JPH0337855B2 - - Google Patents
Info
- Publication number
- JPH0337855B2 JPH0337855B2 JP15655385A JP15655385A JPH0337855B2 JP H0337855 B2 JPH0337855 B2 JP H0337855B2 JP 15655385 A JP15655385 A JP 15655385A JP 15655385 A JP15655385 A JP 15655385A JP H0337855 B2 JPH0337855 B2 JP H0337855B2
- Authority
- JP
- Japan
- Prior art keywords
- foil
- oxide film
- phosphoric acid
- etching
- aluminum
- 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
Links
- 239000011888 foil Substances 0.000 claims description 42
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 23
- 229910052782 aluminium Inorganic materials 0.000 claims description 23
- 239000003990 capacitor Substances 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 20
- 238000005530 etching Methods 0.000 claims description 19
- 239000000126 substance Substances 0.000 claims description 13
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 239000007864 aqueous solution Substances 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 3
- 239000012670 alkaline solution Substances 0.000 claims description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 49
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 25
- 238000004090 dissolution Methods 0.000 description 13
- 238000010438 heat treatment Methods 0.000 description 12
- 238000011282 treatment Methods 0.000 description 9
- 238000010306 acid treatment Methods 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 8
- 230000006866 deterioration Effects 0.000 description 8
- 239000000243 solution Substances 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000002131 composite material Substances 0.000 description 5
- 150000001805 chlorine compounds Chemical class 0.000 description 4
- 239000003792 electrolyte Substances 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 description 2
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 239000004327 boric acid Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 235000019837 monoammonium phosphate Nutrition 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 239000003929 acidic solution Substances 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- 238000007743 anodising Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000006166 lysate Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 235000011007 phosphoric acid Nutrition 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 238000007788 roughening Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- ing And Chemical Polishing (AREA)
Description
[発明の技術分野]
本発明はアルミニウム電解コンデンサの製造工
程においてエツチングしたアルミニウム箔に良質
な酸化皮膜を形成してコンデンサ性能の劣化を防
止し得るようにしたアルミニウム電解コンデンサ
用電極箔の製造方法に関する。
[発明の技術的背景とその問題点]
一般に、アルミニウム電解コンデンサに使用さ
れる陽極側電極箔は、アルミニウム箔の表面を粗
面化して表面積を拡大するエツチング工程と、エ
ツチング箔を陽極酸化して表面に酸化皮膜を形成
する化成工程を経て製造されている。
エツチング工程で製造されるエツチング箔は、
アルミニウム箔を、塩化物を含む水溶液中で電気
化学的に溶解して粗面化し、次に塩化物を除去す
るために純水で洗浄し最後に乾燥を行つて製造さ
れる。この時、洗浄の効果を上げるために、硝
酸、硼酸又はリン酸等の水溶液による洗浄が並用
されることもある。この製造過程において、粗面
化された直後のアルミニウム箔の表面は非常に活
性化されており、洗浄工程及び乾燥工程で、洗浄
水や空気中の酸素と反応してアルミニウムの水和
皮膜やアルミニウムの空気酸化皮膜(以下自然酸
化皮膜という)を表面に形成する。この自然酸化
皮膜は、ひげ状又は多孔質の層で、弱い絶縁性を
示し、化学的に弱い性質を有している。
又、化成工程は前記エツチング箔を硼酸、リン
酸又は有機酸等による電解液中で陽極酸化するこ
とにより、箔表面に酸化アルミニウム(Al2O3)
よりなる障壁層を形成する。この場合、化成で形
成される酸化皮膜の厚みは印加された化成電圧か
ら自然酸化皮膜の耐圧分を差し引いた電圧に相当
するものとなり、自然酸化皮膜は上層に残り、複
合酸化皮膜を形成する。このため、特に低い電圧
で化成された酸化皮膜においては、皮膜全体に占
める自然酸化皮膜の割合ほ大きなものとなる。
ところで、従来の電極箔の製造方法によると、
エツチング箔表面に形成される自然酸化皮膜につ
いて何らの処理もされていなかつたために、その
後の化成工程を経て形成される複合酸化皮膜の上
層部は化学的に弱く溶解し易い性質を有した自然
酸化皮膜からなつている。そのため、この様な電
極箔がコンデンサに使用されるとき、コンデンサ
内部の駆動用電解液と反応して上層の自然酸化膜
が溶解されるので、耐電圧が低くなり電解コンデ
ンサの漏れ電流を増加させる原因となつている。
特に、低い電圧で化成された皮膜については、
