JPH0748461B2 - Aluminum electrode foil for electrolytic capacitor and manufacturing method thereof - Google Patents

Aluminum electrode foil for electrolytic capacitor and manufacturing method thereof

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Publication number
JPH0748461B2
JPH0748461B2 JP1246391A JP24639189A JPH0748461B2 JP H0748461 B2 JPH0748461 B2 JP H0748461B2 JP 1246391 A JP1246391 A JP 1246391A JP 24639189 A JP24639189 A JP 24639189A JP H0748461 B2 JPH0748461 B2 JP H0748461B2
Authority
JP
Japan
Prior art keywords
corrosion
foil
electrode foil
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 - Fee Related
Application number
JP1246391A
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Japanese (ja)
Other versions
JPH03109711A (en
Inventor
香 柿堺
雅信 清水
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.)
Japan Capacitor Industrial Co Ltd
Original Assignee
Japan Capacitor Industrial Co Ltd
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Application filed by Japan Capacitor Industrial Co Ltd filed Critical Japan Capacitor Industrial Co Ltd
Priority to JP1246391A priority Critical patent/JPH0748461B2/en
Publication of JPH03109711A publication Critical patent/JPH03109711A/en
Publication of JPH0748461B2 publication Critical patent/JPH0748461B2/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、特にコンデンサの素子巻きにおける芯部の巻
き回し強度の向上をはかった電解コンデンサ用アルミニ
ウム電極箔及びその製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an aluminum electrode foil for an electrolytic capacitor, in which the winding strength of a core portion of an element winding of a capacitor is improved, and a manufacturing method thereof.

従来の技術 一般に電解コンデンサ用アルミニウム電極箔は、その有
効表面積を拡大する目的で通常、電解エッチングと化学
エッチングが夫々単独あるいは組合わせで行われ、その
際、アルミニウム電極箔の両面は同じエッチング条件の
もとで処理されるのが普通である。
2. Description of the Related Art Generally, an aluminum electrode foil for an electrolytic capacitor is generally subjected to electrolytic etching and chemical etching individually or in combination for the purpose of expanding its effective surface area. It is usually processed at the source.

ところがアルミニウム電極箔の有効表面積を拡大しよう
とするには、エッチングによる腐食量を増大しなければ
ならないが、腐食量を増大するときは箔の物理的強度の
低下をまねき、したがって有効表面積を拡大しながら箔
の強度を維持するために、従来は箔の表面にエッチング
されない線条または帯状の非腐食部分を形成するなどの
方法が提案されている。
However, in order to increase the effective surface area of the aluminum electrode foil, the amount of corrosion due to etching must be increased, but when the amount of corrosion is increased, the physical strength of the foil is reduced, and therefore the effective surface area is increased. However, in order to maintain the strength of the foil, conventionally, there has been proposed a method of forming a non-etched line-shaped or strip-shaped non-corroded portion on the surface of the foil.

発明が解決しようとする課題 しかしながら、線条または帯状の非腐食部分を設けるこ
とは、それ丈有効面積の拡大を妨げるという欠陥を有
し、また有効表面積を拡大するときは箔の物理的強度が
低下するので、化成して使用する場合もろくなって折れ
やすく、そのため、コンデンサ素子の巻き芯部に巻く段
階で、その巻き芯部の直径を太くして巻き回す曲率半径
を大きくする必要があるが、巻き芯部の直径を太くする
ときは、コンデンサ素子の中心部に無駄な空間が生じ
て、静電容量に対するコンデンサの体積効率が低くなる
という不都合を有し、従って従来のエッチング方法によ
り、有効面積の拡大と物理的強度の保持という相反する
作用を同時に解決することは極めて困難であった。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention However, providing a strip-shaped or strip-shaped non-corrosive portion has a defect that it impedes the expansion of the length effective area, and when expanding the effective surface area, the physical strength of the foil is Since it lowers, it becomes fragile and easily broken when it is used after forming it.Therefore, at the stage of winding it around the winding core of the capacitor element, it is necessary to increase the diameter of the winding core to increase the radius of curvature for winding. However, when the diameter of the winding core portion is increased, there is a disadvantage that a space is wasted in the central portion of the capacitor element, and the volumetric efficiency of the capacitor with respect to the electrostatic capacity is lowered. Therefore, the conventional etching method is effective. It was extremely difficult to solve the contradictory effects of increasing the area and maintaining the physical strength at the same time.

