JPH02240299A - Electrolytically treating device - Google Patents

Electrolytically treating device

Info

Publication number
JPH02240299A
JPH02240299A JP5802889A JP5802889A JPH02240299A JP H02240299 A JPH02240299 A JP H02240299A JP 5802889 A JP5802889 A JP 5802889A JP 5802889 A JP5802889 A JP 5802889A JP H02240299 A JPH02240299 A JP H02240299A
Authority
JP
Japan
Prior art keywords
liquid
web
electrolytic
counter electrode
counter electrodes
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
Application number
JP5802889A
Other languages
Japanese (ja)
Inventor
Nagayoshi Kaneko
修芳 金子
Tsutomu Kakei
掛井 勤
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.)
Fujifilm Holdings Corp
Original Assignee
Fuji Photo Film 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 Fuji Photo Film Co Ltd filed Critical Fuji Photo Film Co Ltd
Priority to JP5802889A priority Critical patent/JPH02240299A/en
Publication of JPH02240299A publication Critical patent/JPH02240299A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain an electrolytically treating device capable of making sand dressing uniform and dense and of enhancing electrolysis efficiency by supplying the electrolytic treating liquid contg. metallic ions between a metallic web and the counter electrodes and providing one or a plurality of means for agitating this electrolytic treating liquid in the passage of the electrolyte. CONSTITUTION:A metallic web 1 is traveled along a radial drum roller 2 while holding the clearances against both the main counter electrodes 3a, 3b and an auxiliary counter electrode 8 constant. Alternating wave-form current is allowed to flow between the main counter electrodes 3a, 3b and the auxiliary counter electrode 8 from an AC power source 7 and electrochemical treatment is performed for the web 1. In the meantime, jetted liquid is sent to a cavity 13 via a feed pipe 12 from a jetted liquid feeder 11 provided to the insulator 10 part of the boundary between the counter electrodes 3a, 3b and ejected into the passage 15 of electrolyte through the slits 14. The spent electrolytic treating liquid 5 near to the web 1 is agitated and mixed with the fresher treating liquid 5 in the counter electrodes 3a, 3b sides opposed thereto by this jetted liquid. Thereby the web 1 is brought into contact with fresh treating liquid 5 than in the conventional practice and quality of sand dressing is made more uniform and electrolysis efficiency is enhanced.

Description

【発明の詳細な説明】 (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、金属ウェ
ブの交番波形電流による粗面化に適し、特に1.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
刷版支持体の電解処理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to an electrolytic treatment apparatus, which is suitable for roughening a metal web using an alternating waveform current, and is particularly suitable for 1. roughening for offset printing plates. This invention relates to an apparatus for electrolytic treatment of a printing plate support made of aluminum plate.

〔従来の技術〕[Conventional technology]

印刷版支持体、特に平版印刷版支持体としては、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。
Aluminum plates are used as printing plate supports, especially lithographic printing plate supports. Due to the diversification of users, aluminum plates have diversified from those close to pure aluminum to those with manganese added to increase strength. ing.

そしてその様なアルミニウム板を、平版印刷版支持体と
して使用するためには、感光材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。
In order to use such an aluminum plate as a lithographic printing plate support, it is necessary to have appropriate adhesion to the photosensitive material and water retention.

この為には、アルミニウム板の表面を均−且つ緻密な砂
目を有する樟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
造と重要な要素となっている。
In order to do this, the surface of the aluminum plate must be roughened to have a uniform and finely grained surface. Since it has a significant effect on printing performance, its quality is an important factor in plate material production.

印刷版用アルミニウム支持体の粗面化方法としては、機
械的な砂目立て法、電気化学的な砂目立て法などがあり
、又それらを適時組合わせた形で粗面化を行っている。
Methods for roughening the surface of aluminum supports for printing plates include mechanical graining, electrochemical graining, and the like, and surface roughening is carried out by appropriately combining these methods.

機械的な砂目立て法としては、例えばポールグレイン、
ワイヤーダレイン、ブラッシグレイン。
Mechanical graining methods include, for example, pole graining,
Wire dalein, brush grain.

