アルミニウム電解コンデンサにおいて、駆動用電解液に水を配合して電解液の比抵抗を低減した場合、電極箔にはより耐水性が要求される。従って、従来は、化成処理を行う最終工程で、酸性溶液への浸漬を行い、陽極酸化皮膜の耐水性を高めている(例えば、非特許文献1参照)。
永田伊佐也著、「電解液陰極アルミニウム電解コンデンサ」、日本蓄電器工業株式会社、平成9年2月24日、P311〜319
In an aluminum electrolytic capacitor, when water is mixed in the driving electrolyte and the specific resistance of the electrolyte is reduced, the electrode foil is required to have more water resistance. Therefore, conventionally, in the final step of chemical conversion treatment, immersion in an acidic solution is performed to increase the water resistance of the anodized film (for example, see Non-Patent Document 1).
By Nagata Isaya, “Electrolyte Cathode Aluminum Electrolytic Capacitor”, Nippon Electric Storage Industrial Co., Ltd., February 24, 1997, P311-319

今日、電子機器の小形化、薄形化にともない、アルミニウム電解コンデンサの小形化の要求が高まっている。また、直列等価抵抗が低いコンデンサが求められている。そのため、電解液中に多量の水分を配合して電解液の比抵抗を低減させており、その分、電極箔にはより高い耐水性が要求されている。
しかしながら、更なる低等価直列抵抗化のためには、上記の従来の方法では、陽極酸化皮膜の耐水性が不十分であるという問題点がある。
Today, with the miniaturization and thinning of electronic devices, there is an increasing demand for miniaturization of aluminum electrolytic capacitors. Further, a capacitor having a low series equivalent resistance is required. Therefore, a large amount of water is blended in the electrolytic solution to reduce the specific resistance of the electrolytic solution, and accordingly, higher water resistance is required for the electrode foil.
However, in order to further reduce the equivalent series resistance, there is a problem that the water resistance of the anodized film is insufficient in the conventional method.

以上の問題点に鑑みて、本発明の課題は、電極箔の耐水性をより向上することのできる電解コンデンサ用電極箔の製造方法を提供することにある。   In view of the above problems, an object of the present invention is to provide a method for producing an electrode foil for an electrolytic capacitor that can further improve the water resistance of the electrode foil.

上記課題を解決するために、本発明では、エッチングされたアルミニウム箔に陽極酸化により酸化皮膜を形成する陽極酸化工程を有する電解コンデンサ用電極箔の製造方法において、前記陽極酸化工程の後、または当該陽極酸化工程の途中においてアルミニウム箔を縮合リン酸または/および縮合リン酸塩を含むリン処理液に浸漬することを特徴とする。   In order to solve the above-mentioned problems, in the present invention, in the method for producing an electrode foil for an electrolytic capacitor having an anodizing step of forming an oxide film by anodic oxidation on an etched aluminum foil, or after the anodizing step, In the middle of the anodizing step, the aluminum foil is immersed in a phosphorus treatment solution containing condensed phosphoric acid and / or condensed phosphate.

本発明において、縮合リン酸としては、ピロリン酸、トリポリリン酸、テトラポリリン酸、ヘキサメタリン酸等を挙げることができ、縮合リン酸塩としては、ピロリン酸ナトリウム(Na427)、酸性ピロリン酸ナトリウム(Na2227)、トリポリリン酸ナトリウム(Na5310)、テトラポリリン酸ナトリウム(Na6413)、ヘキサメタリン酸ナトリウム((NaPO3n)、酸性ヘキサメタリン酸ナトリウム({Naxy(PO3x+yn)等を挙げることができる。 In the present invention, examples of the condensed phosphoric acid include pyrophosphoric acid, tripolyphosphoric acid, tetrapolyphosphoric acid, hexametaphosphoric acid, and the like, and examples of the condensed phosphate include sodium pyrophosphate (Na 4 P 2 O 7 ), acidic pyrroline. Sodium phosphate (Na 2 H 2 P 2 O 7 ), sodium tripolyphosphate (Na 5 P 3 O 10 ), sodium tetrapolyphosphate (Na 6 P 4 O 13 ), sodium hexametaphosphate ((NaPO 3 ) n ), acidic sodium hexametaphosphate ({Na x H y (PO 3) x + y} n) , and the like.