そこで本発明は、上記した従来の困難な問題を解決する
ことを目的としたものである。
Then, this invention aims at solving the above-mentioned conventional difficult problems.

問題を解決するための手段 従来アルミニウム電極箔は、箔の両面とも同じ条件のも
とでエッチング処理を行っており、従って誤差があると
しても、両面の腐食量及び腐食の形状は同等で、どちら
の面を内側にしてコンデンサ素子の巻き芯部に巻き回し
ても物理的強度に差は生じない。
Means for Solving the Problem Conventional aluminum electrode foils are etched under the same conditions on both sides of the foil. Therefore, even if there is an error, the amount of corrosion and the shape of corrosion on both sides are the same. There is no difference in the physical strength even if it is wound around the winding core of the capacitor element with the surface of the inside being the inside.

ところが、電極箔は、そのいづれか一方の面が必ず内側
となって、コンデンサ素子の巻き芯部に巻き回されるも
のであるから、一方の面を内側にしたときの巻き回し強
度さえ強ければ、それと反対側の面を内側にしたときの
巻き回し強度が弱くても問題にならないこと、そしても
しどちらか一方の面を内側にしたときだけ巻き回し強度
が向上するならば、電極箔の腐食の形状は両面で異なる
はずであることに注目し、発明者は、電極箔の腐食の形
状が両面で異なる数次の実験を重ねた。即ちアルミニウ
ム箔の表面から内側への腐食の程度は、エッチングの温
度、電流密度及び電気量などに大きく依存するので、そ
れらを単独で変えたり、あるいは適宜組合わせを行い、
またアルミニウム箔面から内部へ向かう腐食の形状が両
面で異なるように別々に設計して、片面づつ異なった条
件で夫々エッチング処理するなどの実験を重ねた結果、
両面の腐食深さを同等にし、かつ、両面の腐食減量を異
ならしめた電極箔では、腐食減量の少ない一方の面を内
側にして巻き回しを行ったときその強度が両面を同じよ
うにエッチング処理し、かつ得られる静電容量を等しく
した場合の電極箔よりも強くなることを見出した。
However, since either one of the electrode foils is always on the inside and is wound around the winding core of the capacitor element, as long as the winding strength when one surface is on the inside is strong, It does not matter if the winding strength is weak when the opposite side is the inside, and if the winding strength is improved only when one side is the inside, corrosion of the electrode foil Noting that the shape should be different on both sides, the inventor has conducted several experiments in which the shape of corrosion of the electrode foil is different on both sides. That is, the degree of corrosion from the surface of the aluminum foil to the inside depends largely on the etching temperature, the current density, the amount of electricity, etc., so these can be changed independently or appropriately combined,
Also, as a result of repeated experiments such as designing separately so that the shape of corrosion going from the aluminum foil surface to the inside is different on both sides, and performing etching treatment under different conditions on each side,
With electrode foils that have the same corrosion depth on both sides and different corrosion weights on both sides, the strength is the same when both sides are wound with one side with less corrosion weight inside being wound. However, it was found that it becomes stronger than the electrode foil when the obtained electrostatic capacitances are equal.

また表裏で腐食深さ、腐食減量を同等にし、表裏の腐食
形状を変えた箔では、その形状の組合わせにより、ある
特定の面を内側にして巻き回しを行なったときその強度
が両面を同じようにエッチング処理し、かつ得られる静
電容量を等しくした場合の電極箔よりも強くなることを
見出した。
In the case of foils with the same corrosion depth and corrosion weight on the front and back and different corrosion shapes on the front and back, the strength is the same on both sides when a certain surface is wound inside due to the combination of the shapes. It was found that it is stronger than the electrode foil in the case of performing the etching treatment and making the obtained capacitances equal.

