JP7368228B2 - Manufacturing method of electrode foil for electrolytic capacitors - Google Patents

Manufacturing method of electrode foil for electrolytic capacitors Download PDF

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JP7368228B2
JP7368228B2 JP2019235838A JP2019235838A JP7368228B2 JP 7368228 B2 JP7368228 B2 JP 7368228B2 JP 2019235838 A JP2019235838 A JP 2019235838A JP 2019235838 A JP2019235838 A JP 2019235838A JP 7368228 B2 JP7368228 B2 JP 7368228B2
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真一 南山
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Nichicon Corp
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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。 The present invention relates to a method of manufacturing an electrode foil for an electrolytic capacitor.

電解コンデンサ用電極箔の製造方法に関し、下記の非特許文献1には、従来から用いられてきたロール給電法(金属製給電ロールを直接アルミニウム箔に接触させて給電する方法)による既存の化成機の一部を改造するだけで比較的容易に液中給電法(電解液を介してアルミニウム箔に間接的に給電する方法)に切り替え可能であることが開示されている。さらに、化成工程における液中給電槽の電解液は、電解液の汚染を防ぐためにも、化成液と共通とすることが好ましいとされ、アジピン酸アンモニウムの水溶液を使用することが記載されている。 Regarding the manufacturing method of electrode foil for electrolytic capacitors, the following non-patent document 1 describes an existing chemical forming machine using the conventionally used roll power feeding method (a method in which power is supplied by bringing a metal power feeding roll into direct contact with an aluminum foil). It is disclosed that it is possible to switch to the submerged power supply method (a method of indirectly supplying power to the aluminum foil through an electrolytic solution) relatively easily by simply modifying a part of the . Further, in order to prevent contamination of the electrolytic solution, it is preferable to use the same electrolytic solution in the submerged power supply tank in the chemical formation process, and it is described that an aqueous solution of ammonium adipate is used.

中島等、「電解コンデンサー用アルミ箔の液中給電化成技術の開発と実用化」、電気化学および工業物理化学(電気化学会編)、64、No.7、(1996)p.801-804Nakajima et al., “Development and practical application of submerged power supply chemical technology for aluminum foil for electrolytic capacitors,” Electrochemistry and Industrial Physical Chemistry (edited by the Electrochemical Society), 64, No. 7, (1996) p. 801-804

しかしながら、非特許文献1のアジピン酸アンモニウムの水溶液を使用した液中給電では、化成皮膜への損傷が大きくなるという問題や、電極箔の歪が大きくなり、外観不良が生じる問題があった。
本発明は、上述の問題点を解決するものであり、化成皮膜への損傷と、電極箔の歪を軽減することが可能な電解コンデンサ用電極箔の製造方法を提供することを課題とする。
However, in the submerged power supply using an aqueous solution of ammonium adipate in Non-Patent Document 1, there were problems such as increased damage to the chemical conversion film and increased distortion of the electrode foil, resulting in poor appearance.
The present invention solves the above-mentioned problems, and an object of the present invention is to provide a method for manufacturing an electrode foil for an electrolytic capacitor that can reduce damage to a chemical conversion film and distortion of an electrode foil.

