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JPH0566005B2 - - Google Patents
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JPH0566005B2 - - Google Patents

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Publication number
JPH0566005B2
JPH0566005B2 JP1037525A JP3752589A JPH0566005B2 JP H0566005 B2 JPH0566005 B2 JP H0566005B2 JP 1037525 A JP1037525 A JP 1037525A JP 3752589 A JP3752589 A JP 3752589A JP H0566005 B2 JPH0566005 B2 JP H0566005B2
Authority
JP
Japan
Prior art keywords
aluminum foil
aqueous solution
acid
treatment
producing
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
JP1037525A
Other languages
Japanese (ja)
Other versions
JPH02216811A (en
Inventor
Kazuyuki Adachi
Noboru Haga
Manabu Kazuhara
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.)
Elna Co Ltd
Original Assignee
Elna 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 Elna Co Ltd filed Critical Elna Co Ltd
Priority to JP1037525A priority Critical patent/JPH02216811A/en
Publication of JPH02216811A publication Critical patent/JPH02216811A/en
Publication of JPH0566005B2 publication Critical patent/JPH0566005B2/ja
Granted legal-status Critical Current

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  • Chemical Treatment Of Metals (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 この発明は電解コンデンサ用アルミニウム箔の
製造方法に関し、さらに詳しく言えば、アルミニ
ウム箔を化成するに先立つて行われる水和処理に
関するものである。 〔従来の技術〕 電解コンデンサの陽極として使用される電極
箔、例えば平滑なアルミニウム箔やエツチングに
より表面積が拡大されたアルミニウム箔は、これ
に陽極酸化皮膜を形成する化成処理に先立つて水
和処理が施される。 水和処理は、アルミニウム箔の表面に水酸化皮
膜を形成させることを目的とするものであるが、
通常はアルミニウム箔を高温の純水中に浸漬する
ことによつて行われる。 〔発明が解決しようとする課題〕 これによれば、化成時の使用電気量が節約さ
れ、また、静電容量も増大される。しかしなが
ら、耐電圧が低い場合には良好な結果が得られ
ず、約150V以上の場合にのみ有用であるという
制約があつた。 そこで、純水中に微量の硅酸アルカリを添加し
て水和処理することが提案された(例えば、特公
昭57−6250号公報参照)。この方法によると、使
用電圧の低いものに対してまでも水和処理が有用
とされるが、tanδ(損失角の正接)、漏れ電流につ
いては特に改善されない。 〔課題を解決するための手段〕 上記の課題を解決するため、この発明において
は、アルミニウム箔に酸化皮膜を形成する化成処
理を行うに先立つて、同アルミニウム箔をアミン
と酸を添加した水溶液中において熱水処理するこ
とを特徴としている。この場合、熱水の温度とし
ては90℃以上が好ましい。 これによれば、使用電圧の低いものまでに対し
ても、化成時の使用電気量の節約、静電容量の増
大はもとより、tanδおよび漏れ電流が低下され
る。 なお、アミン濃度は0.005〜0.1mol/lである
ことが好ましい。使用し得るアミンとしては、エ
チルアミン、ジエチルアミン、トリエタノールア
ミン、プロピルアミン、ジプロピルアミン、ブチ
ルアミンなどが挙げられる。また、使用し得る酸
としては、酢酸、安息香酸、硼酸などである。さ
らに、水溶液のPHは5〜9の範囲が好ましい。 〔実施例〕 実施例 1 (A) 前処理;エチルアミンと酢酸とを添加して、
アミン濃度0.01mol/l、PH6とした水溶液
(液温98℃以上)に、アルミニウム箔を9分間
浸漬して熱水処理した。 (B) 化成処理;硼酸17%、硼安0.05%を含む化成
液(液温85℃)中において、電流密度10mA/
cm2、380Vの化成電圧を40分印加した。 (C) 減極処理;PH9のアンモニア水(液温70℃)
中に3分間浸漬した。 (D) 熱処理;500℃の加熱雰囲気中に2分間放置
した。 (E) 再化成;上記(B)と同じ。ただし、印加時間は
13分。 (F) 減極処理;上記(C)と同じ。 (G) 熱処理;上記(D)と同じ。 (H) 再化成;上記(E)と同じ。 (I) 後処理;PH6.5のリン酸、アンモニア混合水
溶液(液温30℃)中に4分間浸漬した。 実施例 2 (A) 前処理;エチルアミンと安息香酸とを添加し
て、アミン濃度0.01mol/l、PH6とした水溶
液(液温98℃以上)にアルミニウム箔を9分間
浸漬して熱水処理した。以後の(B)〜(I)までの工
程は上記実施例1と同じ。 実施例 3 (A) 前処理;エチルアミンと硼酸とを添加して、
アミン濃度0.01mol/l、PH6とした水溶液
(液温98℃以上)にアルミニウム箔を9分間浸
漬して熱水処理した。以後の(B)〜(I)までの工程
は上記実施例1と同じ。 実施例 4 (A) 前処理;ジエチルアミンと酢酸とを添加し
て、アミン濃度0.01mol/、PH6とした水溶液
(液温98℃以上)にアルミニウム箔を9分間浸
漬して熱水処理した。以後の(B)〜(I)までの工程
は上記実施例1と同じ。 実施例 5 (A) 前処理;トリエタールアミンと酢酸とを添加