本発明において、前記リン処理液には、前記縮合リン酸または前記縮合リン酸塩として、例えば、メタリン酸、メタリン酸ナトリウム塩、またはメタリン酸カリウム塩の少なくとも1種が配合されている構成を採用することができる。   In the present invention, the phosphoric treatment solution has a configuration in which at least one of, for example, metaphosphoric acid, sodium metaphosphate, or potassium metaphosphate is blended as the condensed phosphoric acid or the condensed phosphate. can do.

本発明において、前記リン処理液中における前記縮合リン酸または/および前記縮合リン酸塩の全配合量が、5.0〜50g/Lであることが好ましい。   In this invention, it is preferable that the total compounding quantity of the said condensed phosphoric acid or / and the said condensed phosphate in the said phosphorus treatment liquid is 5.0-50 g / L.

本発明において、前記リン処理液には、さらにオルトリン酸または/およびオルトリン酸塩が配合されていることが好ましい。この場合、前記リン処理液中における前記縮合リン酸または/および前記縮合リン酸塩の全配合量が20〜50g/Lであり、かつ、当該リン処理液における前記オルトリン酸または/および前記オルトリン酸塩の全配合量が1.5〜7.5g/Lであることが好ましい。   In the present invention, it is preferable that orthophosphoric acid and / or orthophosphate is further added to the phosphating solution. In this case, the total amount of the condensed phosphoric acid or / and the condensed phosphate in the phosphorus treatment solution is 20 to 50 g / L, and the orthophosphoric acid and / or the orthophosphoric acid in the phosphorus treatment solution It is preferable that the total amount of the salt is 1.5 to 7.5 g / L.

本発明では、陽極酸化工程の後、または陽極酸化工程の途中においてアルミニウム箔を縮合リン酸または/および縮合リン酸塩を含むリン処理液に浸漬するため、陽極酸化皮膜の表層部へのリン酸の吸着量が増える。このため、静電容量を低下させることなく、陽極酸化皮膜の耐水性を向上することができる。
また、リン酸処理液への浸漬により不要な皮膜を除去でき、静電容量の増加を図ることもできる。それ故、低圧小形品においても、静電容量が大きく、かつ、高温信頼性の高い電解コンデンサを提供することができる。
In the present invention, after the anodizing step or during the anodizing step, the aluminum foil is immersed in a phosphoric acid treatment solution containing condensed phosphoric acid or / and condensed phosphate, so that phosphoric acid is applied to the surface layer portion of the anodized film. The amount of adsorption increases. For this reason, the water resistance of the anodized film can be improved without reducing the capacitance.
Moreover, an unnecessary film | membrane can be removed by immersion in a phosphoric acid processing liquid, and an electrostatic capacity can also be aimed at. Therefore, it is possible to provide an electrolytic capacitor having a large electrostatic capacity and high temperature reliability even in a low-pressure small-sized product.

以下、本発明について実施例に基づき具体的に説明する。   Hereinafter, the present invention will be specifically described based on examples.

[実施例1〜7]
エッチングされたアルミニウム箔を、アジピン酸アンモニウム80g/L、アジピン酸1.5g/Lを溶解した化成液中で、85±2℃にて電圧印加し、22Vまで電圧を上昇させて化成し、デポラリゼーション、再化成処理等を施す(陽極酸化工程)。
[Examples 1-7]
The etched aluminum foil was formed by applying a voltage at 85 ± 2 ° C. in a chemical solution containing 80 g / L ammonium adipate and 1.5 g / L adipic acid, and increasing the voltage to 22 V. Apply laminarization, re-chemical conversion, etc. (anodic oxidation process).