前記の課題を解決可能な本発明の製造方法は、エッチングされた電極箔に液中給電槽の電解液を介して給電する電解コンデンサ用電極箔の製造方法において、前記電解液が、クエン酸のアンモニウム塩とリン酸を含むことを特徴とする。
なお、本明細書において、「クエン酸のアンモニウム塩」とは、クエン酸三アンモニウム、クエン酸二水素アンモニウム、クエン酸水素二アンモニウムを意味する。
尚、本発明の製造方法において使用される電解液は、上記の「クエン酸のアンモニウム塩」に、アンモニア水を添加して水溶液を調製し(この液のpHは、例えば5.6~5.9程度)、その後、リン酸を添加(リン酸添加後のpHは5.6~5.8程度)して調製したものであっても良く、クエン酸を含む水溶液にアンモニア水を添加することにより、クエン酸のアンモニウム塩を生成するとともにpH調整し(例えばpH5.6~5.9)、その後、リン酸を添加して得られた水溶液(リン酸添加後のpHは上記と同じ)であっても良い。
The manufacturing method of the present invention capable of solving the above-mentioned problems is a manufacturing method of an electrode foil for an electrolytic capacitor in which power is supplied to an etched electrode foil via an electrolytic solution in a submerged power supply tank, in which the electrolytic solution is made of citric acid. It is characterized by containing ammonium salt and phosphoric acid.
In addition, in this specification, "ammonium salt of citric acid" means triammonium citrate, ammonium dihydrogen citrate, and diammonium hydrogen citrate.
The electrolytic solution used in the production method of the present invention is prepared by adding ammonia water to the above-mentioned "ammonium salt of citric acid" to prepare an aqueous solution (the pH of this solution is, for example, 5.6-5. 9), then adding phosphoric acid (the pH after adding phosphoric acid is about 5.6 to 5.8), or adding ammonia water to an aqueous solution containing citric acid. to generate an ammonium salt of citric acid and adjust the pH (for example, pH 5.6 to 5.9), and then add phosphoric acid to the resulting aqueous solution (the pH after adding phosphoric acid is the same as above). It's okay.

また、本発明は、上記の特徴を有する電解コンデンサ用電極箔の製造方法において、前記電解液中のクエン酸のアンモニウム塩の濃度が0.13~0.25モル/lであり、リン酸の濃度が0.001~0.1モル/lであることを特徴とするものである。 The present invention also provides a method for manufacturing an electrode foil for an electrolytic capacitor having the above characteristics, wherein the concentration of ammonium salt of citric acid in the electrolytic solution is 0.13 to 0.25 mol/l, and It is characterized by a concentration of 0.001 to 0.1 mol/l.

さらに、本発明は、上記の特徴を有する電解コンデンサ用電極箔の製造方法において、前記電解液を用いた液中給電を、50~200mA/cmの電流密度にて、3~20分間行うことを特徴とするものである。 Furthermore, the present invention provides a method for manufacturing an electrode foil for an electrolytic capacitor having the above-mentioned characteristics, in which submerged power supply using the electrolytic solution is performed at a current density of 50 to 200 mA/cm 2 for 3 to 20 minutes. It is characterized by:

本発明では、液中給電工程において使用される電解液にアジピン酸アンモニウム水溶液を用いる従来技術に比べて、化成皮膜への損傷と、電極箔の歪を軽減した電解コンデンサ用電極箔を製造することができる。 In the present invention, it is possible to manufacture an electrode foil for an electrolytic capacitor that reduces damage to the chemical conversion film and reduces distortion of the electrode foil, compared to the conventional technology that uses an aqueous ammonium adipate solution as the electrolyte used in the submerged power supply process. Can be done.

実施例の電解コンデンサ用電極箔の外観写真である。It is an appearance photograph of the electrode foil for electrolytic capacitors of an example. 比較例1の電解コンデンサ用電極箔の外観写真である。2 is a photograph of the appearance of an electrode foil for an electrolytic capacitor of Comparative Example 1. 比較例2の電解コンデンサ用電極箔の外観写真である。It is an external photograph of the electrode foil for electrolytic capacitors of Comparative Example 2. 比較例3の電解コンデンサ用電極箔の外観写真である。It is an appearance photograph of the electrode foil for electrolytic capacitors of Comparative Example 3.