自然酸化皮膜の占める割合が高い為に、漏れ電流
の増加が大きなものとなつていた。
[発明の目的]
本発明の目的は上述した点にかんがみ、エツチ
ングされたアルミニウム箔の表面に良質な酸化皮
膜を形成することによつて、電解コンデンサの劣
化特性の改良、特に漏れ電流の増加を小さくする
ことが可能なアルミニウム電解コンデンサ用電極
箔の製造方法を提供することである。
[発明の概要]
本発明は、エツチング工程を経たアルミニウム
箔を、リン酸を含む水溶液に浸漬することによつ
てリン酸を吸着させ、次に熱処理を行つて箔表面
にリン酸を含む熱酸化皮膜を形成する。次に、酸
又はアルカリ溶液で処理し溶解され易い酸化皮膜
の一部を溶解して除去することにより、表面に溶
解しにくいリン酸を含む熱酸化皮膜を有したエツ
チング箔を得る。しかし後に、通常の化成処理を
行うことにより、上層に溶解しにくい皮膜部分を
有した複合酸化皮膜を形成させるものである。
[発明の実施例]
本発明に係るアルミニウム電解コンデンサ用電
極箔の製造方法を概略的に説明する。
先ず、アルミニウム箔は塩化物を含んだ水溶液
中で粗面化される(エツチング工程)。
次に、塩化物が純水等で除去される(洗浄工
程)
次に、リン酸、リン酸アンモニウム又はリン酸
カリウム等のリン酸を含む溶液に浸漬することに
より、エツチング箔表面にリン酸を吸着させる
(リン酸処理工程)。このリン酸処理工程において
塩化物の除去を同時に兼ねる事ができるので、上
記洗浄工程で洗浄液としてリン酸水溶液を使用す
れば洗浄工程に代えてリン酸処理工程とすること
も可能である。
その後、150℃〜600℃の炉中を通すことによつ
て、エツチング箔表面にリン酸を含む熱酸化皮膜
を形成させる(熱処理工程)。このとき、エツチ
ング箔表面には、熱処理工程により形成されたリ
ン酸を含む溶解しにくい良質の酸化皮膜と、熱処
理工程以前から存在している溶解し易い弱い皮膜
とが形成されている。即ち、リン酸を含む熱酸化
皮膜は電解コンデンサの駆動用電解液に対して溶
解しない安定した特性を持つている。
しかし、この熱処理において表面のすべてが良
質な熱酸化皮膜で覆われるわけではなくエツチン
グ工程から存在する弱い皮膜も含まれている。
次に、上記エツチング箔を、クエン酸、シユウ
酸、リン酸、硝酸又は硫酸等の酸性溶液、或はア
ンモニア水又は水酸化ナトリウム等のアルカリ性
溶液に浸漬し、溶解し易い弱い皮膜を溶解除去す
る(以下溶解工程という)。こうすることによつ
て、箔表面に溶解しにくい良質の皮膜のみを残留
させる。溶解液は純水で洗浄する。
次に、上記のようにして表面に溶解しにくい皮
膜が形成されているエツチング箔を、化成電解液
中で陽極酸化することにより酸化皮膜を形成する
(化成工程)。この時形成される酸化皮膜は、上層
に溶解しにくい皮膜部分を有した複合酸化皮膜と
なる。この複合酸化皮膜はコンデンサの電解液に
対しても反応の少ないものとなり、電極箔がコン
デンサに組み立てられた場合に性能劣化の少ない
コンデンサを製造することができる。
以上述べた工程の内、リン酸処理工程、熱処理
工程及び溶解工程における各条件を変えた場合の
実施例を表1に示す。
[Technical Field of the Invention] The present invention relates to a method for manufacturing an electrode foil for an aluminum electrolytic capacitor, which prevents deterioration of capacitor performance by forming a high-quality oxide film on an etched aluminum foil during the manufacturing process of the aluminum electrolytic capacitor. . [Technical background of the invention and its problems] In general, the anode side electrode foil used in aluminum electrolytic capacitors is produced by an etching process that roughens the surface of the aluminum foil to increase its surface area, and an anodizing process of the etching foil. It is manufactured through a chemical conversion process that forms an oxide film on the surface. The etching foil produced in the etching process is
It is produced by electrochemically dissolving aluminum foil in an aqueous solution containing chlorides to roughen the surface, then washing with pure water to remove the chlorides, and finally drying. At this time, in order to increase the cleaning effect, cleaning with an aqueous solution such as nitric acid, boric acid, or phosphoric acid may also be used. In this manufacturing process, the surface of the aluminum foil immediately after roughening is highly activated, and during the cleaning and drying processes, it reacts with the cleaning water and oxygen in the air, forming a hydrated film on the aluminum. An air oxide film (hereinafter referred to as natural oxide film) is formed on the surface. This natural oxide film is a whisker-like or porous layer, exhibits weak insulation, and has chemically weak properties. In addition, in the chemical conversion step, the etching foil is anodized in an electrolytic solution using boric acid, phosphoric acid, or an organic acid, so that aluminum oxide (Al 2 O 3 ) is formed on the foil surface.
Form a barrier layer consisting of: In this case, the thickness of the oxide film formed by chemical formation corresponds to the voltage obtained by subtracting the withstand voltage of the natural oxide film from the applied chemical formation voltage, and the natural oxide film remains in the upper layer, forming a composite oxide film. Therefore, especially in an oxide film formed at a low voltage, the ratio of the natural oxide film to the entire film becomes larger. By the way, according to the conventional method of manufacturing electrode foil,