次に、表1に示すように、ヘキサメタリン酸ナトリウム(メタリン酸ナトリウム)を各々の重量で配合した水溶液からなるリン処理液に25±1℃で1分間の浸漬を施し、化成箔(電解コンデンサ用電極箔)を得る。   Next, as shown in Table 1, immersion was performed at 25 ± 1 ° C. for 1 minute in a phosphorous treatment solution composed of an aqueous solution containing sodium hexametaphosphate (sodium metaphosphate) in respective weights, to form a chemical conversion foil (for electrolytic capacitors). Electrode foil) is obtained.

なお、比較例1、2、3として、リン酸(オルトリン酸)の水溶液(各々の重量は、1.5g/l、4.5g/l、7.5g/l)からなるリン処理液に上記と同じ条件で浸漬し、化成箔を得る。   In addition, as Comparative Examples 1, 2, and 3, a phosphoric acid treatment solution composed of an aqueous solution of phosphoric acid (orthophosphoric acid) (each weight is 1.5 g / l, 4.5 g / l, 7.5 g / l) is used. Immerse under the same conditions to obtain a chemical conversion foil.

次に、上記の実施例1〜7および比較例1〜3の化成箔の皮膜耐電圧(Vt)を測定した後、沸騰した純水に60分間浸漬した試料のV−T特性(化成液中で1.0mA/cm印加した際の電圧−時間特性)を計測し、Vt値に到達するまでの時間を計測する耐水性試験、および静電容量を測定した。その結果を表1に示す。 Next, after measuring the film withstand voltage (Vt) of the chemical conversion foils of Examples 1 to 7 and Comparative Examples 1 to 3, the VT characteristics of the samples immersed in boiling pure water for 60 minutes (in the chemical conversion solution) Voltage-time characteristic when 1.0 mA / cm 2 was applied), and a water resistance test for measuring the time until the Vt value was reached, and the capacitance was measured. The results are shown in Table 1.

Figure 2007299916
Figure 2007299916

表1から明らかなように、例えば、実施例2〜6の条件により得られた電解コンデンサ用アルミニウム電極箔は、比較例1(オルトリン酸の配合量1.5g/L)と比較してVt値までの到達時間が0.48〜0.53倍に減少し、皮膜の耐水性が向上していることがわかる。また、実施例2〜6の条件により得られた電解コンデンサ用アルミニウム電極箔では、静電容量が増加していることが分かる。   As can be seen from Table 1, for example, the aluminum electrode foil for electrolytic capacitors obtained under the conditions of Examples 2 to 6 had a Vt value as compared with Comparative Example 1 (blending amount of orthophosphoric acid 1.5 g / L). It can be seen that the arrival time until is reduced by 0.48 to 0.53 times, and the water resistance of the film is improved. Moreover, in the aluminum electrode foil for electrolytic capacitors obtained on the conditions of Examples 2-6, it turns out that an electrostatic capacitance is increasing.

これに対して、比較例2、3のように、オルトリン酸の配合量を4.5g/L、7.5g/Lとすると、電極箔表層部のリン酸根量は増え、耐水性は改良されるが、静電容量が著しく低下する。従って、耐水性および静電容量の双方を比較例2、3と対比すると、オルトリン酸の配合量は、本発明の実施例2〜6に係る条件が優れているといえる。   On the other hand, as in Comparative Examples 2 and 3, when the amount of orthophosphoric acid is 4.5 g / L and 7.5 g / L, the amount of phosphate radicals on the electrode foil surface layer is increased and the water resistance is improved. However, the capacitance is significantly reduced. Therefore, when both water resistance and electrostatic capacity are compared with Comparative Examples 2 and 3, it can be said that the amount of orthophosphoric acid is excellent under the conditions according to Examples 2 to 6 of the present invention.

