JPH06108290A - Continuous electrolytic treatment device - Google Patents

Continuous electrolytic treatment device

Info

Publication number
JPH06108290A
JPH06108290A JP25617192A JP25617192A JPH06108290A JP H06108290 A JPH06108290 A JP H06108290A JP 25617192 A JP25617192 A JP 25617192A JP 25617192 A JP25617192 A JP 25617192A JP H06108290 A JPH06108290 A JP H06108290A
Authority
JP
Japan
Prior art keywords
electrode
current density
strip
shaped metal
metal plate
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.)
Granted
Application number
JP25617192A
Other languages
Japanese (ja)
Other versions
JP2946445B2 (en
Inventor
Hiroo Kubota
洋夫 久保田
Nagayoshi Kaneko
修芳 金子
Akio Uesugi
彰男 上杉
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 JP25617192A priority Critical patent/JP2946445B2/en
Publication of JPH06108290A publication Critical patent/JPH06108290A/en
Application granted granted Critical
Publication of JP2946445B2 publication Critical patent/JP2946445B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To efficiently perform the electrolytic treatment while preventing a current from concentrating in the side end part and sneaking round to the rear side by making the effective area of a high current density smaller than that of a low current density in an electrode arranged to face a band-shaped metallic plate running in an electrolyte. CONSTITUTION:A band-shaped Al product is run in the electrolyte like sulfuric acid, and power is supplied between this product and an electrolytic electrode facing it to perform the anodic oxidation treatment. In this electrolytic treatment device, this electrolytic electrode 8 is so constituted that the effective area of at least a part of the electrode where the current density exceeds about 5A/dm<2> is smaller than that where the current density does not exceed about 5A/dm<2>. For example, the electrolytic electrode 8 is so formed that the width is stepwise changed in the running direction of an arrow (a) of the Al product 7, and the electrolytic electrode 8 consists of a wide electrode part 9 wider than the Al product 7 and a narrow electrode part 10 narrower than it. The wide electrode part 9 consists of a low current density part (b) having <5A/dm<2> current density, and the narrow electrode part 10 consists of a high current density part (c) having >=5A/dm<2> current density.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、平版印刷版用支持体に
用いるアルミニウム板の陽極酸化処理などの帯状金属板
の連続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 apparatus for continuously electrolytically treating a strip-shaped metal plate such as anodizing treatment of an aluminum plate used for a lithographic printing plate support.

【0002】[0002]

【従来の技術】一般に、平版印刷版に使用されるアルミ
ニウム支持体は、親水性及び保水性に優れていることが
要求され、そのために機械的、化学的又は電気化学的な
方法で表面に微細な凹凸を形成して粗面化処理されてい
る。さらに、この粗面化処理された表面の機械的強度及
び保水性を向上させるために、表面を陽極酸化処理する
ことも一般に行われている。
2. Description of the Related Art Generally, an aluminum support used for a lithographic printing plate is required to have excellent hydrophilicity and water retention property, and therefore, the surface thereof is finely divided by a mechanical, chemical or electrochemical method. Rough surface is formed by forming irregularities. Further, in order to improve the mechanical strength and the water retention of the roughened surface, the surface is generally anodized.

【0003】従来、平版印刷版用支持体の陽極酸化処理
は、特開昭48−26638号、特公昭58−24517号、特開昭47
−18739号各公報等で開示されている陽極酸化処理方法
で行われており、この方法は、いわゆる液中給電方式と
呼ばれている。この液中給電方式による陽極酸化処理装
置(いわゆるフラット型)としては、例えば、図11に示
す装置があった。
Conventionally, the anodizing treatment of the support for a lithographic printing plate has been carried out by JP-A-48-26638, JP-B-58-24517 and JP-A-47.
The method is carried out by the anodizing method disclosed in each of Japanese Patent Publication No. 18739, etc., and this method is called a so-called submerged power supply method. As an anodizing apparatus (so-called flat type) by this submerged power feeding method, for example, there is an apparatus shown in FIG.

【0004】図12に示す陽極酸化処理装置は、アルミニ
ウム製品31を負に帯電させるための給電槽32と、アルミ
ニウム製品31を陽極酸化処理する陽極酸化処理槽33と、
給電槽32と陽極酸化処理槽33との間の電流の短絡を防止
する中間部34とが設けられ、給電槽32及び陽極酸化処理
槽33には電解液35が貯留されている。そして、給電槽32
には給電電極36が、陽極酸化処理槽33には電解電極37が
それぞれ電解液35中に配置され、これらの給電電極36電
解電極37は直流電源38を介して接続されている。そし
て、上記陽極酸化処理槽33における電解電極37は、図13
に示すように、アルミニウム製品31の幅より長く形成さ
れている。
The anodizing apparatus shown in FIG. 12 includes a power supply tank 32 for negatively charging the aluminum product 31, an anodizing tank 33 for anodizing the aluminum product 31,
An intermediate portion 34 that prevents a short circuit of current between the power feeding tank 32 and the anodizing treatment tank 33 is provided, and an electrolytic solution 35 is stored in the power feeding tank 32 and the anodizing treatment tank 33. And the power supply tank 32
A power supply electrode 36 is arranged in the electrolytic solution 35, and an electrolytic electrode 37 is arranged in the anodizing tank 33 in the electrolytic solution 35. The power supply electrode 36 and the electrolytic electrode 37 are connected to each other via a DC power supply 38. The electrolytic electrode 37 in the anodizing treatment tank 33 is shown in FIG.
As shown in, the width is formed longer than the width of the aluminum product 31.

【0005】このような陽極酸化処理装置においては、
直流電源38からの電流は、給電槽32で給電電極36から電
解液35を介してアルミニウム製品31に流れ、その電流が
アルミニウム製品31内を陽極酸化処理槽33へ流れる。こ
れにより、陽極酸化処理槽33においてアルミニウム製品
31の表面に陽極酸化皮膜が生成される。
In such an anodizing apparatus,
A current from the DC power supply 38 flows in the power supply tank 32 from the power supply electrode 36 through the electrolytic solution 35 to the aluminum product 31, and the current flows in the aluminum product 31 to the anodizing treatment tank 33. As a result, the aluminum product in the anodizing tank 33 is
An anodized film is formed on the surface of 31.