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、交流電解エツチング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
たこの電気化学的処理立ての前処理として、苛性ソーダ
などでエツチング処理をしても良い。
There is a liquid honing method. Furthermore, as an electrochemical graining method, an alternating current electrolytic etching method is generally employed, and the current used is a normal sinusoidal alternating current or a special alternating waveform current such as a rectangular wave. Further, as a pretreatment before this electrochemical treatment, etching treatment with caustic soda or the like may be performed.

その中で交流電解エツ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0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。
Among these, the AC electrolytic etching method has a problem in that, unlike the phenomenon caused by DC current, the counter electrode made of carbon or metal is extremely susceptible to deterioration.For example, if carbon is used as the counter electrode, an oxidation-reduction reaction occurs every time the polarity changes. This is repeated and the binder deteriorates rapidly, making stable operation over a long period of time extremely difficult.

この様な課題に対して、特公昭61−48596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ェブ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′a、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
ウェブ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’<8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。
To solve this problem, Japanese Patent Publication No. 61-48596 discloses that a circuit for an auxiliary counter electrode is connected in parallel to a circuit connected to a main counter electrode, and a diode is installed to control the flow of anode current in the main counter electrode. Alternatively, an electrolytic treatment apparatus is disclosed in which a mechanism acting like a diode is provided in a circuit for an auxiliary counter electrode. For example, as shown in FIG. 3, a metal web 1, which is a material to be treated, is supported around the circumference of a radial drum roller 2, and a main counter electrode 3a facing
. The main counter electrodes 3a, 3b are supplied with an alternating waveform current from an alternating current power source to perform electrochemical treatment. , a circuit for the auxiliary counter electrode 8 is connected in parallel to the circuit connected to the main counter electrodes 3a and 3b, and a circuit for the anode current at the main counter electrode is connected in parallel to control the flow of the anode current at the main counter electrode. This is an electrolytic treatment apparatus in which a diode 9 or a mechanism acting like a diode is provided in the circuit for the auxiliary counter electrode 8 to flow current.

此の際1対113a、3bはお互いに反対の極性をもつ
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1対i3a、3bは夫々多数本の(例えばn=1
0〜14本)の小電極(3a3at+  31s  ・
・・38a)(3b+、3bt。
In this case, the pairs 113a and 3b have opposite polarities and are connected to the AC power source 7 on opposite sides, and each pair i3a and 3b has a large number of wires (for example, n=1).
0 to 14) small electrodes (3a3at+31s・
...38a) (3b+, 3bt.

3bs  ・・・3b、)がお互いに絶縁体lO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。
3bs...3b,) are configured with an insulator lO as a boundary, and are devised to increase current efficiency.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

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、金属ウェブ1、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に出ていくので、流路におけ
る電解によって電解処理液が次第に疲労して、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、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。
However, the electrolytic treatment liquid 5 replenished from the electrolyte supply port 4 flows to the opposite side of the radial drum roller 2 through a narrow electrolyte passage 15 between the metal web 1 and the electrodes 3a, 3b, and the electrolyte As it exits to the discharge port 6, the electrolytic treatment solution gradually becomes fatigued due to electrolysis in the flow path, and a difference in the components develops between the electrolyte supply port 4 and the electrolyte discharge port 6, causing damage to the entire electrolytic treatment apparatus. There was a problem that sufficient electrolytic efficiency could not be obtained.

特に電解液通路15中の金属ウェブl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、その疲労の度合いが著しく、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もたらす。
In particular, in the treatment liquid on the metal web l side in the electrolyte passage 15,
Mixing with the treatment liquid on the electrodes 3a, 3b side of the electrolyte passage 15 is insufficient, resulting in a significant degree of fatigue, resulting in non-uniform graining, that is, deterioration of electrolytic quality and electrolytic efficiency.

従って均−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。
Therefore, in order to maintain a uniform and dense grain and increase electrolysis efficiency, a method has been used to increase the flow rate supplied from the electrolyte supply port 4. However, increasing the amount of supplied liquid increases costs. Not only did it connect, but even if the flow rate was increased, a sufficient desired grain could not be obtained.