本発明の電解コンデンサ用電極箔の製造方法では、液中給電槽の電解液として、クエン酸のアンモニウム塩とリン酸を含む電解液を調製し、第1化成工程後のアルミニウム箔を、当該電解液を介して所定温度(好ましくは20~40℃)で液中給電する。本発明にて使用される電解液中のクエン酸のアンモニウム塩の濃度は0.13~0.25モル/lであり、例えば、クエン酸のアンモニウム塩として、クエン酸水素二アンモニウムを使用する場合、電解液1リットル中の濃度は35~45g/l(0.155~0.199モル/l)が好ましく、38~42g/lがより好ましく、リン酸の濃度は0.001~0.1モル/lが好ましく、0.003~0.02モル/lがより好ましい。 In the method for manufacturing an electrode foil for an electrolytic capacitor of the present invention, an electrolytic solution containing an ammonium salt of citric acid and phosphoric acid is prepared as an electrolytic solution for a submerged power supply tank, and the aluminum foil after the first chemical conversion step is subjected to the electrolysis. Power is supplied through the liquid at a predetermined temperature (preferably 20 to 40°C). The concentration of ammonium salt of citric acid in the electrolytic solution used in the present invention is 0.13 to 0.25 mol/l, for example, when diammonium hydrogen citrate is used as the ammonium salt of citric acid. , the concentration in 1 liter of electrolyte is preferably 35 to 45 g/l (0.155 to 0.199 mol/l), more preferably 38 to 42 g/l, and the concentration of phosphoric acid is 0.001 to 0.1 The amount is preferably mol/l, more preferably 0.003 to 0.02 mol/l.

また、エッチングされたアルミニウム箔に対して液中給電工程を実施する前に以下の化成工程が実施される。例えば、高圧用電極箔に使用されるエッチングされたアルミニウム箔の場合、純水中で1~20分間程度、熱水ボイルを行った後、アンモニア水で中和されたホウ酸系(ホウ酸またはその塩を含む)化成液中でロール給電による所定電圧まで化成を行う(第1化成工程)。この際、化成液中のホウ酸濃度は5~10重量%であることが好ましく、印加される電流密度、電圧および電圧印加時間については適宜選択することができる。
以下、実施例に基づいて、本発明の製造方法を説明するが、本発明はこれに限定されるものではない。
In addition, the following chemical conversion process is performed on the etched aluminum foil before the submerged power supply process is performed. For example, in the case of etched aluminum foil used for high-voltage electrode foil, it is boiled in pure water for about 1 to 20 minutes, then boric acid-based (boric acid or Chemical formation is performed in a chemical liquid (containing the salt) up to a predetermined voltage by roll power supply (first chemical formation step). At this time, the concentration of boric acid in the chemical conversion liquid is preferably 5 to 10% by weight, and the applied current density, voltage, and voltage application time can be selected as appropriate.
The manufacturing method of the present invention will be described below based on Examples, but the present invention is not limited thereto.

(実施例)
高圧用電極箔に使用されるエッチングされたアルミニウム箔(厚さ:120μm)を準備し、純水中で10分間、熱水ボイルを行った後、第1化成工程としてアンモニア水で中和された10重量%のホウ酸化成液中にて、ロール給電(電極箔接触給電)により定電流条件下(電流密度:20mA/cm)で電圧を上昇させ、500Vに到達した後、当該電圧を3分間維持した。
その後、アンモニア水溶液でpH調整(pH5.6~5.9)されたクエン酸水素二アンモニウム水溶液(電解液中のクエン酸水素二アンモニウム濃度:40g/l、4重量%、アンモニア水濃度0.1モル/l)中に0.005モル/lのリン酸を添加した30℃の電解液中にて液中給電を実施し(5分間)、アンモニア水で中和された5~10重量%のホウ酸化成液中で所定の電圧(例えば、540V)まで電圧を上昇させた後、所定電圧を一定時間(例えば、40分間)維持する第2化成工程を行った。この時の液中給電の電流密度は75mA/cmとした。その後、既知の方法にて熱処理、薬液浸漬、再化成工程を行った。
(Example)
Etched aluminum foil (thickness: 120 μm) used for high-voltage electrode foil was prepared, and after hot water boiling in pure water for 10 minutes, it was neutralized with aqueous ammonia as the first chemical conversion step. In a 10% by weight boric acid solution, the voltage was increased under constant current conditions (current density: 20 mA/cm 2 ) by roll power supply (electrode foil contact power supply), and after reaching 500V, the voltage was increased to 3 It was maintained for a minute.
Then, a diammonium hydrogen citrate aqueous solution whose pH was adjusted (pH 5.6 to 5.9) with an ammonia aqueous solution (concentration of diammonium hydrogen citrate in electrolyte solution: 40 g/l, 4% by weight, aqueous ammonia concentration 0.1 In-liquid power supply was carried out (for 5 minutes) in an electrolytic solution at 30°C containing 0.005 mol/l of phosphoric acid (mol/l), and 5 to 10% by weight neutralized with aqueous ammonia was used. After increasing the voltage to a predetermined voltage (for example, 540 V) in the boric acid solution, a second chemical conversion step was performed in which the predetermined voltage was maintained for a certain period of time (for example, 40 minutes). The current density of the submerged power supply at this time was 75 mA/cm 2 . Thereafter, heat treatment, chemical immersion, and reconversion steps were performed using known methods.