して、アミン濃度0.01mol/l、PH6とした水
溶液(液温98℃以上)にアルミニウム箔を9分
間浸漬して熱水処理した。以後の(B)〜(I)までの
工程は上記実施例1と同じ。 比較例 1 (A) 前処理;アルミニウム箔を純水(液温98℃以
上)中に9分間浸漬して熱水処理した。以後の
(B)〜(I)までの工程は上記実施例1と同じ。 比較例 2 (A) 前処理;アルミニウム箔を硅酸アルカリを硅
素濃度にして0.1%含む熱水(液温98℃以上)
中に9分間浸漬して熱水処理した。以後の(B)〜
(I)までの工程は上記実施例1と同じ。 上記実施例1〜5および比較例1、2にて得ら
れたアルミニウム化成箔(15×270mm)を陽極と
して、定格250V、30μFの電解コンデンサを試作
し、その静電容量、tanδおよび漏れ電流を測定し
た結果を次表に示す。
[Industrial Application Field] The present invention relates to a method for manufacturing aluminum foil for electrolytic capacitors, and more specifically, to a hydration treatment performed prior to chemical conversion of the aluminum foil. [Prior Art] Electrode foils used as anodes for electrolytic capacitors, such as smooth aluminum foils or aluminum foils whose surface area has been expanded by etching, are subjected to hydration treatment prior to chemical conversion treatment to form an anodic oxide film. administered. The purpose of hydration treatment is to form a hydroxide film on the surface of aluminum foil.
This is usually done by immersing the aluminum foil in high-temperature pure water. [Problems to be Solved by the Invention] According to this, the amount of electricity used during chemical formation is saved, and the capacitance is also increased. However, good results cannot be obtained when the withstand voltage is low, and there is a restriction that it is useful only when the withstand voltage is about 150V or higher. Therefore, it has been proposed to add a small amount of alkali silicate to pure water for hydration treatment (see, for example, Japanese Patent Publication No. 1983-6250). According to this method, the hydration treatment is said to be useful even for low voltages, but tan δ (tangent of loss angle) and leakage current are not particularly improved. [Means for Solving the Problems] In order to solve the above problems, in the present invention, prior to performing a chemical conversion treatment to form an oxide film on the aluminum foil, the aluminum foil is soaked in an aqueous solution containing an amine and an acid. It is characterized by hot water treatment. In this case, the temperature of the hot water is preferably 90°C or higher. According to this, even when the voltage used is low, the amount of electricity used during chemical formation is saved, the capacitance is increased, and tan δ and leakage current are reduced. Note that the amine concentration is preferably 0.005 to 0.1 mol/l. Amines that can be used include ethylamine, diethylamine, triethanolamine, propylamine, dipropylamine, butylamine, and the like. Furthermore, examples of acids that can be used include acetic acid, benzoic acid, and boric acid. Furthermore, the pH of the aqueous solution is preferably in the range of 5 to 9. [Example] Example 1 (A) Pretreatment: Adding ethylamine and acetic acid,