【0006】[0006]

【発明が解決しようとする課題】ところで、平版印刷版
用支持体の製造ラインにおいては、平版印刷版製品のサ
イズが非常に多様であるので、通常、被処理物であるア
ルミニウム製品も多様な巾のものが用いられている。
On the other hand, in the production line of the lithographic printing plate support, the size of the lithographic printing plate product is very diverse, so that the aluminum product, which is the object to be processed, usually has various widths. Is used.

【0007】そこで、従来、上述した図13に示すよう
に、電解電極の巾をアルミニウム製品の最大巾よりも広
くして、多様な全てのアルミニウム製品に対応できるよ
うにしていた。
Therefore, conventionally, as shown in FIG. 13 described above, the width of the electrolytic electrode is made wider than the maximum width of the aluminum product so that it can be applied to all various aluminum products.

【0008】したがって、陽極酸化処理槽においてはア
ルミニウム製品の側端部に電流が集中し、両側端部にお
ける酸化皮膜量が中央部に比べて増大するものであっ
た。このような現象は、供給電流量が小さい場合は余り
問題にならないが、生産性向上のために処理ラインを高
速化させたり、品質性能向上のために陽極酸化皮膜量を
増加させたりする場合は高電流密度化しなければなら
ず、高電流密度化させると、アルミニウム製品の側端部
における酸化皮膜量の増大が著しくなり、品質上の許容
限度を越えたり、局所的な反応の集中によりいわゆるヤ
ケ故障が発生するものであった。したがって、高電流密
度化ができず処理ラインの高速化、陽極酸化皮膜量の増
加などを行うことができなかった。また設備が大型化
し、かつ設備費も高くなるものであった。
Therefore, in the anodizing treatment tank, the electric current is concentrated on the side end portions of the aluminum product, and the amount of the oxide film on both side end portions is increased as compared with the central portion. Such a phenomenon does not become a problem when the amount of supplied current is small, but when increasing the processing line speed to improve productivity or increasing the anodized film amount to improve quality performance, It is necessary to increase the current density, and when the current density is increased, the amount of oxide film on the side edges of aluminum products increases significantly, which exceeds the allowable limit in terms of quality and causes so-called discoloration due to local concentration of reactions. It was a failure. Therefore, it was not possible to increase the current density, and it was not possible to speed up the processing line or increase the amount of anodized film. In addition, the equipment is large and the equipment cost is high.

【0009】さらに、アルミニウム製品の被処理面の裏
面に電流が廻り込み、被処理面の皮膜生成効率が低下す
るものであった。そこで、本出願人は、電極の巾を狭く
したり、電極と帯状金属板との間にマスキング板を設け
たりした陽極酸化装置を提案した(特願平3−294204
号)。
Furthermore, an electric current circulates to the back surface of the surface to be processed of the aluminum product, and the efficiency of film formation on the surface to be processed is reduced. Therefore, the present applicant has proposed an anodizing device in which the width of the electrode is narrowed or a masking plate is provided between the electrode and the strip-shaped metal plate (Japanese Patent Application No. 3-294204).
issue).

【0010】本発明は、上記提案した技術をさらに改良
し、電流の側端部への集中および裏面への廻り込みを防
止しつつ、より効率よく電解処理できる連続電解処理装
置を提供することを目的とする。
The present invention is to further improve the above-mentioned proposed technique and provide a continuous electrolytic treatment apparatus capable of more efficiently performing electrolytic treatment while preventing the concentration of electric current on the side end portion and the sneak to the back surface. To aim.

【0011】[0011]

【課題を解決するための手段】本発明は、上記目的を達
成するためになされたもので、本発明の連続電解処理装
置は、電解液と、該電解液中に設けられた電極とを有
し、電解液中に帯状金属板を走行させて帯状金属板を電
解処理する装置において、電流密度が5A/dm2を越える
電極の少なくとも一部の有効面積を、電流密度が5A/dm
2を越えない電極の有効面積より小さくすることを特徴
として構成されている。
The present invention has been made to achieve the above object, and a continuous electrolytic treatment apparatus of the present invention has an electrolytic solution and an electrode provided in the electrolytic solution. In an apparatus for electrolytically treating a strip-shaped metal plate by running the strip-shaped metal plate in an electrolytic solution, the effective area of at least a part of the electrode having a current density of more than 5 A / dm 2 is 5 A / dm 2.
The feature is that it is smaller than the effective area of the electrode that does not exceed 2 .

【0012】電流密度が約5A/dm2を越えるか否かで電
極を区分したのは、電流密度が約5A/dm2を越える場合
は、側端部への電流の集中及び裏面への廻り込みの弊害
が大きいからである。また、この弊害は種々の電解条件
によって変動するので、この変動に応じて、電流密度が
約5A/dm2を越える電極の内、有効面積を小さくする範
囲(電極の1/2の部分、2/3の部分、全部等)を決定す
る。また、この有効面積は、電極の電解処理に寄与して
いる面積のことである。
[0012] The current density was divided electrodes on whether more than about 5A / dm 2, if the current density exceeds about 5A / dm 2, around the concentrate and the back surface of the current to the side edge This is because the harmful effects of inclusion are great. In addition, this adverse effect fluctuates due to various electrolysis conditions. Therefore, in accordance with this fluctuation, the range in which the effective area is reduced in the electrodes whose current density exceeds approximately 5 A / dm 2 (1/2 of the electrode, 2 / 3 part, all etc.). The effective area is an area that contributes to the electrolytic treatment of the electrodes.