(比較例1)
電解液として、アジピン酸アンモニウム水溶液(濃度:40g/l)を用いた以外は、上記実施例と同様にして液中給電を実施した。
(Comparative example 1)
In-liquid power supply was carried out in the same manner as in the above example except that an ammonium adipate aqueous solution (concentration: 40 g/l) was used as the electrolyte.

(比較例2)
電解液として、アジピン酸アンモニウム水溶液(濃度:40g/l)中に0.005モル/lのリン酸を添加したものを用いた以外は、上記実施例と同様にして液中給電を実施した。
(Comparative example 2)
In-liquid power supply was carried out in the same manner as in the above example, except that an ammonium adipate aqueous solution (concentration: 40 g/l) to which 0.005 mol/l of phosphoric acid was added was used as the electrolytic solution.

(比較例3)
電解液として、リン酸無添加のものを用いた以外は、上記実施例と同様にして液中給電を実施した。
(Comparative example 3)
Submerged power supply was performed in the same manner as in the above example except that an electrolytic solution to which no phosphoric acid was added was used.

[評価方法]
上記実施例および比較例1~3について、液中給電時に測定された電極箔の初期電圧を測定し、各初期電圧の比較を行った。比較例2、3および実施例の電圧降下率は比較例1を基準とした百分率を示す。また、実施例および比較例1~3について、電極箔の歪を測定した。図1に実施例、図2に比較例1、図3に比較例2、図4に比較例3の電極箔の外観を示す。歪は電極箔の最も反りが大きい箇所が、水平面からどれだけ離れているか測定することで行った。 その結果を以下の表1に示す。
[Evaluation method]
For the above Examples and Comparative Examples 1 to 3, the initial voltage of the electrode foil measured during submerged power supply was measured, and each initial voltage was compared. The voltage drop rates of Comparative Examples 2 and 3 and Examples are percentages based on Comparative Example 1. In addition, for Examples and Comparative Examples 1 to 3, the strain of the electrode foils was measured. The external appearance of the electrode foil of Example is shown in FIG. 1, Comparative Example 1 is shown in FIG. 2, Comparative Example 2 is shown in FIG. 3, and Comparative Example 3 is shown in FIG. Strain was determined by measuring how far the most warped part of the electrode foil was from the horizontal plane. The results are shown in Table 1 below.