第1図は、腐食減量の重量比に対する静電容量と、巻き
回し強度との関係をエッチピットがトンネル状の中高圧
用の電極箔について示したもので、一方の縦軸に静電容
量(μF/cm2)を、他方の縦軸に、電極箔の強度を表す
ために、電極箔を折損することなく巻き回しできる金属
棒の最小の直径(mm)を夫々示し、かつ横軸に、表裏の
腐食減量の比を示しており、第1図から明らかなよう
に、両面の腐食減量の重量比が1:1.01未満においては腐
食減量の少ないほうの面を内側にして巻き回すときの強
度に、はっきりとした改善が認められず、またこの重量
比が1:1.40を越えると、両面を同等にエッチングした電
極箔と比べ静電容量の低下が顕著であり、従って静電容
量対比で巻き回し強度が改善されるのはエッチング箔の
両面の腐食減量の重量比が1:1.01ないし1:1.40の範囲で
あることが判明した。
FIG. 1 shows the relationship between the capacitance with respect to the weight ratio of corrosion weight loss and the winding strength for an electrode foil for medium and high pressure in which the etch pit has a tunnel shape. μF / cm 2 ), on the other vertical axis, the minimum diameter (mm) of the metal rod that can be wound without breaking the electrode foil to express the strength of the electrode foil is shown, and on the horizontal axis, The ratio of corrosion weight loss on the front and back sides is shown. As is clear from Fig. 1, when the weight ratio of corrosion weight loss on both sides is less than 1: 1.01, the strength when wound with the side with less corrosion weight loss inside However, when the weight ratio exceeds 1: 1.40, there is a marked decrease in capacitance compared to the electrode foil with both sides equally etched. The turning strength is improved when the weight ratio of corrosion weight loss on both sides of the etching foil is 1: It was found to be in the range 1.01 to 1: 1.40.

また両面の腐食深さを同等にし、かつ、両面の腐食減量
も同等にし、一方の面と他方の面の腐食形状を異ならし
めたものでは、表裏の形状の組合わせによって、巻き回
しに対して強い面がかわってくることも判明した。
Also, in the case where the corrosion depth on both sides is the same, the weight loss on both sides is also the same, and the corrosion shapes on one side and the other side are different, the combination of the front and back shapes It turned out that the strong side was changing.

上記において、両面の腐食深さを同等にし、かつ、一方
の面の腐食減量が他方の面の腐食減量と相異なる電極箔
のエッチング方法としては、前段で電極箔を一般的な塩
化物溶液中でエッチングを行い、次いで、後段のエッチ
ングを電解で行う場合には、片面づつ異なった電気量で
電解することによって両面の腐食減量に差を設ける。こ
の場合,電流密度と電解時間を両面で夫々独立に設定し
て両面を別々に電解してもよく、また、両面とも同じ電
解時間をとり、電流密度のみ変えて電解してもよく、上
記の方法によりエッチング処理した場合両面の電気量の
比が1:1.01以下では巻き回し強度にはっきりとした改善
は認められず、またその比が1:5.0より大きくなると、
一方の面の腐食が過度となって静電容量が低下するか、
または一方の面の腐食が足りないため静電容量が増加し
ない結果となり、従って静電容量比で巻き回し強度が改
善されるのは、後段エッチングの両面の電気量の比が1:
1.01乃至1:5.0の範囲である。
In the above, the same depth of corrosion on both sides, and as an electrode foil etching method in which the corrosion weight loss of one surface is different from the corrosion weight loss of the other surface, the electrode foil in a general chloride solution in the previous stage. In the case where the etching is carried out at 1, and then the subsequent etching is carried out by electrolysis, the difference in the corrosion weight loss on both sides is provided by electrolyzing with different amount of electricity on each side. In this case, the current density and the electrolysis time may be set independently on both sides to electrolyze both sides separately, or the same electrolysis time may be taken on both sides and only the current density may be changed to perform electrolysis. When etching by the method, the ratio of the amount of electricity on both sides is 1: 1.01 or less, no clear improvement in the winding strength is observed, and when the ratio is greater than 1: 5.0,
If one side is excessively corroded and the capacitance decreases,
Alternatively, one side of the surface is not corroded enough, so that the electrostatic capacity does not increase.Therefore, the winding strength is improved by the electrostatic capacity ratio when the ratio of the electric quantities of the two surfaces in the latter etching is 1:
The range is from 1.01 to 1: 5.0.

また電極箔を一般的な塩化物溶液中で前段のエッチング
を行ってから後段をケミカルエッチングする場合には、
片面づつ別々に処理し、処理時間に差をつけ両面の腐食
減量を相異ならしめる。この場合ケミカルエッチングの
処理時間の比が1:1.01以下では巻き回しにはっきりした
改善は認められず、またその比が1:5.0より大きいと一
方の面の腐食減量が大き過ぎて静電容量が低下したり、
または一方の面の腐食減量が少な過ぎて、静電容量が増
加しない結果となり、従って静電容量対比で巻き回し強
度が改善されるのは、後段のケミカルエッチングの処理
時間の比が1:1.01ないし1:5.0の範囲である。また表裏
の処理時間に差をつける方法の他に、表裏の処理液温度
に差をつける方法、表裏の処理液組成を代える方法によ
っても表裏の腐食減量を相異ならしめることが可能であ
る。
When the electrode foil is etched in a general chloride solution and then the latter is chemically etched,
Treat one side separately and make a difference in treatment time to make the weight loss on both sides different. In this case, when the ratio of the chemical etching treatment time is 1: 1.01 or less, no clear improvement is observed in the winding, and when the ratio is greater than 1: 5.0, the corrosion weight loss on one side is too large and the electrostatic capacitance becomes large. Or
Alternatively, the corrosion loss on one side is too small, and the capacitance does not increase.Therefore, the reason why the winding strength is improved in comparison with the capacitance is that the processing time ratio of the subsequent chemical etching is 1: 1.01. To 1: 5.0. Further, in addition to the method of making a difference in the processing time of the front and back, the method of making a difference in the temperature of the processing liquid of the front and the back and the method of changing the composition of the processing liquid of the front and the back can also make the corrosion weight loss of the front and the back different.

また、アルミニウム箔にピットを発生せしめにる前段
と、この前段で発生せしめたピットを必要充分な太さに
まで拡大する後段の2段エッチングにおいて、前段で一
方の面と他方の面の腐食電気量に差をつけ、かつ、前段
と後段での腐食電気量の総和が等しくなるように後段に
おいてもそれぞれの面の腐食電気量に差をつけることに
より、両面での腐食形状を異ならしめることも可能であ
る。
Also, in the two-stage etching of the former stage where the pits are generated in the aluminum foil and the latter stage where the pits generated in the former stage are enlarged to a necessary and sufficient thickness, the corrosion electric power of one surface and the other surface is It is also possible to make the corrosion shapes on both sides different by differentiating the amount of corrosion and by differentiating the amount of corrosion electricity on each surface in the latter stage as well so that the total amount of corrosion electricity in the former stage and the latter stage are equal. It is possible.

この場合においても前段での腐食電気量の比を1:1.01な
いし1:5.0とするとき、後段での腐食電気量の比を1.01:
1ないし5.0:1として両面での腐食電気量の総和を同等に
することが好ましく、上記の範囲よりも小さいときは、
巻き回し強度の改善は認められず、また上記の範囲より
大きいときは、過度に大きいピットが低密度に形成され
て静電容量が低下する。
Even in this case, when the ratio of the amount of corrosive electricity in the former stage is 1: 1.01 to 1: 5.0, the ratio of the amount of corrosive electricity in the latter stage is 1.01:
It is preferable to make the total amount of corrosion electricity on both sides equal as 1 to 5.0: 1, and when smaller than the above range,
No improvement in the winding strength is observed, and when it is larger than the above range, excessively large pits are formed at a low density and the capacitance is lowered.

実施例 〔実施例1〕 エッチングピットがトンネル状の中高圧用の電極箔の場
合、 純度99.99%、厚さ104μmのアルミニウム箔の軟質材を
用い、一般的な塩化物溶液中で前段のエッチングをした
後、後記の表1に示すエッチング条件のもとでアルミニ
ウム箔のA面及びB面を夫々個別に直流エッチングを行
い、次いで水洗して乾燥し、375Vの通常行われる化成を
行った。化成後、箔の圧延方向と平行に幅10mm、長さ20
mmの試験片を抜き取り、これを表面の平滑な金属棒にか
け、試験片の両端をそろえて、毎秒1.5Kgの割合で荷重
を漸増させながら引張った。最初は直径6.0mmの金属棒
を用い、そのときの試験片の破断時の荷重が1Kg以上あ
る場合は、金属棒を直径0.5mm小さいものに交換し、こ
のようにして順次金属棒の直径を0.5mmきざみで細くし
て測定を繰り返し、最も細い金属棒の直径をもってアル
ミニウム電極箔の巻き回し強度の指標とし、その結果を
表1に示した。なお、表1では、腐食の多い方の面をA
面、少ない方の面をB面として示している。
Example [Example 1] In the case of an electrode foil for medium- and high-pressure tunnels having etching pits, a soft material made of aluminum foil having a purity of 99.99% and a thickness of 104 µm was used, and the preceding etching was performed in a general chloride solution. After that, the aluminum foil was subjected to direct current etching under the etching conditions shown in Table 1 below, respectively, and then the aluminum foil was washed with water and dried to carry out the usual 375V chemical conversion. After chemical formation, width 10 mm and length 20 parallel to the rolling direction of the foil
A mm test piece was taken out, this was put on a metal rod having a smooth surface, both ends of the test piece were aligned and pulled while gradually increasing the load at a rate of 1.5 kg per second. Initially, use a metal rod with a diameter of 6.0 mm, and if the load at break of the test piece at that time is 1 kg or more, replace the metal rod with one with a diameter of 0.5 mm smaller, and in this way gradually change the diameter of the metal rod. The measurement was repeated by thinning in 0.5 mm increments, and the diameter of the thinnest metal rod was used as an index of the winding strength of the aluminum electrode foil. The results are shown in Table 1. In Table 1, the side with the most corrosion is A
The surface and the smaller surface are shown as the B surface.

また第2図は、上記実施例1によりエッチング処理した
電極箔の断面図を示している。
Further, FIG. 2 shows a sectional view of the electrode foil which has been subjected to the etching treatment according to the above-mentioned Example 1.

表1によれば、腐食の多い方のA面を外側にしたとき、
直径3.0mmまでの金属棒に耐え、両面を同一のエッチン
グ条件のもとでエッチング処理した従来例のものに比し
3ランクの箔強度の向上がはかられた。
According to Table 1, when the A-side of the one with much corrosion is placed outside,
It withstands metal rods up to 3.0 mm in diameter, and is able to improve the foil strength by three ranks as compared with the conventional example in which both sides are etched under the same etching conditions.

〔実施例2〕 エッチングピットがトンネル状の中高圧用の電極箔の場
合、 純度99.99%、厚さ104μmのアルミニウム箔の軟質材を
用い、一般的な塩化物溶液中で前段のエッチングを行っ
た後後記の表2に示すエッチング条件のもとでアルミニ
ウム箔のA面及びB面を夫々個別にケミカルエッチング
を行い、次いで水洗して乾燥し、375Vの通常行われる化
成を行い実施例1と同様の測定を行った。
[Example 2] When the etching pit was an electrode foil for medium- and high-pressure tunnels, a soft material of aluminum foil having a purity of 99.99% and a thickness of 104 µm was used, and the previous etching was performed in a general chloride solution. Under the etching conditions shown in Table 2 below, the A-side and the B-side of the aluminum foil were individually subjected to chemical etching, followed by washing with water and drying, followed by chemical conversion at 375 V, which was normally performed, and the same as Example 1. Was measured.

表2によれば、腐食の多い方のA面を外側にしたとき、
直径3.0mmまでの金属棒に耐え、両面を同一のエッチン
グ条件のもとでエッチング処理した従来例のものに比し
3ランクの箔強度の向上が図られた。
According to Table 2, when the A side of the one with much corrosion is placed outside,
Withstanding metal rods up to 3.0 mm in diameter, the foil strength was improved by 3 ranks as compared with the conventional example in which both surfaces were etched under the same etching conditions.

〔実施例3〕 エッチングピットがトンネル状の中高圧用の電極箔の場
合、 純度99.99%、厚さ104μmのアルミニウム箔の軟質材を
用い、一般的な塩化物溶液中で後記の表3に示すエッチ
ング条件のもとで、即ち前段におけるA面に対する腐食
電気量とB面に対する腐食電気量及び後段におけるA面
に対する腐食電気量とB面に対する腐食電気量とにそれ
ぞれ差を設けると共に、前段と後段におけるA面に対す
る腐食電気量の総和とB面に対する腐食電気量の総和と
が等しくなるようにアルミニウム箔のA面及びB面を夫
々別個に直流エッチングを行った後、水洗して乾燥し、
375Vの通常行われる化成を行い、実施例1と同様の測定
を行った。
[Example 3] In the case of an intermediate- and high-pressure electrode foil having a tunnel-shaped etching pit, a soft material of aluminum foil having a purity of 99.99% and a thickness of 104 µm was used and shown in Table 3 below in a general chloride solution. Under the etching conditions, that is, the amounts of corrosive electricity to the surface A and B in the previous stage and the amounts of electrical charge to the surface A and B in the subsequent stage are made different from each other, and the front and rear stages are different from each other. In order to make the total amount of corrosive electricity to the A surface and the total amount of corrosive electricity to the B surface in (3) are equal, the A surface and the B surface of the aluminum foil are separately subjected to direct current etching, washed with water and dried,
The usual chemical conversion of 375V was performed, and the same measurement as in Example 1 was performed.

表3によれば前段で腐食の多い方のB面を内側にしたと
き、直径3.0mmまでの金属棒に耐え、両面を同一のエッ
チング条件のもとでエッチング処理した従来例のものに
比し3ランクの箔強度の向上がはかられた。なお第3は
実施例3によりエッチング処理した電極箔の断面図で、
腐食深さ、腐食減量が両面で等しく、形状のみが相違し
ている状態を示している。
According to Table 3, when the B side, which is more corroded in the previous stage, is set inside, it withstands metal rods with a diameter of up to 3.0 mm, and compared with the conventional example in which both sides were etched under the same etching conditions. The foil strength of the 3rd rank was improved. The third is a cross-sectional view of the electrode foil etched according to Example 3,
Corrosion depth and weight loss are the same on both sides, but only the shape is different.

〔実施例4〕 低圧用の電極箔の場合、 純度99.9%、厚さ90μmのアルミニウム箔の軟質材を用
い、一般的な塩化物溶液中で後記の表4に示すエッチン
グ条件のもとで交流エッチングを行った後、水洗して乾
燥し、20Vの通常行われる化成を行った。化成後、実施
例1と同様に箔強度の試験を行ないその結果を表4に示
した。
[Example 4] In the case of an electrode foil for low voltage, a soft material of aluminum foil having a purity of 99.9% and a thickness of 90 µm was used, and an alternating current was applied in a general chloride solution under the etching conditions shown in Table 4 below. After etching, it was washed with water, dried, and subjected to the usual chemical conversion of 20V. After the chemical conversion, the foil strength test was conducted in the same manner as in Example 1, and the results are shown in Table 4.

表4によれば、腐食の多い方のA面を外側にしたとき、
直径0.5mmまでの金属棒に耐え、両面を同一のエッチン
グ条件のもとでエッチング処理した従来のものに比し、
1ランクの箔強度の向上がはかられた。
According to Table 4, when the A side of the one with much corrosion is placed outside,
It withstands metal rods up to 0.5 mm in diameter, compared to the conventional one that has been etched on both sides under the same etching conditions.
The foil strength of 1 rank was improved.

発明の効果 本発明による電解コンデンサ用のアルミニウム電極箔に
よれば、電極箔の両面を同様のエッチング条件のもとで
エッチング処理した従来の電極箔と比べ、電極箔を巻き
回してコンデンサ素子を作る際の巻き芯部の巻き回し強
度が著しく改善されて、素子巻きにおける箔の切断事故
を軽減することができ、従って電極箔の歩留まりの向上
及び素子巻きの作業性の向上をはかることができ、コス
トダウンが得られるという利点を有し、また、コンデン
サ素子の巻き芯部の直径を細くすることができるため、
静電容量に対するコンデンサの体積効率が高まり、コン
デンサの小型化に有効であるなどの利点を有する。
EFFECTS OF THE INVENTION According to the aluminum electrode foil for electrolytic capacitors of the present invention, the electrode foil is wound to form a capacitor element as compared with the conventional electrode foil in which both surfaces of the electrode foil are etched under the same etching conditions. When the winding strength of the winding core portion is significantly improved, it is possible to reduce a foil cutting accident in the element winding, and thus it is possible to improve the yield of the electrode foil and the workability of the element winding. It has the advantage of cost reduction, and since the diameter of the winding core of the capacitor element can be reduced,
The volume efficiency of the capacitor with respect to the electrostatic capacity is increased, and it is effective in miniaturizing the capacitor.

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

第1図は腐食減量の重量比に対する巻き回し強度の指
標、及び静電容量の関係を示す図、第2図は、表裏の腐
食減量の相違を示すエッチング箔の断面図、第3図は、
表裏での腐食形状の相違を示すエッチング箔の断面図で
ある。
FIG. 1 is a diagram showing a relationship between an index of a winding strength and a capacitance with respect to a weight ratio of corrosion weight loss, FIG. 2 is a sectional view of an etching foil showing a difference in corrosion weight loss between front and back, and FIG.
It is sectional drawing of the etching foil which shows the difference of the corrosion shape on the front and back.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】アルミニウムエッチング箔において、両面
の腐食深さを同等にし、かつ、一方の面の腐食の形状と
他方の面の腐食の形状とを異ならしめたことを特徴とす
る電解コンデンサ用アルミニウム電極箔。
1. Aluminum for electrolytic capacitors, characterized in that in an aluminum etching foil, the corrosion depths on both sides are made equal, and the shape of corrosion on one surface and the shape of corrosion on the other surface are made different. Electrode foil.
【請求項2】一方の面の腐食減量が他方の面の腐食減量
と相異なりその重量比が1:1.01ないし1:1.40であること
を特徴とする請求項1記載の電解コンデンサ用アルミニ
ウム電極箔。
2. The aluminum electrode foil for an electrolytic capacitor according to claim 1, wherein the weight loss of corrosion on one surface is different from the weight loss of corrosion on the other surface, and the weight ratio is 1: 1.01 to 1: 1.40. .
【請求項3】両面の腐食減量を同等にしたことを特徴と
する請求項1記載の電解コンデンサ用アルミニウム電極
箔。
3. The aluminum electrode foil for an electrolytic capacitor according to claim 1, wherein both sides have the same corrosion weight loss.
【請求項4】アルミニウム箔を、前段と後段で2段エッ
チングする電解コンデンサ用アルミニウム電極箔の製造
方法において、後段の電解エッチングにおける一方の面
の腐食電気量と、他方の面の腐食電気量との比を、1:1.
01ないし1:5.0としたことを特徴とする電解コンデンサ
用アルミニウム電極箔の製造方法。
4. A method of manufacturing an aluminum electrode foil for an electrolytic capacitor, wherein an aluminum foil is etched in two stages, a front stage and a rear stage, and a corrosive electricity amount on one surface and a corrosive electricity amount on the other surface in the latter electrolytic etching. The ratio of 1: 1.
A method for manufacturing an aluminum electrode foil for an electrolytic capacitor, characterized in that it is 01 to 1: 5.0.
【請求項5】アルミニウム箔を、前段と後段で2段エッ
チングする電解コンデンサ用アルミニウム電極箔の製造
方法において、後段のケミカルエッチングにおける一方
の面の腐食時間と他方の面の腐食時間との比を1:1.01な
いし1:5.0としたことを特徴とする電解コンデンサ用ア
ルミニウム電極箔の製造方法。
5. A method for producing an aluminum electrode foil for an electrolytic capacitor, comprising the steps of etching an aluminum foil in two stages, a front stage and a rear stage, wherein the ratio of the corrosion time on one surface to the corrosion time on the other surface in the chemical etching in the latter step is calculated. A method for manufacturing an aluminum electrode foil for an electrolytic capacitor, characterized in that the ratio is 1: 1.01 to 1: 5.0.
【請求項6】アルミニウム箔を、前段と後段で2段エッ
チングする電解コンデンサ用アルミニウム電極箔の製造
方法において、前段の電解エッチングにおける一方の面
の腐食電気量と他方の面の腐食電気量との比を1:1.01な
いし1:5.0とし、かつ、後段の電解エッチングにおける
一方の面の腐食電気量と他方の面の腐食電気量とに差を
設けて両面の腐食電気量の総和を等しくしたことを特徴
とする電解コンデンサ用アルミニウム電極箔の製造方
法。
6. A method for producing an aluminum electrode foil for an electrolytic capacitor, comprising the steps of etching an aluminum foil in two stages, a front stage and a rear stage. The ratio is 1: 1.01 to 1: 5.0, and the total amount of corrosive electricity on both sides is made equal by providing a difference between the amount of corrosive electricity on one surface and the amount of corrosive electricity on the other surface in the subsequent electrolytic etching. A method for producing an aluminum electrode foil for an electrolytic capacitor, which comprises:
JP1246391A 1989-09-25 1989-09-25 Aluminum electrode foil for electrolytic capacitor and manufacturing method thereof Expired - Fee Related JPH0748461B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1246391A JPH0748461B2 (en) 1989-09-25 1989-09-25 Aluminum electrode foil for electrolytic capacitor and manufacturing method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1246391A JPH0748461B2 (en) 1989-09-25 1989-09-25 Aluminum electrode foil for electrolytic capacitor and manufacturing method thereof

Publications (2)

Publication Number Publication Date
JPH03109711A JPH03109711A (en) 1991-05-09
JPH0748461B2 true JPH0748461B2 (en) 1995-05-24

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ID=17147831

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Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH0748461B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5584890A (en) * 1995-01-24 1996-12-17 Macfarlane; Douglas R. Methods of making multiple anode capacitors
WO1998014969A1 (en) * 1996-10-02 1998-04-09 Telectronics Pacing Systems, Inc. Multiple anode capacitors and methods of making the same
CN120660161A (en) * 2023-01-30 2025-09-16 松下知识产权经营株式会社 Electrode foil for electrolytic capacitor, and method for manufacturing electrode foil for electrolytic capacitor

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5853817A (en) * 1981-09-26 1983-03-30 エルナ−株式会社 Method of producing electrode foil for electrolytic condenser

Also Published As

Publication number Publication date
JPH03109711A (en) 1991-05-09

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