The aluminum foil was immersed in an aqueous solution (liquid temperature of 98° C. or higher) with an amine concentration of 0.01 mol/l and a pH of 6 for 9 minutes to undergo hot water treatment. (B) Chemical conversion treatment; current density 10 mA/
cm 2 , and a formation voltage of 380 V was applied for 40 minutes. (C) Depolarization treatment; PH9 ammonia water (liquid temperature 70℃)
immersed in it for 3 minutes. (D) Heat treatment: The sample was left in a heated atmosphere at 500°C for 2 minutes. (E) Reconstitution; same as (B) above. However, the application time is
13 minutes. (F) Depolarization treatment; same as (C) above. (G) Heat treatment; same as (D) above. (H) Reconstitution; same as (E) above. (I) Post-treatment: Immersed for 4 minutes in a mixed aqueous solution of phosphoric acid and ammonia (liquid temperature: 30°C) of pH 6.5. Example 2 (A) Pretreatment: Aluminum foil was immersed in an aqueous solution (liquid temperature of 98°C or higher) for 9 minutes to perform hot water treatment by adding ethylamine and benzoic acid to give an amine concentration of 0.01 mol/l and a pH of 6. . The subsequent steps (B) to (I) are the same as in Example 1 above. Example 3 (A) Pretreatment: Adding ethylamine and boric acid,
The aluminum foil was immersed in an aqueous solution with an amine concentration of 0.01 mol/l and a pH of 6 (liquid temperature of 98° C. or higher) for 9 minutes to undergo hot water treatment. The subsequent steps (B) to (I) are the same as in Example 1 above. Example 4 (A) Pretreatment: Aluminum foil was immersed in an aqueous solution (liquid temperature of 98° C. or higher) of 0.01 mol/mol/pH 6 for 9 minutes to perform hot water treatment by adding diethylamine and acetic acid. The subsequent steps (B) to (I) are the same as in Example 1 above. Example 5 (A) Pretreatment: Aluminum foil was immersed in an aqueous solution (liquid temperature of 98°C or higher) of 98°C or higher for 9 minutes to undergo hot water treatment by adding triethalamine and acetic acid to give an amine concentration of 0.01 mol/l and a pH of 6. did. The subsequent steps (B) to (I) are the same as in Example 1 above. Comparative Example 1 (A) Pretreatment: Aluminum foil was immersed in pure water (liquid temperature 98° C. or higher) for 9 minutes to undergo hot water treatment. subsequent
The steps (B) to (I) are the same as in Example 1 above. Comparative Example 2 (A) Pretreatment: Aluminum foil was heated with hot water containing alkali silicate at a silicon concentration of 0.1% (liquid temperature 98°C or higher)
The samples were immersed in a hot water solution for 9 minutes and treated with hot water. Subsequent (B)~
The steps up to (I) are the same as in Example 1 above. An electrolytic capacitor with a rating of 250 V and 30 μF was prototyped using the chemically formed aluminum foil (15 x 270 mm) obtained in Examples 1 to 5 and Comparative Examples 1 and 2 as an anode, and its capacitance, tanδ, and leakage current were measured. The measured results are shown in the table below.