Figure 0007368228000001
Figure 0007368228000001

上記表1の結果から、本発明の製造方法を用いて得られた電解コンデンサ用電極箔(実施例)は、アジピン酸アンモニウムを単独で含む水溶液(比較例1)、アジピン酸アンモニウムとリン酸を含む水溶液(比較例2)およびリン酸を添加していない水溶液(比較例3)を用いて得られた電極箔よりも初期電圧が小さく、化成皮膜への損傷が少ないことが確認された。 From the results in Table 1 above, it can be seen that the electrode foil for electrolytic capacitors (Example) obtained using the manufacturing method of the present invention contains an aqueous solution containing ammonium adipate alone (Comparative Example 1), ammonium adipate and phosphoric acid. It was confirmed that the initial voltage was lower than the electrode foils obtained using the aqueous solution containing phosphoric acid (Comparative Example 2) and the aqueous solution without phosphoric acid (Comparative Example 3), and there was less damage to the chemical conversion coating.

また、表1と図1~4より、実施例の電解コンデンサ用電極箔は、比較例1~3の電解コンデンサ用電極箔と比較して歪が軽減されている。 Further, from Table 1 and FIGS. 1 to 4, the electrode foils for electrolytic capacitors of Examples have reduced distortion compared to the electrode foils for electrolytic capacitors of Comparative Examples 1 to 3.

なお、実施例ではクエン酸をアンモニアでpH調整した液として、クエン酸水素二アンモニウムを用いたが、他にクエン酸三アンモニウム、クエン酸二水素アンモニウムを用いても同様の効果が得られる。 In the examples, diammonium hydrogen citrate was used as a solution in which the pH of citric acid was adjusted with ammonia, but the same effect can be obtained by using triammonium citrate or ammonium dihydrogen citrate.

また、実施例では第1化成工程をすべてロール給電としたが、第1化成工程の終段を液中給電による給電としてもよい。 Further, in the embodiment, the first chemical formation step was entirely powered by roll power, but the final stage of the first chemical formation step may be powered by submerged power supply.

本発明の製造方法は、電解コンデンサ用電極箔の製造において、優れた特性を有した電極箔を生産性良く製造するのに有用である。 The manufacturing method of the present invention is useful for manufacturing electrode foils with excellent properties with high productivity in manufacturing electrode foils for electrolytic capacitors.

Claims (4)

エッチングされた電極箔に液中給電槽の電解液を介して液中給電する電解コンデンサ用電極箔の製造方法において、
前記電解液が、クエン酸のアンモニウム塩とリン酸を含み、
前記電解液中のクエン酸のアンモニウム塩の濃度が0.13~0.25モル/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。
In a method for manufacturing an electrode foil for an electrolytic capacitor in which electricity is supplied submerged to the etched electrode foil via an electrolyte in a submerged power supply tank,
The electrolyte solution contains ammonium salt of citric acid and phosphoric acid,
A method for producing an electrode foil for an electrolytic capacitor, characterized in that the concentration of ammonium salt of citric acid in the electrolytic solution is 0.13 to 0.25 mol/l .
前記電解液中のリン酸の濃度が0.001~0.1モル/lであ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。 The method for producing an electrode foil for an electrolytic capacitor according to claim 1, wherein the concentration of phosphoric acid in the electrolytic solution is 0.001 to 0.1 mol/l. 前記クエン酸のアンモニウム塩が、クエン酸三アンモニウム、クエン酸二水素アンモニウム、およびクエン酸水素二アンモニウムからなるグループより選ばれたもの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 electrolytic capacitor according to claim 1, wherein the ammonium salt of citric acid is selected from the group consisting of triammonium citrate, ammonium dihydrogen citrate, and diammonium hydrogen citrate. Method for manufacturing electrode foil for use. 前記電解液を用いた液中給電を、50~200mA/cmの電流密度にて、3~20分間行うことを特徴とする請求項1~3のいずれか1項に記載の電解コンデンサ用電極箔の製造方法。 The electrode for an electrolytic capacitor according to any one of claims 1 to 3, wherein the submerged power supply using the electrolytic solution is performed at a current density of 50 to 200 mA/cm 2 for 3 to 20 minutes. Method of manufacturing foil.
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