なお、ヘキサメタリン酸ナトリウムの配合量が1.0g/Lの実施例1では、耐水性の改良効果が十分でなく、ヘキサメタリン酸ナトリウムの配合量が70.0g/Lの実施例7では、静電容量が減少している。
よって、ヘキサメタリン酸ナトリウムの配合量は、5.0〜50.0g/Lの範囲が好ましく、この条件によれば、表層部のリン酸根量を5.61〜29.5倍に増加させることができ、かつ、静電容量の向上も図ることができる。
In Example 1 where the amount of sodium hexametaphosphate was 1.0 g / L, the effect of improving water resistance was not sufficient, and in Example 7 where the amount of sodium hexametaphosphate was 70.0 g / L, Capacity is decreasing.
Therefore, the blending amount of sodium hexametaphosphate is preferably in the range of 5.0 to 50.0 g / L. According to this condition, the amount of phosphate in the surface layer portion can be increased 5.61 to 29.5 times. In addition, the capacitance can be improved.

[実施例8〜26]
上記実施例1〜7と同様に、エッチングされたアルミニウム箔を、アジピン酸アンモニウム80g/L、アジピン酸1.5g/Lを溶解した化成液中で、85±2℃にて電圧印加し、22Vまで電圧を上昇させて化成し、デポラリゼーション、再化成処理等を施す(陽極酸化工程)。
[Examples 8 to 26]
In the same manner as in Examples 1 to 7, a voltage was applied to an etched aluminum foil at 85 ± 2 ° C. in a chemical solution in which ammonium adipate 80 g / L and adipic acid 1.5 g / L were dissolved. Then, the voltage is raised until formation, followed by depolarization, re-forming treatment, etc. (anodic oxidation step).

次に、表2に示す添加量からなるヘキサメタリン酸ナトリウム(メタリン酸ナトリウム)およびオルトリン酸を含む水溶液からなるリン処理液に25±1℃で1分間浸漬を施し、化成箔(電解コンデンサ用電極箔)を得る。   Next, immersion was performed at 25 ± 1 ° C. for 1 minute in a phosphorous treatment solution comprising an aqueous solution containing sodium hexametaphosphate (sodium metaphosphate) and orthophosphoric acid having the addition amounts shown in Table 2 to form a chemical conversion foil (electrode foil for electrolytic capacitors) )

次に、上記の実施例1〜7と同様、上記の実施例8〜26の化成箔を、沸騰した純水に60分間浸漬した後、V−T特性(化成液中で低電流を印加した際の電圧−時間特性)を計測し、所定の電圧(Vt値)に到達するまでの時間を計測する耐水性試験、および静電容量を測定した。その結果を表2に示す。   Next, as in Examples 1 to 7, the chemical conversion foils of Examples 8 to 26 were immersed in boiling pure water for 60 minutes, and then subjected to VT characteristics (a low current was applied in the chemical conversion liquid). Voltage-time characteristics), and a water resistance test for measuring the time required to reach a predetermined voltage (Vt value), and the capacitance was measured. The results are shown in Table 2.

Figure 2007299916
Figure 2007299916

表2に示す結果において、耐水性および静電容量の双方を比較例と対比すると、ヘキサメタリン酸ナトリウムとオルトリン酸の添加量については、本発明の実施例8〜26に係る条件が優れているといえる。   In the results shown in Table 2, when both water resistance and capacitance are compared with the comparative examples, the addition amount of sodium hexametaphosphate and orthophosphoric acid is excellent in the conditions according to Examples 8 to 26 of the present invention. I can say that.