又、上記の問題はラインの速度上昇に対応した電解処理
装置全体により顕著になり、ラインの速度上昇の大きな
制約となっていた。
In addition, the above-mentioned problem becomes more noticeable as the entire electrolytic treatment apparatus responds to an increase in line speed, and becomes a major constraint on increasing line speed.

本発明の目的は、これら従来の問題点を解決し、砂目立
てが均−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 conventional problems and to provide an electrolytic treatment apparatus that has uniform and dense graining, has good electrolytic efficiency, and is effective in increasing line speed.

〔11B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、金属ウェブと対極と
の間に交番波形電流を供給して該金属ウェブに連続的に
電気化学的処理を施す電解処理装置において、該金属ウ
ェブと該対極間に供給される該電解処理液を電解液通路
において攪拌する手段を1または複数個有することを特
徴とする電解処理装置 によって達成される。
[Means and effects for solving 11B] That is, the above object of the present invention is to supply an alternating waveform current between a metal web and a counter electrode in an electrolytic treatment solution containing metal ions to continuously flow the metal web. An electrolytic treatment apparatus that performs electrochemical treatment on a metal web and a counter electrode, the electrolytic treatment apparatus comprising one or more means for stirring the electrolytic treatment liquid supplied between the metal web and the counter electrode in an electrolyte passageway. achieved by.

本発明における電解処理液の電解液通路における攪拌手
段としては、金属ウェブ面に対して電解処理液を吹きつ
ける噴流を起こす手段、又は電解液通路内の液流を攪拌
混合する手段であれば、如何なる手段を用いてもよい、
 例えば、スリットより金属ウェブに垂直に液を吹きつ
けて通路内の電解処理液を撹拌混合する手段、電解液通
路の幅方向に亘って回転軸を有する攪拌羽根、電解液通
路内の電解処理液を金属ウェブ方向に向ける邪魔板、電
解液通路を収縮、拡大する絞り機構等をあげることがで
きる。
The stirring means for the electrolytic treatment solution in the electrolyte passage in the present invention may be a means for generating a jet stream that sprays the electrolyte treatment liquid against the metal web surface, or a means for stirring and mixing the liquid flow in the electrolyte passage. Any means may be used,
For example, a means for stirring and mixing the electrolytically treated liquid in the passage by spraying the liquid perpendicularly onto the metal web through a slit, a stirring blade having a rotating shaft spanning the width direction of the electrolyte passage, and a means for stirring and mixing the electrolytically treated liquid in the electrolyte passage. Examples include a baffle plate that directs the electrolyte toward the metal web, and a diaphragm mechanism that contracts and expands the electrolyte passage.

以下、図を用いて本発明の実施態様を説明する。Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の電解処理装置の一実施例である。1は
金属ウェブであり、2はウェブを支えるラジアルドラム
ローラであり。金属ウェブlは主対極3a、3b、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3〜50鴫程度が適当である。
FIG. 1 shows an embodiment of the electrolytic treatment apparatus of the present invention. 1 is a metal web, and 2 is a radial drum roller that supports the web. The metal web 1 runs while maintaining a constant clearance with the main counter electrodes 3a, 3b and the auxiliary counter electrode 8. The appropriate clearance is usually about 3 to 50 mm.

主対極と補助対極との比は求める電解エツチング条件に
より異なる。7は交流電源であり、通常0.1〜500
Hzの交流電源が使用される。周波数については求める
エツチング形態によって変化させるが、周波数が15H
z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。
The ratio of the main counter electrode to the auxiliary counter electrode varies depending on the desired electrolytic etching conditions. 7 is an AC power supply, usually 0.1 to 500
A Hz AC power source is used. The frequency is changed depending on the desired etching form, but the frequency is 15H.
If it is less than z, the main counter electrodes 3a and 3b will deteriorate significantly, especially in the case of carbon.