Since the natural oxide film formed on the surface of the etching foil had not been subjected to any treatment, the upper layer of the composite oxide film formed through the subsequent chemical conversion process was a natural oxide film that was chemically weak and easily dissolved. It consists of a membrane. Therefore, when such electrode foil is used in a capacitor, it reacts with the driving electrolyte inside the capacitor and dissolves the upper natural oxide film, lowering the withstand voltage and increasing the leakage current of the electrolytic capacitor. It is the cause. In particular, for films chemically formed at low voltage,
Due to the high proportion of the natural oxide film, the leakage current increased significantly. [Object of the Invention] In view of the above-mentioned points, the object of the present invention is to improve the deterioration characteristics of electrolytic capacitors, particularly to reduce the increase in leakage current, by forming a high-quality oxide film on the surface of etched aluminum foil. An object of the present invention is to provide a method for manufacturing an electrode foil for an aluminum electrolytic capacitor that can be made small. [Summary of the Invention] The present invention involves immersing an aluminum foil that has undergone an etching process in an aqueous solution containing phosphoric acid to adsorb phosphoric acid, and then heat-treating the foil to form a thermal oxidation layer containing phosphoric acid on the surface of the foil. Forms a film. Next, by treating with an acid or alkaline solution to dissolve and remove a portion of the easily soluble oxide film, an etched foil having a thermal oxide film containing phosphoric acid that is difficult to dissolve on the surface is obtained. However, by subsequently performing a normal chemical conversion treatment, a composite oxide film having a film portion that is difficult to dissolve is formed in the upper layer. [Embodiments of the Invention] A method for manufacturing an electrode foil for an aluminum electrolytic capacitor according to the present invention will be schematically explained. First, the aluminum foil is roughened in an aqueous solution containing chloride (etching step). Next, chlorides are removed with pure water, etc. (cleaning step) Next, phosphoric acid is applied to the surface of the etching foil by immersing it in a solution containing phosphoric acid, such as phosphoric acid, ammonium phosphate, or potassium phosphate. Adsorb (phosphoric acid treatment step). This phosphoric acid treatment step can also serve as the removal of chlorides at the same time, so if a phosphoric acid aqueous solution is used as the cleaning liquid in the cleaning step, the phosphoric acid treatment step can be used instead of the cleaning step. Thereafter, a thermal oxide film containing phosphoric acid is formed on the surface of the etching foil by passing it through a furnace at 150°C to 600°C (heat treatment step). At this time, on the surface of the etching foil, there are formed a high quality oxide film containing phosphoric acid which is formed by the heat treatment process and which is difficult to dissolve, and a weak film which is easily soluble and which has existed before the heat treatment process. That