【表】【table】

〔発明の効果〕〔Effect of the invention〕

以上説明したように、この発明によれば、アル
ミニウム箔をアミンと酸を添加した水溶液中にお
いて熱水処理することにより、その後に行われる
化成処理時における使用電気量の節約、静電容量
の増大、tanδ(電気損失角)および漏れ電流の低
下が達成される。
As explained above, according to the present invention, aluminum foil is treated with hot water in an aqueous solution containing an amine and an acid, thereby reducing the amount of electricity used during the subsequent chemical conversion treatment and increasing the capacitance. , tan δ (electrical loss angle) and leakage current reduction are achieved.

Claims (1)

【特許請求の範囲】 1 アルミニウム箔に酸化皮膜を形成する化成処
理を行うに先立つて、同アルミニウム箔をアミン
と酸を添加した水溶液中において熱水処理するこ
とを特徴とする電解コンデンサ用アルミニウム箔
の製造方法。 2 上記水溶液中におけるアミンの濃度は、
0.005〜0.1mol/lである請求項1記載の電解コ
ンデンサ用アルミニウム箔の製造方法。 3 上記水溶液中に添加されるアミンは、エチル
アミン、ジエチルアミン、トリエタノールアミ
ン、プロピルアミン、ジプロピルアミン、ブチル
アミンから選ばれる請求項1または2記載の電解
コンデンサ用アルミニウム箔の製造方法。 4 上記酸は、酢酸、安息香酸、硼酸から選ばれ
る請求項1記載の電解コンデンサ用アルミニウム
箔の製造方法。 5 上記水溶液のPHは、5〜9である請求項1記
載の電解コンデンサ用アルミニウム箔の製造方
法。
[Claims] 1. An aluminum foil for an electrolytic capacitor, characterized in that, prior to performing a chemical conversion treatment to form an oxide film on the aluminum foil, the aluminum foil is subjected to hot water treatment in an aqueous solution containing an amine and an acid. manufacturing method. 2 The concentration of amine in the above aqueous solution is
The method for producing aluminum foil for electrolytic capacitors according to claim 1, wherein the content is 0.005 to 0.1 mol/l. 3. The method for producing an aluminum foil for an electrolytic capacitor according to claim 1 or 2, wherein the amine added to the aqueous solution is selected from ethylamine, diethylamine, triethanolamine, propylamine, dipropylamine, and butylamine. 4. The method for producing an aluminum foil for an electrolytic capacitor according to claim 1, wherein the acid is selected from acetic acid, benzoic acid, and boric acid. 5. The method for producing an aluminum foil for an electrolytic capacitor according to claim 1, wherein the aqueous solution has a pH of 5 to 9.
JP1037525A 1989-02-17 1989-02-17 Manufacture of aluminum foil for electrolytic capacitor Granted JPH02216811A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1037525A JPH02216811A (en) 1989-02-17 1989-02-17 Manufacture of aluminum foil for electrolytic capacitor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1037525A JPH02216811A (en) 1989-02-17 1989-02-17 Manufacture of aluminum foil for electrolytic capacitor

Publications (2)

Publication Number Publication Date
JPH02216811A JPH02216811A (en) 1990-08-29
JPH0566005B2 true JPH0566005B2 (en) 1993-09-20

Family

ID=12499958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1037525A Granted JPH02216811A (en) 1989-02-17 1989-02-17 Manufacture of aluminum foil for electrolytic capacitor

Country Status (1)

Country Link
JP (1) JPH02216811A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110073455A (en) * 2016-11-18 2019-07-30 日本轻金属株式会社 The manufacturing method of aluminium electrolutic capacitor electrode
TWI811289B (en) * 2018-03-16 2023-08-11 日商日本輕金屬股份有限公司 Manufacturing method of electrode for aluminum electrolytic capacitor

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06275473A (en) * 1993-03-19 1994-09-30 Matsushita Electric Ind Co Ltd Production of anode foil for aluminum electrolytic capacitor
JP2007053292A (en) * 2005-08-19 2007-03-01 Nichicon Corp Solid electrolytic capacitor and its manufacturing method
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

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110073455A (en) * 2016-11-18 2019-07-30 日本轻金属株式会社 The manufacturing method of aluminium electrolutic capacitor electrode
CN110073455B (en) * 2016-11-18 2021-03-19 日本轻金属株式会社 Manufacturing method of electrode for aluminum electrolytic capacitor
US11094472B2 (en) 2016-11-18 2021-08-17 Nippon Light Metal Company, Ltd. Method for producing electrode for aluminum electrolytic capacitor
TWI811289B (en) * 2018-03-16 2023-08-11 日商日本輕金屬股份有限公司 Manufacturing method of electrode for aluminum electrolytic capacitor

Also Published As

Publication number Publication date
JPH02216811A (en) 1990-08-29

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