波形としては、いろいろあるが、特公昭56−1928
0号、特公昭55−19191号各公報定記載の特殊交
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、B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。
There are various waveforms, but the
It is also possible to use the special alternating waveforms described in each publication. 9 is a diode;
This controls the current flowing to the auxiliary counter electrode of B. As the material for the auxiliary counter electrode 8, it is preferable to use platinum, which is resistant to deterioration.

本発明における電解処理液攪拌手段として第1図では、
主対極3aと1対1i3bとの境界の絶縁体部に噴流液
供給装置llを設けたものである。
In FIG. 1, as an electrolytically treated solution stirring means in the present invention,
A jet liquid supply device 11 is provided at the insulator section at the boundary between the main counter electrode 3a and the 1i3b.

噴流液供給装置11では、噴流液は供給管12よリキャ
ビティ13に入り、スリット14より電解液通路15の
中に噴出される。
In the jet liquid supply device 11 , the jet liquid enters the cavity 13 through the supply pipe 12 and is ejected from the slit 14 into the electrolyte passage 15 .

この噴流液により、金属ウェブ1近傍の疲労した電解処
理液が、それに対向した主対i3a、3b側のより新鮮
な電解処理液とat*混合されることによ、りて、金属
ウェブ1が従来より新鮮な電解処理液によって接触させ
られ、砂目立ての品質もより均一になり、電解効率も上
昇するのである。
Due to this jet liquid, the exhausted electrolytic treatment liquid near the metal web 1 is mixed at* with the fresher electrolytic treatment liquid on the opposite main pair i3a, 3b side, and thus the metal web 1 is Since contact is made with a fresher electrolytic solution than in the past, the quality of the graining becomes more uniform and the electrolytic efficiency increases.

金属ウェブlがラジアルドラムローラ2によって支持さ
れるこの種の電解処理装置では、電解液通路15を流れ
る電解処理液5が金属ウェブ1の表面に′a、膜となっ
て主対極3a、3b側に流れる電解処理液とは混合しに
くい状態になるからであると考えられる。従って電解液
通路内の攪拌手段が処理液の均−化及び金属ウェブ表面
の境膜更新に非常に有効な働きをなすものと考えられる
In this type of electrolytic processing apparatus in which the metal web 1 is supported by the radial drum roller 2, the electrolytic processing liquid 5 flowing through the electrolytic liquid passage 15 forms a film on the surface of the metal web 1, forming a film on the main counter electrodes 3a, 3b side. This is thought to be because it becomes difficult to mix with the electrolytically treated solution flowing through the water. Therefore, it is considered that the stirring means in the electrolytic solution passage plays a very effective role in equalizing the processing solution and renewing the film on the surface of the metal web.

噴流液供給装置から供給される噴流液は電解処理液と同
じ成分、濃度、温度のものが好ましいが、電解処理液に
悪影響を与えるものでなければ他の成分1m度5温度で
あっても構わない。
The jet liquid supplied from the jet liquid supply device preferably has the same composition, concentration, and temperature as the electrolytic treatment liquid, but other components may be at a temperature of 5 degrees Celsius per meter as long as it does not adversely affect the electrolytic treatment liquid. do not have.

又、噴流液の作用は攪拌作用をおこすことを主体となす
ため、噴流液の供給量は少なくても、撹拌効果の大きい
速度をもたせることが望まれる。
Furthermore, since the main effect of the jet liquid is to produce a stirring action, it is desirable that the jet liquid be supplied at a speed that provides a large stirring effect even if the amount of the jet liquid is small.

また噴流液供給装置11は撹拌効果を高める為に第1図
に示すように、例えばキャビティ13より金属ウェブl
に直角に噴流するスリット14を1ケ又は2ヶ以上設け
ることも効果的である。この噴流によって、金属ウェブ
表面の疲労した電解処理液は取り去られ電解液通路15
内の電解処理液5は全流量が均一な濃度と温度になり、
金属ウェブ1はより新鮮な電解処理液に接触し、均−且
つ緻密な砂目立てを行い、電解効率が上昇する。
Further, in order to enhance the stirring effect, the jet liquid supply device 11 is configured such that, for example, the metal web l is
It is also effective to provide one or more slits 14 that allow the jet to flow at right angles to the air. By this jet flow, the fatigued electrolytic treatment liquid on the surface of the metal web is removed and the electrolyte passage 15
The entire flow rate of the electrolytically treated liquid 5 in the chamber becomes uniform in concentration and temperature,
The metal web 1 comes into contact with a fresher electrolytic treatment solution, and is evenly and densely grained, increasing the electrolytic efficiency.