is, the thermal oxide film containing phosphoric acid has a stable property of not being dissolved in the driving electrolyte of the electrolytic capacitor. However, in this heat treatment, not all of the surface is covered with a high-quality thermal oxide film, and a weak film that is present from the etching process is also included. Next, the etching foil is immersed in an acidic solution such as citric acid, oxalic acid, phosphoric acid, nitric acid, or sulfuric acid, or an alkaline solution such as aqueous ammonia or sodium hydroxide to dissolve and remove the easily soluble film. (hereinafter referred to as the dissolution process). By doing this, only a high-quality film that is difficult to dissolve remains on the foil surface. Wash the solution with pure water. Next, the etching foil, on which a film that is difficult to dissolve is formed on the surface as described above, is anodized in a chemical electrolyte to form an oxide film (chemical conversion step). The oxide film formed at this time becomes a composite oxide film having a film portion that is difficult to dissolve in the upper layer. This composite oxide film has less reaction to the electrolyte of the capacitor, and when the electrode foil is assembled into the capacitor, it is possible to manufacture a capacitor with less deterioration in performance. Table 1 shows examples in which the conditions in the phosphoric acid treatment step, heat treatment step, and dissolution step among the steps described above were changed.
【表】
実施例1〜5は、エツチングされ純水で洗浄さ
れたアルミニウム箔を表1に示すリン酸処理条件
でリン酸処理した後、表1に示す熱処理条件で熱
処理を行ない、続いて表1に示す溶解条件で溶解
処理を行つた後、純水で洗浄して溶解液を除去し
た後乾燥した。又、比較例として前記3つの処理
の内1つを除いた場合を、さらに従来例として3
つの処理をいずれも行つていない場合をそれぞれ
示した。
次に、表1の条件で処理したそれぞれの箔を、
何れも0.1%リン酸二水素アンモニウム水溶液中
で15Vの化成電圧で化成処理を行つた。
次に、これらの電極箔を使用し、セパレータ紙
を介在させて陰極箔と共に巻回し、電解液を含浸
した後、アルミニウムケースにパツキング材を用
いて封入することにより、実施例1〜5、比較例
1〜3および従来例に対応した定格電圧10V、定
格容量470μFのアルミニウム電解コンデンサを製
作した。
以上のように製作されたコンデンサの漏れ電流
を測定し、製作後の漏れ電流を初期値とし、その
後無負荷の状態で85℃、500時間放置した後の漏
れ電流値を比較して表2に示した。[Table] In Examples 1 to 5, aluminum foil that had been etched and washed with pure water was treated with phosphoric acid under the phosphoric acid treatment conditions shown in Table 1, and then heat treated under the heat treatment conditions shown in Table 1. After performing the dissolution treatment under the dissolution conditions shown in 1, the solution was washed with pure water to remove the solution, and then dried. In addition, as a comparative example, a case in which one of the three processes mentioned above is excluded, and as a conventional example, three
The cases in which none of the two treatments are performed are shown. Next, each foil treated under the conditions in Table 1 was
In both cases, chemical conversion treatment was performed in a 0.1% aqueous ammonium dihydrogen phosphate solution at a formation voltage of 15V. Next, these electrode foils were wound together with a cathode foil with a separator paper interposed between them, impregnated with an electrolytic solution, and then sealed in an aluminum case using a packing material. Aluminum electrolytic capacitors with a rated voltage of 10 V and a rated capacity of 470 μF corresponding to Examples 1 to 3 and the conventional example were manufactured. The leakage current of the capacitor fabricated as described above was measured, and the leakage current after fabrication was taken as the initial value, and the leakage current values after being left at 85°C for 500 hours in an unloaded state were compared and shown in Table 2. Indicated.