【0013】電流密度が約5A/dm2を越える電極の少な
くとも一部の有効面積を、電流密度が約5A/dm2 を越え
ない電極の有効面積より小さくする手段としては、例え
ば、 電流密度が約5A/dm2を越える電極の少なくとも一部
の巾を、電流密度が約5A/dm2を越えない電極の巾及び
帯状金属板の巾より小さく形成する手段、電流密度が
約5A/dm2を越える電極の少なくとも一部の側端部に切
欠を形成する手段、 電流密度が約5A/dm2を越える電極の少なくとも一部
の側端部にマスキング板を設ける手段がある。
[0013] at least a portion of the effective area of the current density exceeds about 5A / dm 2 electrode, as a means to be smaller than the effective area of the electrode current density does not exceed about 5A / dm 2, for example, current density at least a portion of the width of the electrode in excess of about 5A / dm 2, means for reducing formation than the width of the width and the strip metal plate electrode current density does not exceed about 5A / dm 2, current density of about 5A / dm 2 There is a means for forming a notch in the side end of at least a part of the electrode exceeding 5 cm, and a means for providing a masking plate at the side end of at least a part of the electrode having a current density exceeding approximately 5 A / dm 2 .

【0014】電流密度が約5A/dm2を越える電極の少な
くとも一部の巾を、電流密度が約5A/dm2を越えない電
極の巾及び帯状金属板の巾より小さく形成する手段にお
いて、小さくした巾は、帯状金属板の巾、帯状金属板と
電極との距離等によって、適宜最適な長さに設定され
る。例えば、帯状金属板の巾が1000mm、帯状金属板と電
極との距離が20mmの場合、300〜900mmの範囲が好まし
く、500〜800mmの範囲が特に好ましい。
[0014] at least a portion of the width of the current density exceeds about 5A / dm 2 electrodes, the means to smaller than forming width of width and strip metal plate electrode current density does not exceed about 5A / dm 2, small The width is appropriately set to an optimum length depending on the width of the strip-shaped metal plate, the distance between the strip-shaped metal plate and the electrodes, and the like. For example, when the width of the strip-shaped metal plate is 1000 mm and the distance between the strip-shaped metal plate and the electrode is 20 mm, the range of 300 to 900 mm is preferable, and the range of 500 to 800 mm is particularly preferable.

【0015】電流密度が約5A/dm2を越える電極の少な
くとも一部に切欠及び穴の1種以上を形成する手段は、
例えば、電極の側端部を連続する三角形、四角形、円弧
状等に形成したり、電極全体に穴を穿設し、その穴を側
端に行くに従って小さくしたりする。
Means for forming one or more notches and holes in at least a portion of the electrode having a current density of greater than about 5 A / dm 2 is
For example, the side end portion of the electrode is formed in a continuous triangle, quadrangle, arc shape, or the like, or a hole is formed in the entire electrode and the hole is made smaller toward the side end.

【0016】電流密度が約5A/dm2を越える電極の少な
くとも一部の側端部にマスキング板を設ける手段におい
て、マスキング板は、電極と帯状金属板の間であって、
少なくとも帯状金属板に対向しないが電極に対向する位
置に設けられる。すなわち、マスキング板が最小の場
合、マスキング板の内側の側端が帯状金属板の側端と一
致するものであり、それ以外の場合、マスキング板の内
側の側端が、帯状金属板の側端より内側に位置している
ものである。このマスキング板の内側の側端の位置は、
帯状金属板の巾、電極の巾、帯状金属板と電極の距離等
により適宜決定され、例えば、帯状金属板の側端から20
0mmの範囲が好ましい。マスキング板の内側側端が帯状
金属板の側端より外側にあると、帯状金属板の側端部へ
の電流の集中を有効に抑制することができず、マスキン
グ板の内側側端が帯状金属板の側端から内側に向かって
200mmより内側にあると、帯状金属板の側端部における
陽極酸化皮膜量が通常より減少する。
In the means for providing a masking plate on the side edge of at least a part of the electrode having a current density of more than about 5 A / dm 2 , the masking plate is between the electrode and the strip-shaped metal plate.
It is provided at least at a position not facing the strip-shaped metal plate but facing the electrode. That is, when the masking plate is the minimum, the inner side edge of the masking plate coincides with the side edge of the strip-shaped metal plate, and in other cases, the inner side edge of the masking plate is the side edge of the strip-shaped metal plate. It is located inside. The position of the inner side edge of this masking plate is
It is appropriately determined by the width of the strip-shaped metal plate, the width of the electrode, the distance between the strip-shaped metal plate and the electrode, for example, 20 from the side edge of the strip-shaped metal plate.
A range of 0 mm is preferred. If the inner side edge of the masking plate is outside the side edge of the strip-shaped metal plate, the concentration of current on the side edge of the strip-shaped metal plate cannot be effectively suppressed, and the inner side edge of the masking plate is From the side edge of the board to the inside
If it is inside 200 mm, the amount of anodized film on the side edge of the strip-shaped metal plate will be smaller than usual.

【0017】このようなマスキング板は、電極の表面に
設けられ、帯状金属板の巾方向において側端部より中央
部の方が開口率が大きい電極カバーを用いることができ
る。この電極カバーは、開口部が穿設されており、この
開口部の開口率が中央部の方が大きくなっている。例え
ば、開口部を円形としたとき、中央部は径を大きく側端
部は径を小さくしたり、中央部側を底辺そして側端部側
を頂点とするような二等辺三角形としたりする。
Such a masking plate is provided on the surface of the electrode, and it is possible to use an electrode cover in which the central portion has a larger aperture ratio than the side end portions in the width direction of the strip-shaped metal plate. The electrode cover is provided with an opening, and the opening ratio of the opening is larger in the central portion. For example, when the opening has a circular shape, the central portion has a large diameter and the side end portions have a small diameter, or the central portion has a base and the side end has an apex.

【0018】また、本発明の連続電解装置は、電解液
と、該電解液中に設けられた電極とを有し、電解液中に
帯状金属板を走行させて帯状金属板を電解処理する装置
において、電流密度が約5A/dm2を越える電極の少なく
とも一部が、帯状金属板の巾方向において側端に行くに
従って帯状金属板との距離が長くなるように形成されて
いることを特徴として構成されている。
Further, the continuous electrolysis apparatus of the present invention has an electrolytic solution and electrodes provided in the electrolytic solution, and is an apparatus for electrolytically treating the strip-shaped metal plate by running the strip-shaped metal plate in the electrolytic solution. In at least a part of the electrodes having a current density of more than about 5 A / dm 2 , the distance between the electrode and the strip-shaped metal plate becomes longer toward the side edge in the width direction of the strip-shaped metal plate. It is configured.

【0019】側端に行くに従って帯状金属板との距離が
長くなるようにするには、その断面形状において、中央
に行くに従って帯状金属板方向に突出した形状に形成す
る。この突出した形状は、連続的であっても、非連続的
であってもよく、例えば、連続的に変化する形状として
は、円弧状、二等辺三角形状、放物線状等があり、非連
続的に変化する形状としては、階段状がある。
In order to make the distance to the strip-shaped metal plate longer toward the side edge, the cross-sectional shape is formed so as to project toward the strip-shaped metal plate toward the center. This protruding shape may be continuous or discontinuous. For example, the continuously changing shape may be a circular arc shape, an isosceles triangle shape, a parabolic shape, or the like. There is a staircase shape as the shape that changes to.

【0020】帯状金属板は、純アルミニウム又はアルミ
ニウム合金の帯状金属板があり、上記アルミニウム合金
としては、例えば、珪素、鉄、銅、マンガン、マグネシ
ウム、クロム、亜鉛、ビスマス、ニッケルなどの金属と
のアルミニウム合金がある。帯状金属板の厚みは、一般
に、0.1〜0.5mmの範囲である。
The strip-shaped metal plate may be a strip-shaped metal plate made of pure aluminum or an aluminum alloy. Examples of the aluminum alloy include metals such as silicon, iron, copper, manganese, magnesium, chromium, zinc, bismuth and nickel. There is an aluminum alloy. The thickness of the strip-shaped metal plate is generally in the range of 0.1 to 0.5 mm.

【0021】電解液としては、例えば、硫酸、燐酸、シ
ュウ酸又はそれらの塩の水溶液、あるいはそれらの混合
液があるが、所望の品質を得るために最適なものを選べ
ばよい。電解液の濃度、温度も自由に選択できる。電源
波形としては、直流の場合が一般的であるが、他にも交
流波形や交直重畳波形など所望の品質を得るために最適
なものを選択できる。電解処理時の電流密度としては、
自由に選択できる。例えば、処理時間中常に一定値とし
てもよいし、次第に電流密度を上げていくようにしても
よい。
The electrolytic solution may be, for example, an aqueous solution of sulfuric acid, phosphoric acid, oxalic acid or a salt thereof, or a mixed solution thereof, and an optimum one may be selected to obtain a desired quality. The concentration and temperature of the electrolytic solution can be freely selected. As the power supply waveform, a direct current is generally used, but in addition, an optimum waveform such as an AC waveform or an AC / DC superposed waveform can be selected to obtain a desired quality. As the current density during electrolytic treatment,
You can choose freely. For example, the value may be constant during the processing time, or the current density may be gradually increased.

【0022】本発明の連続電解処理方法及び装置は、陽
極酸化処理、電解エッチング処理、電解メッキ処理など
に適用することができる。陽極酸化装置とする場合、従
来用いられている公知の陽極酸化装置(フラット型)に
適用することができるが、帯状金属板を支持する支持ロ
ーラーと、該支持ローラーの上流または下流の少なくと
も一方に設けられた帯状金属板と接触する給電ローラー
と、前記支持ローラーの外周面に沿って設置された略同
心円状の電極とを有する装置(ラジアル型)に適用する
こともできる。
The continuous electrolytic treatment method and apparatus of the present invention can be applied to anodizing treatment, electrolytic etching treatment, electrolytic plating treatment and the like. When it is used as an anodizing device, it can be applied to a conventionally used known anodizing device (flat type), but a supporting roller for supporting the strip-shaped metal plate and at least one of the upstream and downstream of the supporting roller. It can also be applied to a device (radial type) having a power feeding roller provided in contact with a band-shaped metal plate and a substantially concentric electrode provided along the outer peripheral surface of the supporting roller.

【0023】本発明を平板印刷支持版の陽極酸化装置に
用いる場合、陽極酸化処理の前段階において、通常、粗
面化処理が施されている。この粗面化処理は、アルミニ
ウム支持体の保水性及びその上に塗設される感光材料と
の密着性を向上させるためのもので、機械的粗面化法、
化学的粗面化法、電気化学的粗面化法又はそれらを組み
合わせた方法により行われる。
When the present invention is used in an anodizing apparatus for a lithographic printing plate, a roughening treatment is usually performed before the anodizing treatment. This roughening treatment is for improving the water retention of the aluminum support and the adhesion to the photosensitive material coated on the aluminum support.
It is carried out by a chemical surface roughening method, an electrochemical surface roughening method or a combination thereof.

【0024】機械的粗面化法としては、ワイヤーブラシ
グレイニング法、ブラシグレイニング法、サンドブラス
ト法、ボールグレイニング法などがある。化学的粗面化
法としては、選択的に表面を溶解させる方法などがあ
る。電気化学的粗面化法としては、硝酸、塩酸及びその
混合液を電解液として用いる方法がある。さらに、これ
らに硝酸アルミニウム、塩化アルミニウム、硝酸アンモ
ニウム、塩化アンモニウム、硝酸マンガン、塩化マンガ
ン、硝酸鉄、塩化鉄などの塩類を添加してもよい。ま
た、塩化ナトリウムや硝酸ナトリウムなどの中性塩水溶
液も用いることができる。
As the mechanical surface roughening method, there are a wire brush graining method, a brush graining method, a sandblast method, a ball graining method and the like. Examples of the chemical surface roughening method include a method of selectively dissolving the surface. As an electrochemical graining method, there is a method using nitric acid, hydrochloric acid and a mixed solution thereof as an electrolytic solution. Furthermore, salts such as aluminum nitrate, aluminum chloride, ammonium nitrate, ammonium chloride, manganese nitrate, manganese chloride, iron nitrate and iron chloride may be added thereto. Further, an aqueous solution of a neutral salt such as sodium chloride or sodium nitrate can also be used.

【0025】また、粗面化処理した後陽極酸化処理前
に、必要に応じてアルカリエッチング処理、中和処理、
デスマット処理などが適宜選択、複合して実施すること
ができる。また、以上のような装置を1ユニットとして
2つ以上の複数のユニットを長手方向に連結させ、複数
回上述した同様の陽極酸化処理を繰り返してもよい。
Further, after the surface roughening treatment and before the anodizing treatment, if necessary, an alkali etching treatment, a neutralization treatment,
Desmutting treatment or the like can be appropriately selected and combined. In addition, two or more units may be connected in the longitudinal direction with the above-mentioned device as one unit, and the same anodizing treatment described above may be repeated a plurality of times.

【0026】帯状金属板を陽極酸化処理した後、必要に
より特開平1−150583号公報記載の封孔処理、特開昭60
−149491号公報記載の親水化処理、米国特許3181461号
明細書記載のアルカリ金属シリケート水溶液処理、米国
特許3860426号明細書記載の水溶性金属塩を含む親水性
セルロースの下塗り層塗設などを適宜選択して実施でき
る。
After subjecting the strip-shaped metal plate to anodizing treatment, if necessary, the sealing treatment described in JP-A-1-150583, JP-A-60
-149491 disclosed hydrophilic treatment, U.S. Pat. No. 3,181,461, aqueous alkali metal silicate solution treatment, U.S. Pat.No. 3,860,426, hydrophilic cellulose-containing undercoat layer coating containing a water-soluble metal salt are appropriately selected. Can be implemented.

【0027】本発明による帯状金属板を平版印刷版用支
持体に用いる場合は、その表面に感光層を設けて感光性
平版印刷版とすることができる。この感光層の組成物と
しては、ジアゾ樹脂からなるもの、o−キノンジアジゾ
化合物からなるもの、感光性アジド化合物からなるも
の、光重合性組成物、分子中に不飽和二重結合を有する
感光性樹脂からなる組成物等がある。
When the strip-shaped metal plate according to the present invention is used as a lithographic printing plate support, a photosensitive layer can be provided on the surface of the lithographic printing plate support to prepare a photosensitive lithographic printing plate. The composition of the photosensitive layer includes a diazo resin, an o-quinonediadizo compound, a photosensitive azide compound, a photopolymerizable composition, and a photosensitive resin having an unsaturated double bond in the molecule. And the like.

【0028】[0028]

【作用】本発明では、電流が側端に集中したり、裏面に
廻り込んだりする電極の部位において、電極の有効面積
を小さくすること又は電極の側端と帯状金属板との距離
を長くすることにより、電流の側端への集中及び廻り込
みを防止し、かつ、電流が側端に集中したり、裏面に廻
り込んだりしない電極の部位においては、充分に電流を
供給する。
According to the present invention, the effective area of the electrode is reduced or the distance between the side end of the electrode and the strip-shaped metal plate is increased at the portion of the electrode where the electric current concentrates on the side edge or sneak into the back surface. As a result, the current is prevented from concentrating and sneaking into the side end, and the current is sufficiently supplied to the electrode portion where the current is not concentrating on the side end or sneaking into the back surface.

【0029】本発明の帯状金属板の連続電解処理装置の
一例を図面に基づいて説明する。図1は平版印刷版用支
持体の陽極酸化装置の模式図、図2は電解電極の平面
図、図3は図2中A−A線断面図、図4は図2中B−B
線断面図である。これらの図において、給電槽1、陽極
酸化槽2、中間部3、給電電極4、電解液5及び直流電
源6は、図12に示した従来の陽極酸化装置と略同様に構
成されており、また、アルミニウム製品7も同様であ
る。
An example of the continuous electrolytic treatment apparatus for a strip-shaped metal plate of the present invention will be described with reference to the drawings. 1 is a schematic view of an anodizing device for a lithographic printing plate support, FIG. 2 is a plan view of an electrolytic electrode, FIG. 3 is a sectional view taken along line AA in FIG. 2, and FIG. 4 is BB in FIG.
It is a line sectional view. In these figures, the power feeding tank 1, the anodizing tank 2, the intermediate portion 3, the power feeding electrode 4, the electrolytic solution 5 and the DC power source 6 are configured in substantially the same manner as the conventional anodizing device shown in FIG. The same applies to the aluminum product 7.

【0030】図1において、符号8はアルミニウム製品
7を陽極酸化するための電解電極で、この電解電極8
は、図2に示すように、アルミニウム製品7の走行方向
aに沿って巾が階段状に変化するように形成されてお
り、図3に示すように、アルミニウム製品7の巾より広
い巾広電極部9と、図4に示すように、アルミニウム製
品7の巾より狭い巾狭電極部10とから構成されている。
そして、この巾広電極部9部分は、電流密度が5A/dm2
未満の低電流密度部bであり、巾狭電極部10部分は電流
密度が5A/dm2以上の高電流密度部cである。
In FIG. 1, reference numeral 8 is an electrolytic electrode for anodizing the aluminum product 7, and this electrolytic electrode 8
2 is formed so that the width changes stepwise along the traveling direction a of the aluminum product 7, as shown in FIG. 2, and as shown in FIG. It is composed of a portion 9 and a narrow electrode portion 10 narrower than the width of the aluminum product 7, as shown in FIG.
The wide electrode portion 9 has a current density of 5 A / dm 2
Is a low current density portion b, and the narrow electrode portion 10 is a high current density portion c having a current density of 5 A / dm 2 or more.

【0031】以上のような陽極酸化装置で陽極酸化する
には、従来と同様に、直流電原6かで給電電極4及び電
解電極8に通電し、これにより、陽極酸化槽2において
アルミニウム製品7の表面に陽極酸化皮膜が生成させ
る。このとき、巾狭電極部10では、アルミニウム製品7
の巾より巾狭電極部10の巾が小さいので、電流はアルミ
ニウム製品7の前面に略均等に供給される。また、巾広
電極部9では、電流がアルミニウム製品7の側端部へ集
中するが、電流密度が小さいので皮膜の不均一、ヤケ故
障、裏面における皮膜の生成はほとんど発生しない。
To perform anodization with the anodizing device as described above, the power supply electrode 4 and the electrolytic electrode 8 are energized by the DC power source 6 in the same manner as in the conventional case, whereby the aluminum product 7 is stored in the anodizing tank 2. An anodic oxide film is formed on the surface. At this time, in the narrow electrode portion 10, the aluminum product 7
Since the width of the narrow electrode portion 10 is smaller than the width of, the current is supplied to the front surface of the aluminum product 7 substantially evenly. Further, in the wide electrode portion 9, current concentrates on the side end portion of the aluminum product 7, but since the current density is small, unevenness of the film, burn failure, and film formation on the back surface hardly occur.

【0032】図5は、電流密度が約5A/dm2を越える電
極の少なくとも一部の巾を、電流密度が約5A/dm2を越
えない電極の巾及び帯状金属板の巾より小さく形成し
た、他の例の電極の平面図である。図5に示す例の電極
11は、アルミニウム製品7の巾より広い巾広電極部12
と、アルミニウム製品7の巾より狭い巾狭電極部13が、
略等間隔で交互に形成されている。
[0032] Figure 5, a current density of at least a portion of the width of the electrode in excess of about 5A / dm 2, the current density was smaller than the width and the width of the strip-shaped metal plate electrodes not exceeding about 5A / dm 2 FIG. 6 is a plan view of another example of an electrode. Example electrode shown in FIG.
11 is a wide electrode portion 12 wider than the width of the aluminum product 7
And the narrow electrode part 13 narrower than the width of the aluminum product 7,
They are formed alternately at substantially equal intervals.

【0033】図6は、電流密度が約5A/dm2を越える電
極の少なくとも一部に切欠及び穴の1種以上を形成した
例の電極の部分平面図である。図6に示す例の電極15
は、両側端部において長方形状の切欠き16が一定間隔で
穿設されている。
FIG. 6 is a partial plan view of an electrode in which one or more kinds of notches and holes are formed in at least a part of the electrode having a current density exceeding about 5 A / dm 2 . Example electrode 15 shown in FIG.
Has rectangular notches 16 formed at both ends at regular intervals.

【0034】図7、図8及び図9は、電流密度が約5A/
dm2を越える電極の少なくとも一部の側端部にマスキン
グ板を設けた例の電極部分の部分平面図である。
In FIGS. 7, 8 and 9, the current density is about 5 A /
FIG. 9 is a partial plan view of an electrode portion of an example in which a masking plate is provided on at least a side end portion of an electrode exceeding dm 2 .

【0035】図7に示す例の電極11は従来と同一である
が、この電極11の中央の一部分を残して上表面にマスキ
ング板15が固着されている。このマスキング板は、中央
部側において長方形状の切欠き16が一定間隔で穿設され
ている。したがって、電極11の側端部は中央部より露出
面積が小さくなっている。
The electrode 11 of the example shown in FIG. 7 is the same as the conventional one, but a masking plate 15 is fixed to the upper surface of the electrode 11 leaving a part of the center thereof. In this masking plate, rectangular notches 16 are formed at regular intervals on the center side. Therefore, the exposed area of the side end portion of the electrode 11 is smaller than that of the central portion.

【0036】図8に示す例の電極18は従来と同一である
が、この電極18の中央の一部分を残して上表面にマスキ
ング板19が固着されている。このマスキング板19は、円
形の穴20が多数穿設され、すなわち、その穴20において
電極18が露出している、その穴20の大きさは中央部側へ
行くにつれて大きくなっている。したがって、電極18は
中央部に行くにつれて露出面積が大きくなっている。
Although the electrode 18 of the example shown in FIG. 8 is the same as the conventional one, a masking plate 19 is fixed to the upper surface of the electrode 18 leaving a part of the center thereof. The masking plate 19 is provided with a large number of circular holes 20, that is, the electrodes 18 are exposed in the holes 20. The size of the holes 20 becomes larger toward the central portion side. Therefore, the exposed area of the electrode 18 increases toward the center.

【0037】図9に示す例の電極22は従来と同一である
が、電極22の側端部にマスキング板23が固着されてい
る。このマスキング板23は、中央部側において二等辺三
角形状の切欠き24が一定間隔で穿設されている。したが
って、電極22の側端部は中央部より露出面積が小さくな
っている。
The electrode 22 of the example shown in FIG. 9 is the same as the conventional one, but a masking plate 23 is fixed to the side end of the electrode 22. The masking plate 23 has isosceles notches 24 formed at regular intervals on the center side. Therefore, the exposed area of the side end portion of the electrode 22 is smaller than that of the central portion.

【0038】図10及び図11は、電流密度が約5A/dm2
越える電極の少なくとも一部が、帯状金属板の巾方向に
おいて側端に行くに従って帯状金属板との距離が長くな
るように形成した例の陽極酸化槽の断面図である。
FIGS. 10 and 11 show that at least a part of the electrode having a current density of more than about 5 A / dm 2 is arranged such that the distance from the strip-shaped metal plate becomes longer toward the side edge in the width direction of the strip-shaped metal plate. It is sectional drawing of the anodization tank of the example formed.

【0039】図10に示す例の電極25は、その上面(アル
ミニウム製品に対向する面)が中央が高く両側端が低い
二等辺三角形状に形成されている。図11に示す例の電極
27は、その上面(アルミニウム製品に対向する面)が中
央が高く両側端が低い円弧状に形成されている。
The electrode 25 of the example shown in FIG. 10 is formed into an isosceles triangle whose upper surface (the surface facing the aluminum product) has a high center and both ends are low. Example electrode shown in Figure 11
27 has an upper surface (a surface facing an aluminum product) formed in an arc shape having a high center and low side edges.

【0040】[0040]

【実施例】【Example】

陽極酸化処理する帯状金属板;長尺のJIS 1050アル
ミニウムの帯板状製品(厚み0.2mm、幅1000mm)をライ
ン搬送速度50m/分で、以下の処理を行なった。まず、
パミスー水懸濁液を研磨剤として回転ナイロンブラシで
表面を砂目立てした。この時の表面粗さ(中心線平均粗
さ)は0.5μmであった。水洗後、70℃の10%苛性ソー
ダ水溶液中でアルミニウムの溶解量が6g/m2になるよ
うにエッチングした。水洗後、30%硝酸水溶液中で中和
し、再び水洗を行なった。その後、0.7%硝酸水溶液中
で陽極時電圧13ボルト、陰極時電圧6ボルトの矩形波交
番波形を用いて(特開昭52−77702号公報実施例に記載
の電源波形)20秒間電解粗面化を行ない、20%硫酸水溶
液中で表面を洗浄した後、水洗した。
Strip-shaped metal plate to be anodized: A long JIS 1050 aluminum strip-shaped product (thickness 0.2 mm, width 1000 mm) was subjected to the following treatment at a line transfer speed of 50 m / min. First,
The surface was grained with a rotating nylon brush using the Pamisu water suspension as an abrasive. At this time, the surface roughness (center line average roughness) was 0.5 μm. After washing with water, etching was carried out in a 10% aqueous solution of caustic soda at 70 ° C. so that the amount of aluminum dissolved was 6 g / m 2 . After washing with water, the mixture was neutralized in a 30% aqueous solution of nitric acid and washed again with water. Thereafter, in a 0.7% nitric acid aqueous solution, a rectangular wave alternating waveform having a voltage of 13 V for the anode and a voltage of 6 V for the cathode was used (power supply waveform described in the example of JP-A-52-77702) for 20 seconds for electrolytic surface roughening. The surface was washed with a 20% aqueous solution of sulfuric acid, and then washed with water.

【0041】〔実施例1〕上記アルミニウム製品を、図
4に示す形態の電極を用いて陽極酸化処理した。この電
極の巾は、600mmとした。陽極酸化処理条件は、電解液
として150g/l、30℃の硫酸水溶液を用い、30秒間行っ
た。
Example 1 The above aluminum product was anodized by using the electrode having the form shown in FIG. The width of this electrode was 600 mm. The conditions of the anodizing treatment were as follows: an electrolytic solution was an aqueous solution of sulfuric acid of 150 g / l and 30 ° C. for 30 seconds.

【0042】〔実施例2〕上記アルミニウム製品を、図
10に示す形態の電極を用いて陽極酸化処理した。この電
極は、巾700mm、中央の最高点(アルミニウム製品に最
も近い点)と両端の最下点との距離が100mmとした。陽
極酸化条件は実施例1と同一である。
Example 2 The above aluminum product was
Anodizing treatment was performed using the electrode of the form shown in FIG. This electrode had a width of 700 mm, and the distance between the highest point at the center (point closest to the aluminum product) and the lowest points at both ends was 100 mm. Anodizing conditions are the same as in Example 1.

【0043】〔実施例3〕上記アルミニウム製品を、図
9に示すカバーで覆われた形態の電極を用いて陽極酸化
処理した。この電極は、巾1500mmで、カバーの内側の二
等辺三角形状の切欠は、底辺200mm、高さ300mmとした。
陽極酸化条件は実施例1と同一である。
Example 3 The above aluminum product was anodized by using an electrode covered with a cover shown in FIG. This electrode had a width of 1500 mm, and an isosceles triangular notch inside the cover had a base of 200 mm and a height of 300 mm.
Anodizing conditions are the same as in Example 1.

【0044】〔従来例1〕上記アルミニウム製品を、図
13に示す形態の電極を用いて陽極酸化処理した。この電
極の巾は、1500mmであった。陽極酸化条件は実施例1と
同一である。
[Prior Art 1] The above aluminum product is shown in FIG.
Anodization was performed using the electrode having the form shown in FIG. The width of this electrode was 1500 mm. Anodizing conditions are the same as in Example 1.

【0045】以上の実施例1〜3及び従来例1の特性を
比較した結果を表1に示す。
Table 1 shows the results obtained by comparing the characteristics of Examples 1 to 3 and Conventional Example 1 described above.

【0046】[0046]

【表1】 [Table 1]

【0047】皮膜のエッジ集中、裏廻り量は重量法で、
ヤケの発生は目視でそれぞれ評価・比較することにより
判定した。
The edge concentration of the film and the amount of backing are measured by the gravimetric method.
The occurrence of burns was judged by visual evaluation and comparison.

【0048】[0048]

【発明の効果】本発明は、電流の側端部への集中を抑制
することができるので、皮膜のエッジ集中を抑制し巾方
向の皮膜分布を均一にでき、かつ、ヤケ故障限界電流密
度を高くし高電流密度化することができる。また、電流
の裏廻りを抑制して裏面の皮膜量を減少させることがで
きるので、表面の皮膜生成効率を向上させることができ
る。
According to the present invention, since the concentration of the electric current on the side end portion can be suppressed, the edge concentration of the film can be suppressed and the film distribution in the width direction can be made uniform. Higher current density can be achieved. Further, since the backside of the electric current can be suppressed and the amount of the film on the back surface can be reduced, the efficiency of forming the film on the surface can be improved.

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

【図1】 本発明による帯状金属板の連続電解処理装置
の一例である平版印刷版用支持体の陽極酸化装置の断面
模式図。
FIG. 1 is a schematic cross-sectional view of an anodizing device for a lithographic printing plate support, which is an example of a continuous electrolytic treatment device for a strip-shaped metal plate according to the present invention.

【図2】 本発明による帯状金属板の連続電解処理装置
の他の例である平版印刷版用支持体の電解の平面図。
FIG. 2 is a plan view of electrolysis of a lithographic printing plate support which is another example of the continuous electrolytic treatment apparatus for strip-shaped metal plates according to the present invention.

【図3】 図2中A−A線断面図。3 is a sectional view taken along line AA in FIG.

【図4】 図2中B−B線断面図。FIG. 4 is a sectional view taken along line BB in FIG.

【図5】 本発明による帯状金属板の連続電解処理装置
の他の例である電極平面図。
FIG. 5 is a plan view of an electrode as another example of the continuous electrolytic treatment apparatus for strip-shaped metal plates according to the present invention.

【図6】 本発明による帯状金属板の連続電解処理装置
の他の例である電極部分の部分平面図。
FIG. 6 is a partial plan view of an electrode portion which is another example of the continuous electrolytic treatment apparatus for strip-shaped metal plates according to the present invention.

【図7】 本発明による帯状金属板の連続電解処理装置
の他の例である電極部分の部分平面図。
FIG. 7 is a partial plan view of an electrode portion which is another example of the continuous electrolytic treatment apparatus for a strip-shaped metal plate according to the present invention.

【図8】 本発明による帯状金属板の連続電解処理装置
の他の例である電極部分の部分平面図。
FIG. 8 is a partial plan view of an electrode portion which is another example of the continuous electrolytic treatment apparatus for strip-shaped metal plates according to the present invention.

【図9】 本発明による帯状金属板の連続電解処理装置
の他の例である陽極酸化槽の断面図。
FIG. 9 is a sectional view of an anodizing tank which is another example of the continuous electrolytic treatment apparatus for strip-shaped metal plates according to the present invention.

【図10】 本発明による帯状金属板の連続電解処理装置
の他の例である電極部分の部分平面図。
FIG. 10 is a partial plan view of an electrode portion which is another example of the continuous electrolytic treatment apparatus for a strip-shaped metal plate according to the present invention.

【図11】 本発明による帯状金属板の連続電解処理装置
の他の例である陽極酸化槽の断面図。
FIG. 11 is a sectional view of an anodizing tank which is another example of the continuous electrolytic treatment apparatus for strip-shaped metal plates according to the present invention.

【図12】 従来の平版印刷版用支持体の陽極酸化装置の
断面模式図。
FIG. 12 is a schematic cross-sectional view of a conventional anodizing device for a lithographic printing plate support.

【図13】 従来の平版印刷版用支持体の陽極酸化装置の
電極の平面図。
FIG. 13 is a plan view of an electrode of a conventional anodizing device for a lithographic printing plate support.

【符号の説明】[Explanation of symbols]

8,11,18,22,25,27…電極 9,12…巾広電極部 10,13…巾狭電極部 16…切欠き 15,19,23…マスキング板 20…穴 24…切欠き 8, 11, 18, 22, 22, 25, 27 ... Electrodes 9, 12 ... Wide electrode section 10, 13 ... Narrow electrode section 16 ... Notches 15, 19, 23 ... Masking plate 20 ... Hole 24 ... Notch

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】電解液と、該電解液中に設けられた電極と
を有し、電解液中に帯状金属板を走行させて帯状金属板
を電解処理する装置において、電流密度が約5A/dm2
越える電極の少なくとも一部の有効面積を、電流密度が
約5A/dm2を越えない電極の有効面積より小さくするこ
とを特徴とする電解処理装置
1. An apparatus having an electrolytic solution and an electrode provided in the electrolytic solution, wherein a strip-shaped metal plate is run in the electrolytic solution to electrolytically treat the strip-shaped metal plate, and a current density is about 5 A / An electrolytic treatment apparatus characterized in that the effective area of at least a part of the electrodes exceeding dm 2 is made smaller than the effective area of the electrodes whose current density does not exceed about 5 A / dm 2.
【請求項2】 電流密度が約5A/dm2を越える電極の少
なくとも一部の巾が、電流密度が約5A/dm2を越えない
電極の巾及び帯状金属板の巾より小さく形成されている
請求項1に記載の連続電解処理装置
At least a portion of the width of 2. A current density exceeds about 5A / dm 2 electrode is smaller than the width of the width and the strip metal plate electrode current density does not exceed about 5A / dm 2 The continuous electrolytic treatment apparatus according to claim 1.
【請求項3】 電解液と、該電解液中に設けられた電極
とを有し、電解液中に帯状金属板を走行させて帯状金属
板を電解処理する装置において、電流密度が約5A/dm2
を越える電極の少なくとも一部が、帯状金属板の巾方向
において側端に行くに従って帯状金属板との距離が長く
なるように形成されていることを特徴とする連続電解処
理装置
3. An apparatus comprising an electrolytic solution and an electrode provided in the electrolytic solution, wherein a strip-shaped metal plate is run in the electrolytic solution to electrolytically treat the strip-shaped metal plate, and the current density is about 5 A / dm 2
At least a part of the electrode exceeding the distance is formed so that the distance from the strip-shaped metal plate becomes longer toward the side end in the width direction of the strip-shaped metal plate.
JP25617192A 1992-09-25 1992-09-25 Continuous electrolyzer Expired - Fee Related JP2946445B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25617192A JP2946445B2 (en) 1992-09-25 1992-09-25 Continuous electrolyzer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25617192A JP2946445B2 (en) 1992-09-25 1992-09-25 Continuous electrolyzer

Publications (2)

Publication Number Publication Date
JPH06108290A true JPH06108290A (en) 1994-04-19
JP2946445B2 JP2946445B2 (en) 1999-09-06

Family

ID=17288900

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25617192A Expired - Fee Related JP2946445B2 (en) 1992-09-25 1992-09-25 Continuous electrolyzer

Country Status (1)

Country Link
JP (1) JP2946445B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012167295A (en) * 2011-02-09 2012-09-06 Nisshin Steel Co Ltd Method for constructing electroplating equipment, and method and apparatus for producing electroplated steel sheet

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012167295A (en) * 2011-02-09 2012-09-06 Nisshin Steel Co Ltd Method for constructing electroplating equipment, and method and apparatus for producing electroplated steel sheet

Also Published As

Publication number Publication date
JP2946445B2 (en) 1999-09-06

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