本発明において、金属ウェブ1と主対極3a3b間に供
給される電解処理液を攪拌する手段として、第1図では
液噴流による方法をしめしたが、勿論これに限定される
ものではなく、電解液通路内の電解処理液を攪拌出来る
手段であれば、どのようなものでも良(例えばその1例
として、第1図に第2図(a)に示した電解液通路の幅
方向に亘って回転軸を有する攪拌翼16を必要個所に配
置することも効果的である。
In the present invention, as a means for stirring the electrolytically treated liquid supplied between the metal web 1 and the main counter electrode 3a3b, a method using a liquid jet is shown in FIG. Any means can be used as long as it can stir the electrolyte treatment solution in the passage (for example, one example is a means that rotates across the width of the electrolyte passage shown in Fig. 1 and Fig. 2 (a)). It is also effective to arrange stirring blades 16 having shafts at necessary locations.

また、攪拌手段の数は1個以上であれば、いくつでも良
く、その位置も自由に決定出来る。
Further, the number of stirring means may be any number as long as it is one or more, and the positions thereof can be determined freely.

又、第2図0))及び(C)に示すように主対極3aと
主対極3bとの境界の絶縁体10の所に電解処理液の流
れが収縮・膨張する邪[Fi、、ペンチエリ−管状のも
の17や邪魔板18等を設けてもよい。
In addition, as shown in FIG. 2 0)) and (C), the flow of the electrolytic treatment solution contracts and expands at the insulator 10 at the boundary between the main counter electrode 3a and the main counter electrode 3b. A tubular member 17, a baffle plate 18, etc. may be provided.

(実 施 例) 実施例−1 第1図のような装置を用いて、電解液供給口4から電解
処理液を25004!/sin供給し、噴流液供給装置
11より下記主対極の電解処理液と同一の液を1001
 /winの流量で噴流攪拌した。
(Example) Example-1 Using the apparatus shown in Fig. 1, 25,004 liters of electrolytically treated solution was supplied from the electrolyte supply port 4. /sin is supplied, and the same liquid as the electrolytic treatment liquid of the main counter electrode shown below is supplied from the jet liquid supply device 11 to 1001.
Jet stirring was performed at a flow rate of /win.

この時の条件は 1対8i=  カーボン 補助対極        : 白金 ウェブとその対極のクリアランス:lO關主対極の電解
処理液条件 :処理液  硝酸濃度 50g/ j! 温度 60℃ 神助対極の電解処理液条件:処理液  硝酸濃度 50
g/ 1 温度 20°C ウェブ幅          1000閤処理速度  
        15醜/sin周波数       
    10011zであった。
The conditions at this time are 1:8i = Carbon auxiliary counter electrode: Clearance between the platinum web and its counter electrode: 1O. Electrolytic treatment solution conditions for the main counter electrode: Treatment solution Nitric acid concentration 50g/j! Temperature: 60℃ Kamisuke counter electrode electrolytic treatment solution conditions: Treatment solution nitric acid concentration: 50
g/1 Temperature 20°C Web width 1000 sheets Processing speed
15 ugliness/sin frequency
It was 10011z.

以上の条件で砂目立てを行ったところ、均−且つ緻密な
砂目を生成することが出来た。
When graining was carried out under the above conditions, uniform and dense grains could be produced.