また、各実施例のうち、実施例9〜11、14〜16、19〜21の条件より得られた電解コンデンサ用アルミニウム電極箔は、表層部のリン酸根量が14.2〜45.1倍に増加し、従来例と比較してVt値までの到達時間が0.45〜0.52倍に減少しており、皮膜の耐水性が向上している。さらに、静電容量の増加も見られる。   Moreover, among each Example, the aluminum electrode foil for electrolytic capacitors obtained from the conditions of Examples 9-11, 14-16, 19-21 has a phosphate group amount of the surface layer part of 14.2-45.1 times. As compared with the conventional example, the time to reach the Vt value is reduced by 0.45 to 0.52 times, and the water resistance of the film is improved. Furthermore, an increase in capacitance is also observed.

これに対して、ヘキサメタリン酸ナトリウムの配合量が10g/Lの実施例8、13、18では、皮膜の耐水性の改良は見られるが、静電容量のわずかな減少も見られる。また、ヘキサメタリン酸ナトリウムの配合量が70g/Lの実施例12、17、22でも、多少の静電容量の減少が見られる。
また、オルトリン酸の配合量が0.75g/L、10.5g/Lの実施例23〜26では、表層部のリン酸根量は増え、皮膜の耐水性の改良は見られるが、静電容量の減少も見られる。よって、ヘキサメタリン酸ナトリウムの配合量は20.0〜50.0g/Lで、オルトリン酸の配合量は、1.5〜7.5g/Lの範囲が適当である。
On the other hand, in Examples 8, 13, and 18 in which the amount of sodium hexametaphosphate was 10 g / L, the water resistance of the film was improved, but a slight decrease in capacitance was also observed. Further, in Examples 12, 17, and 22 in which the amount of sodium hexametaphosphate was 70 g / L, a slight decrease in capacitance was observed.
Further, in Examples 23 to 26 in which the blending amount of orthophosphoric acid was 0.75 g / L and 10.5 g / L, the amount of phosphate radicals in the surface layer portion was increased, and the water resistance of the film was improved, but the capacitance There is also a decrease. Therefore, the blending amount of sodium hexametaphosphate is 20.0-50.0 g / L, and the blending amount of orthophosphoric acid is suitably in the range of 1.5-7.5 g / L.

なお、上記実施例としてヘキサメタリン酸ナトリウムを用いたが、ナトリウム塩だけでなく、カリウム塩であっても、同様の効果を得ることができる。また、上記形態では、縮合リン酸塩としてヘキサメタリン酸塩を用いたが、ピロリン酸塩、酸性ピロリン酸塩、トリポリリン酸塩、テトラポリリン酸塩、酸性ヘキサメタリン酸塩などを用いてもよい。
さらに、縮合リン酸塩に代えて、縮合リン酸の状態で配合してもよい。また、オルトリン酸については塩の形態で配合してもよい。
In addition, although sodium hexametaphosphate was used as the said Example, even if it is not only a sodium salt but potassium salt, the same effect can be acquired. Moreover, in the said form, although hexametaphosphate was used as condensed phosphate, you may use pyrophosphate, acidic pyrophosphate, tripolyphosphate, tetrapolyphosphate, acidic hexametaphosphate, etc.
Furthermore, it may be blended in the state of condensed phosphoric acid instead of the condensed phosphate. Orthophosphoric acid may be added in the form of a salt.

さらに、上記実際例では、陽極酸化工程の後、アルミニウム箔を縮合リン酸または/および縮合リン酸塩を含むリン処理液に浸漬する例であったが、陽極酸化工程の途中において、アルミニウム箔を縮合リン酸または/および縮合リン酸塩を含むリン処理液に浸漬してもよい。   Further, in the above actual example, after the anodizing step, the aluminum foil was immersed in a phosphorus treatment solution containing condensed phosphoric acid or / and condensed phosphate, but in the middle of the anodizing step, the aluminum foil was You may immerse in the phosphorus treatment liquid containing condensed phosphoric acid or / and condensed phosphate.