【表】
表2に示されるように、本発明に係るリン酸処
理工程、熱処理工程及び溶解工程を加えた各実施
例1〜5は、従来例および比較例1〜3に比べ
て、85℃、500時間放置後の漏れ電流が小さく抑
えられている。従つて、上記リン酸処理工程、熱
処理工程及び溶解工程を行うことによつて、漏れ
電流劣化を小さく抑え得る良質な酸化皮膜を形成
することができると言える。
次に、熱処理工程後の溶解工程において溶解時
間と漏れ電流の関係を試験した結果を図に示す。
この試験は、エツチング箔を0.5%リン酸水溶
液に浸漬後、500℃で1分間の熱処理を行ない、
続いて1%水酸化ナトリウム水溶液25℃中に浸漬
して溶解処理を行つた。その後、溶解液は洗浄除
去した。この場合、溶解処理を行わなかつたサン
プルと、溶解処理を0.5、1、2、4、6分の各
時間について行つたサンプルを作成した。そし
て、各サンプルについて0.1%リン酸二水素アン
モニウム水溶液中で電圧15Vの化成を行つた後、
各電極箔を用いて定格電圧10V、定格容量470μF
のアルミニウム電解コンデンサを製造し、85℃、
500時間無負荷放置後の漏れ電流を測定した。
図から分かるように、溶解処理を行つてないサ
ンプルでは漏れ電流劣化が大きく、溶解時間が1
〜3分では弱い皮膜部分が溶解して除かれ劣化が
小さくなつている。しかし、更に溶解時間を長く
すると溶解しにくい酸化皮膜も溶解して無くなり
劣化が増大する。一般的に、最適溶解時間は熱処
理工程で生成した熱酸化皮膜の量と、溶解液の種
類、濃度、温度によつて決められる。
尚、エツチング箔にリン酸処理を行うリン酸処
理工程、熱処理を行つて熱酸化皮膜を形成する熱
処理工程及び皮膜の一部を溶解させる溶解工程
は、エツチング工程と化成工程との間で時間的に
連続した工程として行うこともでき、又それぞれ
の工程が或は1つの工程が時間的に離れて行われ
ても、同様の効果を得ることができる。
[発明の効果]
以上述べたように本発明によれば、エツチング
されたアルミニウム箔の表面に良質な酸化皮膜を
形成することができ、漏れ電流劣化の少ないアル
ミニウム電解コンデンサを実現できる。[Table] As shown in Table 2, each of Examples 1 to 5 in which a phosphoric acid treatment step, a heat treatment step, and a dissolution step according to the present invention were added was more effective at 85°C than in the conventional example and Comparative Examples 1 to 3. , the leakage current after being left for 500 hours is kept small. Therefore, it can be said that by performing the above-mentioned phosphoric acid treatment step, heat treatment step, and melting step, a high-quality oxide film that can suppress leakage current deterioration can be formed. Next, the results of testing the relationship between melting time and leakage current in the melting step after the heat treatment step are shown in the figure. In this test, the etching foil was immersed in a 0.5% phosphoric acid aqueous solution and then heat-treated at 500℃ for 1 minute.
Subsequently, it was immersed in a 1% aqueous sodium hydroxide solution at 25°C for dissolution treatment. Thereafter, the lysate was washed away. In this case, samples were prepared in which the dissolution treatment was not performed and the samples were subjected to the dissolution treatment for each time of 0.5, 1, 2, 4, and 6 minutes. Then, after performing chemical conversion on each sample in a 0.1% ammonium dihydrogen phosphate aqueous solution at a voltage of 15V,
Rated voltage 10V, rated capacity 470μF using each electrode foil
We manufacture aluminum electrolytic capacitors at 85℃,
Leakage current was measured after being left unloaded for 500 hours. As can be seen from the figure, leakage current deterioration is large in samples that have not been subjected to dissolution treatment, and the dissolution time is 1.