比較例−1 第3図の装置を用いて、電解処理液供給量を25 Q 
01 /sinとした他、実施例−1と同じ電解処理液
条件で砂目立てを行ったところ、金属ウェブと接触する
電解処理液とその主対極側を流れる電解処理液との混合
が出来ない為、金属ウェブと接触する電解処理液の疲労
がそのまま表れて金属ウェブに不均一な砂目を生じた。
Comparative Example-1 Using the apparatus shown in Figure 3, the amount of electrolytic treatment solution supplied was 25 Q.
01/sin, and graining was performed under the same electrolytic treatment liquid conditions as in Example-1, but the electrolytic treatment liquid in contact with the metal web and the electrolytic treatment liquid flowing on the main opposite electrode side could not mix. , fatigue of the electrolytic treatment solution in contact with the metal web was directly manifested, resulting in uneven grains on the metal web.

〔発明の効果〕〔Effect of the invention〕

上記実施例から明らかなように、本発明の電解処理装置
により、金属ウェブと対極間に供給される電解処理液の
攪拌手段により、金属ウェブに接触する電解処理液の濃
度が上がり、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、生産ラインのスピードアップが可能
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 clear from the above embodiments, in the electrolytic treatment apparatus of the present invention, the concentration of the electrolytic treatment liquid in contact with the metal web is increased by means of stirring the electrolytic treatment liquid supplied between the metal web and the counter electrode, and as a result, sand The uniformity and fineness of the eyes are maintained,
The electrolysis efficiency has increased, making it possible to speed up the production line, greatly contributing to improving quality and reducing product costs.

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

第1図は本発明の電解処理装置の一実施例の側面図、第
2図(a)、 (b)、 (C)は本発明の電解液攪拌
装置の他の実施例の部分側面図、第3図は従来の電解処
理装置の一例の側面図である。 l・・・金属ウェブ 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・・・電解液排出ロア・・・交
流電源  8・・・補助対極9・・・ダイオード 10
・・・絶縁体11・・・噴流液供給装置 12・・・供給管  13・・・キャビティ14・・・
スリット 15・・・電解液通路16・・・攪拌羽根 17・・・ペンチエリ−管状物 18 ・ ・ ・ 邪魔番反 第 図
FIG. 1 is a side view of one embodiment of the electrolytic treatment device of the present invention, and FIGS. 2(a), (b), and (C) are partial side views of another embodiment of the electrolytic solution stirring device of the present invention. FIG. 3 is a side view of an example of a conventional electrolytic treatment apparatus. l... Metal web 2... Radial drum rollers 3a, 3b... Main counter electrode 4... Electrolyte supply port 5... Electrolytic treatment liquid 6... Electrolyte discharge lower... AC power supply 8 ...Auxiliary counter electrode 9...Diode 10
... Insulator 11 ... Jet liquid supply device 12 ... Supply pipe 13 ... Cavity 14 ...
Slit 15... Electrolyte passage 16... Stirring blade 17... Pentier tubular object 18...

Claims (1)

【特許請求の範囲】[Claims] 金属イオンを含む電解処理液中で、金属ウェブと対極と
の間に交番波形電流を供給して該金属ウェブに連続的に
電気化学的処理を施す電解処理装置において、該金属ウ
ェブと該対極間に供給される該電解処理液を電解液通路
において攪拌する手段を1または複数個有することを特
徴とする電解処理装置
In an electrolytic treatment apparatus that continuously applies an electrochemical treatment to the metal web by supplying an alternating waveform current between the metal web and the counter electrode in an electrolytic treatment solution containing metal ions, between the metal web and the counter electrode. An electrolytic treatment device characterized by having one or more means for stirring the electrolytic treatment solution supplied to the electrolytic treatment solution in an electrolytic solution passage.
JP5802889A 1989-03-13 1989-03-13 Electrolytically treating device Pending JPH02240299A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5802889A JPH02240299A (en) 1989-03-13 1989-03-13 Electrolytically treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5802889A JPH02240299A (en) 1989-03-13 1989-03-13 Electrolytically treating device

Publications (1)

Publication Number Publication Date
JPH02240299A true JPH02240299A (en) 1990-09-25

Family

ID=13072495

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5802889A Pending JPH02240299A (en) 1989-03-13 1989-03-13 Electrolytically treating device

Country Status (1)

Country Link
JP (1) JPH02240299A (en)

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