さらにまた、本発明を適用した電解コンデンサ用電極箔は、耐水性に他、静電容量も向上していることから、電解液中に水分を配合した電解コンデンサに限らず、全ての電解コンデンサに用いることができる。   Furthermore, the electrolytic capacitor electrode foil to which the present invention is applied has improved water resistance and capacitance, so it is not limited to electrolytic capacitors in which moisture is mixed in the electrolytic solution, but to all electrolytic capacitors. Can be used.

Claims (5)

エッチングされたアルミニウム箔に陽極酸化により酸化皮膜を形成する陽極酸化工程を有する電解コンデンサ用電極箔の製造方法において、
前記陽極酸化工程の後、または当該陽極酸化工程の途中においてアルミニウム箔を縮合リン酸または/および縮合リン酸塩を含むリン処理液に浸漬することを特徴とする電解コンデンサ用電極箔の製造方法。
In the method of manufacturing an electrode foil for an electrolytic capacitor having an anodizing step of forming an oxide film by anodic oxidation on an etched aluminum foil,
A method for producing an electrode foil for an electrolytic capacitor, comprising immersing an aluminum foil in a phosphorus treatment solution containing condensed phosphoric acid or / and condensed phosphate after the anodizing step or during the anodizing step.
前記リン処理液には、前記縮合リン酸または前記縮合リン酸塩として、メタリン酸、メタリン酸ナトリウム塩、またはメタリン酸カリウム塩の少なくとも1種が配合されていることを特徴とする請求項1に記載の電解コンデンサ用電極箔の製造方法。   2. The phosphoric acid treatment liquid according to claim 1, wherein at least one of metaphosphoric acid, sodium metaphosphate, or potassium metaphosphate is blended as the condensed phosphoric acid or the condensed phosphate. The manufacturing method of the electrode foil for electrolytic capacitors of description. 前記リン処理液中における前記縮合リン酸または/および前記縮合リン酸塩の全配合量が、5.0〜50g/Lであることを特徴とする請求項1または2に記載の電解コンデンサ用電極箔の製造方法。   3. The electrode for an electrolytic capacitor according to claim 1, wherein the total amount of the condensed phosphoric acid or / and the condensed phosphate in the phosphorus treatment solution is 5.0 to 50 g / L. 4. Foil manufacturing method. 前記リン処理液には、さらにオルトリン酸または/およびオルトリン酸塩が配合されていることを特徴とする請求項1または2に記載の電解コンデンサ用電極箔の製造方法。   The method for producing an electrode foil for an electrolytic capacitor according to claim 1, wherein orthophosphoric acid and / or orthophosphate is further blended in the phosphorus treatment solution. 請求項4に記載のリン処理液中における前記縮合リン酸または/および前記縮合リン酸塩の全配合量が20〜50g/Lであり、かつ、
当該リン処理液における前記オルトリン酸または/および前記オルトリン酸塩の全配合量が1.5〜7.5g/Lであることを特徴とする電解コンデンサ用電極箔の製造方法。
The total amount of the condensed phosphoric acid or / and the condensed phosphate in the phosphorus treatment solution according to claim 4 is 20 to 50 g / L, and
The manufacturing method of the electrode foil for electrolytic capacitors characterized by the total compounding quantity of the said orthophosphoric acid or / and the said orthophosphate in the said phosphorus treatment liquid being 1.5-7.5 g / L.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003289021A (en) * 2002-03-28 2003-10-10 Nippon Chemicon Corp Electrode foil for electrolytic capacitor and method for manufacturing the same and electrolytic capacitor using the method
JP2005142343A (en) * 2003-11-06 2005-06-02 Nichicon Corp Method of manufacturing electrode foil for aluminum electrolytic capacitor

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003289021A (en) * 2002-03-28 2003-10-10 Nippon Chemicon Corp Electrode foil for electrolytic capacitor and method for manufacturing the same and electrolytic capacitor using the method
JP2005142343A (en) * 2003-11-06 2005-06-02 Nichicon Corp Method of manufacturing electrode foil for aluminum electrolytic capacitor

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