At ~3 minutes, the weak film portion was dissolved and removed, and the deterioration was reduced. However, if the dissolution time is further increased, the oxide film that is difficult to dissolve will also dissolve and disappear, resulting in increased deterioration. Generally, the optimum dissolution time is determined by the amount of thermal oxide film produced in the heat treatment process, and the type, concentration, and temperature of the dissolving solution. It should be noted that the phosphoric acid treatment step in which the etching foil is treated with phosphoric acid, the heat treatment step in which a thermal oxide film is formed by heat treatment, and the dissolution step in which a part of the film is melted are separated in time between the etching step and the chemical conversion step. The same effect can be obtained even if these steps are performed as consecutive steps, or even if each step or one step is performed separately in time. [Effects of the Invention] As described above, according to the present invention, a high-quality oxide film can be formed on the surface of an etched aluminum foil, and an aluminum electrolytic capacitor with less deterioration due to leakage current can be realized.
図は本発明における溶解工程の溶解時間を変え
て製造されるアルミニウム電解コンデンサの85
℃、500時間放置後の漏れ電流を測定した結果を
示すグラフである。
The figure shows 85 aluminum electrolytic capacitors manufactured by changing the melting time of the melting process in the present invention.
3 is a graph showing the results of measuring leakage current after being left at ℃ for 500 hours.
Claims (1)
と、次にエツチング箔の表面に酸化皮膜を形成す
る化成工程より成るアルミニウム電解コンデンサ
用電極箔の製造方法において、前記化成工程の前
に、エツチング箔をリン酸を含む水溶液中で処理
する工程と、次に高温にて処理を行なつて箔表面
に熱酸化皮膜を形成する工程と、次に酸又はアル
カリ溶液にて処理し前記熱酸化皮膜の一部を残留
させる工程とを設けたことを特徴とするアルミニ
ウム電解コンデンサ用電極箔の製造方法。1. In a method for manufacturing an electrode foil for an aluminum electrolytic capacitor, which comprises an etching process to roughen the surface of the aluminum foil, and a chemical conversion process to form an oxide film on the surface of the etched foil, the etching foil is rinsed before the chemical conversion process. A step of treating in an aqueous solution containing an acid, then a step of treating at high temperature to form a thermal oxide film on the foil surface, and then a step of treating with an acid or alkaline solution to form a part of the thermal oxide film. 1. A method for manufacturing an electrode foil for an aluminum electrolytic capacitor, comprising a step of leaving a residue.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15655385A JPS6217185A (en) | 1985-07-15 | 1985-07-15 | Production of electrode foil for aluminum electrolytic capacitor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15655385A JPS6217185A (en) | 1985-07-15 | 1985-07-15 | Production of electrode foil for aluminum electrolytic capacitor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6217185A JPS6217185A (en) | 1987-01-26 |
| JPH0337855B2 true JPH0337855B2 (en) | 1991-06-06 |
Family
ID=15630310
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15655385A Granted JPS6217185A (en) | 1985-07-15 | 1985-07-15 | Production of electrode foil for aluminum electrolytic capacitor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6217185A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2631488B2 (en) * | 1988-02-23 | 1997-07-16 | 三菱アルミニウム株式会社 | Electrolytic capacitor electrode foil |
| JP3313133B2 (en) * | 1992-02-26 | 2002-08-12 | ニチコン株式会社 | Manufacturing method of cathode foil for electrolytic capacitor |
| US6452784B2 (en) | 2000-05-31 | 2002-09-17 | Matsushita Electric Industrial Co., Ltd. | Aluminum electrolytic capacitor and method for producing the same |
| US6507480B2 (en) | 2001-02-26 | 2003-01-14 | Matsushita Electric Industrial Co., Ltd. | Electric double layer capacitor |
-
1985
- 1985-07-15 JP JP15655385A patent/JPS6217185A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6217185A (en) | 1987-01-26 |
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|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |