JPH05195300A - Electrolytic treating device - Google Patents
Electrolytic treating deviceInfo
- Publication number
- JPH05195300A JPH05195300A JP3132292A JP3132292A JPH05195300A JP H05195300 A JPH05195300 A JP H05195300A JP 3132292 A JP3132292 A JP 3132292A JP 3132292 A JP3132292 A JP 3132292A JP H05195300 A JPH05195300 A JP H05195300A
- Authority
- JP
- Japan
- Prior art keywords
- electrolytic
- counter electrode
- liquid
- edge
- web
- 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.)
- Pending
Links
Landscapes
- Printing Plates And Materials Therefor (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、電解処理装置に関する
ものであり、金属ウエブの交番波形電流による粗面化及
び陽極酸化処理に適し、特に、オフセット印刷版用に粗
面化されたアルミニウム板からなる印刷版用支持体の電
解処理装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic treatment apparatus and is suitable for roughening and anodizing a metal web by an alternating waveform current, and in particular, an aluminum plate roughened for an offset printing plate. And an electrolytic treatment apparatus for a printing plate support.
【0002】[0002]
【従来の技術】印刷版用支持体、特に平版印刷版用支持
体としては、アルミニウム板が用いられ、ユーザーの多
様化から、アルミニウム板も、純アルミニウムに近いも
のから、マンガンを添加し、強度を上げたものまで多様
化している。そしてその様なアルミニウム板を、平版印
刷版用支持体として使用するためには、感光材料との適
度な接着性と保水性を有していることが必要である。こ
の為には、アルミニウム板の表面を均一且つ緻密な砂目
を有する様に粗面化しなければならない。この粗面化処
理は、実際に印刷を行った時、版材の汚れ性能などの印
刷性能に著しい影響を及ぼすので、その良否は版材製造
上重要な要素となっている。2. Description of the Related Art Aluminum plates are used as a support for printing plates, especially a support for lithographic printing plates. Due to the diversification of users, aluminum plates are similar to pure aluminum, and manganese has Have been diversified. In order to use such an aluminum plate as a support for a lithographic printing plate, it is necessary to have appropriate adhesiveness to a photosensitive material and water retention. For this purpose, the surface of the aluminum plate must be roughened so as to have uniform and fine grain. This roughening treatment has a significant influence on the printing performance such as the stain performance of the plate material when printing is actually performed, and therefore its quality is an important factor in plate material manufacture.
【0003】印刷版用アルミニウム支持体の粗面化方法
としては、機械的な砂目立て方法、電気化学的な砂目立
て方法などがあり、又それらを適時組合わせた形で粗面
化を行っている。機械的な砂目立て法としては、例えば
ボールグレイン,ワイヤーグレイン,ブラッシグレイ
ン,液体ホーニング法などがある。また電気化学的砂目
立て方法としては、交流電解エッチング方法が一般的に
採用されており、電流としては、普通の正弦波交流電
流、あるいは矩形波など特殊交番波形電流が用いられて
いる。またこの電気化学的砂目立ての前処理として、苛
性ソーダなどでエッチング処理をしても良い。その中で
交流電解エッチング方法においては、直流電流によって
生じる現象と異なり炭素や金属等による対極が非常に劣
化し易いという問題があった。例えば炭素を対極とする
と極性変化のたびに酸化還元の反応が繰り返され、バイ
ンダーの劣化が激しく長期間安定稼働が非常に難しい。As a roughening method for the aluminum support for printing plates, there are a mechanical graining method, an electrochemical graining method, and the like, and the roughening is performed by appropriately combining them. There is. Mechanical graining methods include, for example, ball grain, wire grain, brush grain, and liquid honing method. An alternating current electrolytic etching method is generally adopted as the electrochemical graining method, and a normal sine wave alternating current or a special alternating waveform current such as a rectangular wave is used as the current. Further, as a pretreatment for this electrochemical graining, etching treatment may be performed with caustic soda or the like. Among them, the AC electrolytic etching method has a problem that the counter electrode due to carbon, metal, etc. is very likely to deteriorate unlike the phenomenon caused by the DC current. For example, when carbon is used as the counter electrode, the redox reaction is repeated each time the polarity changes, and the deterioration of the binder is severe and stable operation for a long period of time is extremely difficult.
【0004】この様な課題に対して、特公昭61−48
596号公報には、主対極に接続された回路に補助対極
に対する回路を並列に連結すると共に、アノード電流の
主対極における流れを制御するためのダイオード又はダ
イオード的作用をなす機構を補助対極に対する回路に設
けたことを特徴とする電解処理装置が開示されている。
例えば第3図に示すように、被処理材である金属ウエブ
1がラジアルドラムローラ2の円周で支持され、対向す
る主対極3a,3bとの間の空間を、電解液供給口4か
ら金属イオンを含む電解処理液5を補給し電解液排出口
6から排出することによって満たし、電解液通路15と
する。主対極3a,3bには交流電源より交番波形電流
を供給して、電気化学的処理を施す電解処理装置であっ
て、金属ウエブ1との対極を主対極3a,3bと補助対
極8によって形成し、主対極3a,3bに接続された回
路に補助対極8に対する回路を並列に連結し、アノード
電流の主対極における回路を並列に連結し、アノード電
流の主対極における流れを制御するためのダイオード9
またはダイオード的作用をなす機構を補助対極8に対す
る回路に設けて電流を流す電解処理装置である。此の際
主対極3a,3bはお互いに反対の極性を持つもので、
交流電源7には互いに反対側に結線されており、更に主
対極3a,3bは夫々多数本の(例えばn=10〜14
本)の小電極(3a1 ,3a2 ,3a3 ・・・3an )
(3b1,3b2 ,3b3 ・・・3bn )がお互いに絶
縁体10を境として構成されたもので電流効率をあげる
ため工夫されている。To address such problems, Japanese Examined Patent Publication No. 61-48
No. 596, a circuit for the auxiliary counter electrode is connected to the circuit connected to the main counter electrode in parallel with the circuit for the auxiliary counter electrode, and a diode or a mechanism acting as a diode for controlling the flow of the anode current in the main counter electrode. There is disclosed an electrolytic treatment apparatus characterized by being provided in the.
For example, as shown in FIG. 3, a metal web 1 as a material to be treated is supported by the circumference of a radial drum roller 2, and a space between the opposing main counter electrodes 3a and 3b is connected to the metal from the electrolytic solution supply port 4 to form a space. The electrolytic solution 5 containing ions is replenished and discharged from the electrolytic solution discharge port 6 to fill it, thereby forming an electrolytic solution passage 15. An electrolytic treatment apparatus for supplying an alternating waveform current from an AC power source to the main counter electrodes 3a, 3b to perform an electrochemical treatment, in which the counter electrode with the metal web 1 is formed by the main counter electrodes 3a, 3b and the auxiliary counter electrode 8. , A circuit for connecting the auxiliary counter electrode 8 in parallel to the circuit connected to the main counter electrodes 3a, 3b, a circuit for connecting the anode current in the main counter electrode in parallel, and a diode 9 for controlling the flow of the anode current in the main counter electrode.
Alternatively, it is an electrolytic treatment apparatus in which a mechanism that acts as a diode is provided in the circuit for the auxiliary counter electrode 8 to flow an electric current. In this case, the main counter electrodes 3a and 3b have polarities opposite to each other,
The AC power supply 7 is connected to the opposite sides of each other, and the main counter electrodes 3a and 3b each have a large number (for example, n = 10 to 14).
Small electrodes of the) (3a 1, 3a 2, 3a 3 ··· 3a n)
(3b 1 , 3b 2 , 3b 3 ... 3b n ) are configured with the insulator 10 as a boundary, and are devised to improve current efficiency.
【0005】[0005]
【発明が解決しようとする課題】しかしながら、電解液
供給口4から補給された電解処理液5は、金属ウエブ1
と電極3a,3bとの間の狭い電解液通路15を通っ
て、ラジアルドラムローラ2の反対側に流れ、電解液排
出口6に出ていく間において、抵抗の少ないラジアルド
ラムローラの縁に向って金属ウエブの両縁部に流れがち
になり、それによってウエブの両縁部に処理が集中して
しまい、中央流路における電解液は液の流動が緩慢にな
り、電解によって電解処理液が次第に疲労して、かつ電
解液供給口4と電解液排出口6の間ではその成分に差が
できてきて、金属ウエブ巾方向処理が不均一になり、電
解処理装置全体として充分な電解効率が得られないとい
う問題点があった。また、電解液供給口4と電解液排出
口6の金属ウエブ近傍の温度差が大きくなり、所望の砂
目が得られなかった。特に電解液通路15中の金属ウエ
ブ1側の処理液では、電解液通路15の電極3a,3b
側の処理液との混合が不充分で、その成分の疲労の度合
い、及び温度の違いが著しく、砂目立ての不均一、即ち
電解品質の低下と電解効率の悪化を来す。従って金属ウ
エブ巾方向に均一且つ緻密な砂目を保ち、電解効率を上
げるために、電解液供給口4から供給する流量を増量す
る方法が行われたが、しかしながら供給液量を増量する
ことは、コストアップにつながるばかりでなく、流量を
増量しても充分なる所望の砂目は得られなかった。又、
上記の問題はラインの速度上昇に対応した電解処理長増
大時に於いて顕著になり、ラインの速度上昇の大きな制
約となっていた。However, the electrolytic treatment solution 5 replenished from the electrolytic solution supply port 4 is the metal web 1
It flows toward the opposite side of the radial drum roller 2 through the narrow electrolyte passage 15 between the electrode 3a and the electrodes 3a, 3b, and while flowing out to the electrolyte discharge port 6, toward the edge of the radial drum roller with low resistance. Tend to flow to both edges of the metal web, which concentrates the treatment on both edges of the web, slowing the flow of the electrolytic solution in the central flow path, and electrolysis causes the electrolytic solution to gradually disappear. As a result of fatigue, the components of the electrolytic solution supply port 4 and the electrolytic solution discharge port 6 are different from each other, the treatment in the width direction of the metal web becomes uneven, and sufficient electrolytic efficiency is obtained in the electrolytic treatment apparatus as a whole. There was a problem that I could not do it. Further, the temperature difference between the electrolytic solution supply port 4 and the electrolytic solution discharge port 6 in the vicinity of the metal web was large, and desired grain could not be obtained. In particular, in the treatment liquid on the metal web 1 side in the electrolyte passage 15, the electrodes 3a, 3b of the electrolyte passage 15 are treated.
Insufficient mixing with the treatment liquid on the side, the degree of fatigue of the components and the difference in temperature are significant, resulting in uneven graining, that is, deterioration of electrolytic quality and deterioration of electrolytic efficiency. Therefore, in order to maintain a uniform and dense grain in the width direction of the metal web and to increase the electrolysis efficiency, a method of increasing the flow rate supplied from the electrolytic solution supply port 4 has been carried out. Not only does this lead to an increase in cost, but even if the flow rate is increased, the desired desired grain size could not be obtained. or,
The above-mentioned problem becomes remarkable when the length of the electrolytic treatment corresponding to the increase in the speed of the line is increased, and it has been a great limitation on the increase in the speed of the line.
【0006】本発明の目的は、これら従来の問題点を解
消し、砂目立てが金属ウエブの巾方向に均一で且つ緻密
であり、電解効率の良い、そしてライン速度上昇に効果
的な電解処理装置を提供することにある。An object of the present invention is to solve these problems of the prior art and to provide an electrolytic treatment apparatus in which the graining is uniform and dense in the width direction of the metal web, the electrolytic efficiency is good, and the line speed is increased. To provide.
【0007】[0007]
【課題を解決するための手段及び作用】即ち、本発明の
上記目的は、金属イオンを含む電解処理液中で、金属ウ
エブと対極との間に交番波形電流を供給して該金属ウエ
ブに連続的に電気化学的処理を施す電解処理装置におい
て、前記金属ウエブの両縁部に対し、主対極側よりウエ
ブに対して複数個のエッジ給液ノズルを設けたことを特
徴とする電解処理装置によって達成される。本発明にお
いて、前記金属ウエブの両縁部に対し、主対極側よりウ
エブに対し複数個のエッジ給液ノズルを設けたというこ
とは、この複数個のエッジ給液ノズルから供給される液
がウエブ両縁部にカーテン膜を形成し、それがない場合
の中央部の液が両縁部に流れることを防ぐためのもので
ある。複数個のエッジ給液ノズルとしては主対極3a,
3bの数だけ設置されるのが好ましいが、供給ノズルよ
りの給液量が多い場合は最小個数として2ケ所であって
もかまはない。本発明における複数個のエッジ給液ノズ
ルより供給される電解液量により、金属ウエブ両縁部よ
り外側を流れる電解液が充分に補給され、流速も上昇し
且エッジ給液ノズルより吹出す液によってカーテン膜が
作られることもあって、電解液供給口より補給された電
解処理液はウエブ両縁部に流れることなく、金属ウエブ
幅全巾に亘って均一な流速で初めから終り迄流れること
になり、金属ウエブ表面は電解処理液の循環中の混合攪
拌により従来よりも新鮮な電解処理液に接触する機会が
多くなり、砂目も均一・緻密に、電解処理装置として電
解効率は上昇し、ライン速度の上昇を実施することが出
来る。That is, the above object of the present invention is to provide an alternating waveform current between a metal web and a counter electrode in an electrolytic treatment solution containing metal ions to continuously supply the metal web. In an electrolytic treatment apparatus for performing an electrochemical treatment, a plurality of edge liquid supply nozzles are provided on both edges of the metal web from the main counter electrode side to the web. To be achieved. In the present invention, a plurality of edge liquid supply nozzles are provided to the web from both sides of the main counter electrode on both edges of the metal web, which means that the liquid supplied from the plurality of edge liquid supply nozzles is not A curtain film is formed on both edges to prevent the liquid in the central portion from flowing to both edges when there is no curtain film. As a plurality of edge liquid supply nozzles, a main counter electrode 3a,
It is preferable to install the same number as 3b, but when the amount of liquid supplied from the supply nozzle is large, the minimum number may be two. By the amount of the electrolyte supplied from the plurality of edge supply nozzles in the present invention, the electrolyte flowing outside the both edges of the metal web is sufficiently replenished, the flow velocity is increased, and the liquid discharged from the edge supply nozzle is used. Since the curtain film is formed, the electrolytic treatment solution replenished from the electrolytic solution supply port does not flow to both edges of the web but flows from the beginning to the end at a uniform flow rate over the entire width of the metal web. The metal web surface has more opportunities to come into contact with a fresh electrolytic treatment solution than before due to the mixing and stirring during circulation of the electrolytic treatment solution, the grain is even and dense, and the electrolytic efficiency as an electrolytic treatment apparatus increases, It is possible to increase the line speed.
【0008】以下、図を用いて本発明の実施態様を説明
する。第1図は本発明の電解処理装置の一実施例であ
る。1は金属ウエブであり、2はウエブを支えるラジア
ルドラムローラであり。金属ウエブ1は主対極3a,3
b,及び補助対極8とのクリアランスを一定に保って走
行している。クリアランスは通常3〜50mm程度が適
当である。主対極と補助対極との比は求める電解エッチ
ング条件により異なる。7は交流電源であり、通常0.
1〜500Hzの交流電源が使用される。周波数につい
ては求めるエッチング形態によって変化させるが、周波
数が15Hz以下であると3a,3bの主対極の劣化が
大きく特にカーボンの場合顕著である。波形としては、
いろいろあるが、特公昭56−19280号,特公昭5
5−19191号各公報に記載の特殊交番波形を用いる
ことも出来る。9はダイオードであり、これにより、8
の補助対極に流れる電流を制御する。補助対極8の材料
としては、劣化に強い白金を用いることが好ましい。本
発明の電解液供給口としては、4を設けた。また、電解
処理液5は電解液供給口4内に入り、ディストリビュー
タ12を経てラジアルドラムローラ2の幅方向全体に均
一に分布するようキャビティ13内に入り、スリット1
4より電解液通路15の中に噴出される。図1ではエッ
ジ給液ノズル16a,16bをそれぞれ主対極3a,3
b毎に設けたが、エッジ給液ノズルの数としては2ケ所
以上あれば良く、エッジ給液ノズルの位置及び構造も丸
型管に限定されるものではなく、四角でも細長いもので
もよい。但しエッジ給液ノズルのセンターの位置は金属
ウエブ両縁より50mm内側が好ましい。要は、エッジ
給液ノズルを設けることによって、電解処理液液が中央
部より両縁部に流れることを防ぐことにある。これら、
エッジ給液ノズルを2ケ所以上複数ケ設けてカーテン膜
を作り、且つラジアルドラムの両縁部の液流を満たすこ
とにより、電解液供給口よりの処理液の巾全体におい
て、自然混合・攪拌による電解液濃度・温度の均一化、
金属ウエブと接触する電解処理液の濃度・温度の均一化
が可能となり、それによって砂目の均一化,緻密化が可
能となり、電解効率が上昇し、そしてライン速度の上昇
が可能となるのである。An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 shows an embodiment of the electrolytic treatment apparatus of the present invention. Reference numeral 1 is a metal web, and 2 is a radial drum roller that supports the web. The metal web 1 has main counter electrodes 3a, 3
The vehicle is traveling while maintaining a constant clearance between b and the auxiliary counter electrode 8. A clearance of 3 to 50 mm is usually suitable. The ratio of the main counter electrode and the auxiliary counter electrode differs depending on the electrolytic etching conditions to be obtained. 7 is an AC power supply, which is normally 0.
An AC power supply of 1 to 500 Hz is used. The frequency is changed depending on the etching pattern to be obtained, but if the frequency is 15 Hz or less, the main counter electrodes 3a and 3b are greatly deteriorated, particularly in the case of carbon. As a waveform,
There are various types, but Japanese Patent Publication Nos. 56-19280 and 5
It is also possible to use the special alternating waveform described in each publication of 5-19191. 9 is a diode, which allows
Controls the current flowing through the auxiliary counter electrode. As the material of the auxiliary counter electrode 8, it is preferable to use platinum, which is resistant to deterioration. 4 was provided as the electrolytic solution supply port of the present invention. Further, the electrolytic treatment liquid 5 enters the electrolytic solution supply port 4, passes through the distributor 12, enters the cavity 13 so as to be uniformly distributed in the entire width direction of the radial drum roller 2, and the slit 1
4 is ejected into the electrolyte passage 15. In FIG. 1, the edge liquid supply nozzles 16a and 16b are connected to the main counter electrodes 3a and 3 respectively.
Although it is provided for each b, the number of edge liquid supply nozzles may be two or more, and the position and structure of the edge liquid supply nozzles are not limited to the round tube, and may be square or elongated. However, the center position of the edge liquid supply nozzle is preferably 50 mm inside from both edges of the metal web. The point is to prevent the electrolytically treated liquid solution from flowing from the central portion to both edge portions by providing the edge liquid supply nozzle. these,
By providing a plurality of edge liquid supply nozzles at two or more locations to form a curtain film and filling the liquid flow at both edges of the radial drum, the entire width of the processing liquid from the electrolytic solution supply port can be naturally mixed and stirred. Uniform electrolyte concentration and temperature,
It is possible to make the concentration and temperature of the electrolytic treatment liquid that comes into contact with the metal web uniform, which makes it possible to make the sand uniform and densified, increasing the electrolysis efficiency and increasing the line speed. ..
【0009】[0009]
(実施例−1)図1のような装置を用いて、電解液供給
口4より1500l/min,エッジ給液ノズル16a
又は16bより100l/min×9ケ所、電解処理液
を合計2400l/minを供給し、電解液排出口6か
ら電解処理液を排出した。この時の条件は 主対極 : カーボン 補助対極 : 白金 ウエブとその対極のクリアランス: 10mm 主対極の電解処理液条件 : 処理液 硝酸 濃度 50g/l 温度 60℃ 補助対極の電解処理液条件 : 処理液 硝酸 濃度 50g/l 温度 20℃ ウエブ幅 : 1000mm 処理速度 : 15m/min 周波数 : 100Hz であった。以上の条
件で砂目立てを行ったところ、入口硝酸濃度50g/l
に対し、金属ウエブ近傍での出口硝酸濃度は40g/l
を示し、入口温度60℃に対し出口における金属ウエブ
近傍での温度は62℃であり、均一且つ緻密な砂目立て
が可能であり、電解効率が上昇した。又、陽極酸化処理
においても同様の効果が得られた。(Embodiment 1) Using an apparatus as shown in FIG. 1, 1500 l / min from the electrolytic solution supply port 4, edge liquid supply nozzle 16a
Alternatively, a total of 2400 l / min of the electrolytic treatment solution was supplied from 16b at 100 l / min × 9 places, and the electrolytic treatment solution was discharged from the electrolytic solution discharge port 6. The conditions at this time are: Main counter electrode: Carbon auxiliary counter electrode: Platinum web and its counter electrode clearance: 10 mm Main counter electrode electrolytic treatment liquid condition: Treatment liquid nitric acid concentration 50 g / l Temperature 60 ° C Auxiliary electrode electrolytic treatment liquid condition: Treatment liquid nitric acid The concentration was 50 g / l, the temperature was 20 ° C., the web width was 1000 mm, the processing speed was 15 m / min, and the frequency was 100 Hz. When graining was performed under the above conditions, the concentration of nitric acid at the inlet was 50 g / l
In contrast, the outlet nitric acid concentration near the metal web was 40 g / l.
The temperature in the vicinity of the metal web at the outlet was 62 ° C. while the inlet temperature was 60 ° C., and uniform and fine graining was possible, and the electrolysis efficiency was increased. The same effect was obtained in the anodizing treatment.
【0010】(比較例−1)図3の装置を用いて、実施
例−1と同じ条件で処理を行った。その時の電解処理液
の供給量は2400l/minが限界であり、入口硝酸
濃度50g/lが電解処理液の均一な混合が出来ないた
め、出口における金属ウエブ近傍の硝酸濃度が40g/
lに低下し、同じく温度は60℃であったものが出口に
おける金属ウエブ近傍の温度では68℃を示し、その為
砂目も不均一な不合格製品となった。(Comparative Example-1) Using the apparatus shown in FIG. 3, processing was performed under the same conditions as in Example-1. At that time, the supply amount of the electrolytic treatment solution is limited to 2400 l / min, and the nitric acid concentration of 50 g / l at the inlet makes it impossible to uniformly mix the electrolytic treatment liquid.
However, the temperature was 60 ° C., but the temperature in the vicinity of the metal web at the outlet was 68 ° C. Therefore, the grain was also a non-uniform rejected product.
【0011】[0011]
【発明の効果】上記実施例から明らかなように、本発明
の主対極にエッジ給液ノズルを複数ケ所以上設けること
により、電解処理液の濃度・温度を入口と出口とを近づ
けることが可能となり、その結果砂目の均一性,緻密性
が保たれ、電解効率が上昇し、生産スピードの向上が可
能となり品質向上並びに製品コストの低減に大きく貢献
した。As is apparent from the above embodiments, by providing the main counter electrode of the present invention with a plurality of edge feed nozzles, it is possible to bring the concentration and temperature of the electrolytic treatment solution closer to the inlet and the outlet. As a result, the uniformity and the denseness of the grain are maintained, the electrolysis efficiency is increased, and the production speed can be improved, which greatly contributes to quality improvement and product cost reduction.
【図1】本発明の電解処理装置の一実施例の側面断面図FIG. 1 is a side sectional view of an embodiment of an electrolytic treatment apparatus of the present invention.
【図2】本発明の電解処理装置の図1の正面断面図FIG. 2 is a front sectional view of the electrolytic treatment apparatus of the present invention shown in FIG.
【図3】従来の電解処理装置の一例の側面断面図FIG. 3 is a side sectional view of an example of a conventional electrolytic treatment apparatus.
1 金属ウエブ 2 ラジアルドラムローラ 3a,3b 主対極 4 電解液供給口 5 電解処理液 6 電解液排出口 7 交流電源 8 補助対極 9 ダイオード 10 絶縁体 11 供給管 12 ディストリビュータ 13 キャビティ 14 スリット 15 電解液通路 16a,16b エッジ給液ノズル 1 Metal Web 2 Radial Drum Rollers 3a, 3b Main Counter Electrode 4 Electrolyte Supply Port 5 Electrolysis Solution 6 Electrolyte Discharge Port 7 AC Power Supply 8 Auxiliary Counter Electrode 9 Diode 10 Insulator 11 Supply Pipe 12 Distributor 13 Cavity 14 Slit 15 Electrolyte Passage 16a, 16b Edge liquid supply nozzle
Claims (1)
ウエブと対極との間に交番波形電流を供給して該金属ウ
エブに連続的に電気化学的処理を施す電解処理装置にお
いて、前記金属ウエブの両縁部に対し、主対極側よりウ
エブに対して複数個のエッジ給液ノズルを設けたことを
特徴とする電解処理装置。1. An electrolytic treatment apparatus for supplying an alternating waveform current between a metal web and a counter electrode in an electrolytic treatment liquid containing metal ions to continuously electrochemically treat the metal web, An electrolytic treatment apparatus characterized in that a plurality of edge liquid supply nozzles are provided to the web from both sides of the main counter electrode on both edges of the web.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3132292A JPH05195300A (en) | 1992-01-23 | 1992-01-23 | Electrolytic treating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3132292A JPH05195300A (en) | 1992-01-23 | 1992-01-23 | Electrolytic treating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05195300A true JPH05195300A (en) | 1993-08-03 |
Family
ID=12328033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3132292A Pending JPH05195300A (en) | 1992-01-23 | 1992-01-23 | Electrolytic treating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05195300A (en) |
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