JPH0215198A - Electrolytic device - Google Patents
Electrolytic deviceInfo
- Publication number
- JPH0215198A JPH0215198A JP16490788A JP16490788A JPH0215198A JP H0215198 A JPH0215198 A JP H0215198A JP 16490788 A JP16490788 A JP 16490788A JP 16490788 A JP16490788 A JP 16490788A JP H0215198 A JPH0215198 A JP H0215198A
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- counter electrode
- web
- electrolytic
- 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.)
- Granted
Links
- 239000000463 material Substances 0.000 claims abstract description 9
- 239000000243 solution Substances 0.000 claims description 5
- 229910021645 metal ion Inorganic materials 0.000 claims description 3
- 239000008151 electrolyte solution Substances 0.000 claims description 2
- 239000003792 electrolyte Substances 0.000 abstract description 37
- 238000000034 method Methods 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 5
- 238000005868 electrolysis reaction Methods 0.000 abstract description 4
- 229910052782 aluminium Inorganic materials 0.000 description 8
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 8
- 229910052751 metal Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 238000007639 printing Methods 0.000 description 7
- 239000007788 liquid Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- 239000012212 insulator Substances 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 238000007788 roughening Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000000866 electrolytic etching Methods 0.000 description 3
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 238000005530 etching Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 238000007645 offset printing Methods 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000010186 staining Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野]
本発明は、電解処理装置においての電解液補給口に関す
るものであり、金属ウェブの交番電流による粗面化に適
し、特に、オフセット印刷版用に適する粗面化されたア
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 electrolyte replenishment port in an electrolytic processing apparatus, and is suitable for roughening the surface of a metal web by alternating current, and is particularly suitable for use in offset printing plates. The present invention relates to an electrolytic treatment apparatus for a printing plate support made of a roughened aluminum plate suitable for use in the present invention.
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.
このためには、アルミニウム板の表面を、均一かつ緻密
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とき、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。For this purpose, the surface of the aluminum plate must be roughened to have uniform and dense grains. This surface roughening treatment has a significant effect on the printing performance such as staining performance of the plate material when printing is actually performed, so its quality is an important factor in the production of the plate material.
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、例えばボールグレイン、
ワイヤーグレイン ブラック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布て方法としては、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
殊交番電流が用いられている。またこの電気化学的砂目
布ての前処理として、苛性ソーダなとでエツチング処理
をしても良い。Examples of mechanical graining methods include ball grain,
There are wire grain black grain liquid honing methods. Furthermore, as the electrochemical graining method, an alternating current electrolytic etching method is generally employed, and the current used is a special alternating current such as an ordinary sine wave alternating current or a rectangular wave. Further, as a pretreatment of this electrochemical grained cloth, 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
によって生しる現象と異なり炭素や金属などによる対極
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 alternating current electrolytic etching method has a problem in that, unlike the phenomenon caused by direct current, the counter electrode made of carbon, metal, etc. is extremely susceptible to deterioration. For example, if carbon is used as a counter electrode, redox reactions are repeated every time the polarity changes, causing severe deterioration of the binder and 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り
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2図
に示すように、被処理材である金属ウェブ1がドラムロ
ーラ2の円周で支持され対向する主対極3a、3bとの
間に電解液供給114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06から111出することによ
って満し主対極3a、3bには交流型[7より交番電流
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との対極を主対局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−I
・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だめのダイオード
9又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。In order to solve such problems, Japanese Patent Publication No. 61-48596 discloses a method in which a circuit for an auxiliary counter electrode is connected in parallel to a circuit connected to a main counter electrode, and the flow of anode current to the main counter electrode is controlled. An electrolytic treatment apparatus is disclosed in which a diode or a mechanism acting like a diode is provided in a circuit for an auxiliary counter electrode. For example, as shown in FIG. 2, a metal web 1, which is a material to be treated, is supported around the circumference of a drum roller 2, and an electrolytic treatment solution containing metal ions is supplied between an electrolyte supply 114 and opposing main counter electrodes 3a and 3b. The main counter electrodes 3a and 3b are supplied with alternating current from the main counter electrodes 3a and 3b. A counter electrode to the web 1 is formed by the main counter electrodes 3a, 3b and the auxiliary counter electrode 8, and a circuit for the auxiliary counter electrode 8 is connected in parallel to the circuit connected to the main counter electrodes 3a, 3b.
- An electrolytic treatment device in which the circuits for the main counter electrode of the current are connected in parallel, and a diode 9 for controlling the flow of the anode current at the main counter electrode or a mechanism acting like a diode is provided in the circuit for the auxiliary counter electrode 8 to flow the current. be.
この際主対極3a、3bばお互いに反対の極性をもつも
ので電源7には互いに反対側に結線されており、更に主
対極3a、3bば夫々多数本の(例えばn−10〜14
本)の小電極(3a1.3az3a3 H+ ・3an
、)(3b+、3bz、3b:+ ・・・3 bn)
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。At this time, the main counter electrodes 3a and 3b have opposite polarities and are connected to the power source 7 on opposite sides, and each of the main counter electrodes 3a and 3b has a large number of wires (for example, n-10 to 14
small electrode (3a1.3az3a3 H+ ・3an
, ) (3b+, 3bz, 3b:+ ...3 bn)
are constructed with an insulator 10 as their boundary, and are devised to increase current efficiency.
しかしながら、従来は電解液供給口4は1ケ所でありこ
!から補給された電解液ば金属ウェブ1と電極3a、3
bとの間の定められた狭い空間の間(例えば10mm)
を通ってドラムローラ2の反対側に流れ電解液排出口6
に出て行くので、流路におりる電解によって次第に電解
液が疲労し主対極の初めと、終りでは電解液が疲労して
その成分に差が出てきて充分な電解効率が得られない。However, in the past, there was only one electrolyte supply port 4! The electrolyte supplied from the metal web 1 and the electrodes 3a, 3
a narrow space (e.g. 10 mm) between
through the electrolyte outlet 6 to the opposite side of the drum roller 2
Therefore, the electrolyte is gradually fatigued by the electrolysis that flows into the flow path, and the electrolyte is fatigued at the beginning and end of the main counter electrode, resulting in a difference in its components, making it impossible to obtain sufficient electrolytic efficiency.
また液の入口と出口との温度差が大きくなり所望の砂目
が得られなかった。Furthermore, the temperature difference between the inlet and outlet of the liquid became large, making it impossible to obtain the desired grain.
本発明の目的は、従来の問題点を解消し電解効率の良い
電解処理装置を提供するものである。SUMMARY OF THE INVENTION An object of the present invention is to solve the conventional problems and provide an electrolytic treatment apparatus with high electrolytic efficiency.
〔課題を解決するための手段及び作用〕すなわち、本発
明の上記目的は金属イオンを含む電解処理液中で、被処
理材と対極との間に交番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、電解液供給口を、該対極
間の2ケ所以」二に設けることを特徴とする電解処理方
法によって達成される。[Means and effects for solving the problem] That is, the above object of the present invention is to perform electrochemical treatment by supplying an alternating current between a material to be treated and a counter electrode in an electrolytic treatment solution containing metal ions. This is achieved by an electrolytic treatment method characterized in that the electrolytic treatment apparatus is provided with electrolyte supply ports at two locations between the counter electrodes.
本発明Qこおける電解液供給口を対極間の2ケ所以上G
こ設けるということば、電解液通路で電解液が疲労して
電解効率が下らない様に2ケ所以」二の必要ケ所に電解
液供給口を設りることを意味する。In the present invention, the electrolyte supply port in Q is placed at two or more locations between the counter electrodes.
The provision of this means that electrolyte supply ports are provided at two or more necessary locations to prevent electrolysis efficiency from decreasing due to fatigue of the electrolyte in the electrolyte passage.
又電解液供給口としてはスリット給液ノズルが好ましい
。Further, as the electrolyte supply port, a slit liquid supply nozzle is preferable.
以下図を用いて実施態様を説明する。第1図は本発明の
電解処理方法の1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トラムローラでありウェ
ブと主対極3a、3b、及び補助対極8とのクリアラン
スは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.IHz〜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、3a、3bの主対極の劣化が1
5 Hz以下であると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56−1
9280号、特公昭55−191.91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
てあり、これにより、8の補助対極に流れる電流を制御
する。Embodiments will be described below using figures. FIG. 1 shows one embodiment of the electrolytic treatment method of the present invention. 1 is a metal web, and 2 is a radial tram roller supporting the web, which runs while maintaining constant clearances between the web and the main counter electrodes 3a, 3b and the auxiliary counter electrode 8. Clearance is usually
Approximately 3 to 50 mm is appropriate. 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. An AC power source of IHz to 500 Hz is used. The frequency is changed depending on the desired etching form, but the deterioration of the main opposite electrodes of 3a and 3b is 1
If it is 5 Hz or less, it is large, especially in the case of carbon. There are various waveforms, but the
It is also possible to use the special alternating waveforms described in Japanese Patent Publication No. 9280 and Japanese Patent Publication No. 55-191.91. A diode 9 controls the current flowing to the auxiliary counter electrode 8.
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。As the material for the auxiliary counter electrode 8, it is preferable to use platinum, which is resistant to deterioration.
本発明の電解液供給[」4としては例えば従来のものを
4aとすると、主対極3aの中間の小電極の間に絶縁体
10を挾んで電解液供給口4b、主対極3aと主対極3
bとの境界にやはり絶縁体10を挿し挟んで電解液供給
口4c更に主対極3bの中間に前記同様な方法で電解液
供給口4dを設けたものである。As the electrolyte supply port 4 of the present invention, for example, if the conventional one is 4a, an insulator 10 is sandwiched between the small electrode in the middle of the main counter electrode 3a, and the electrolyte supply port 4b is connected to the main counter electrode 3a and the main counter electrode 3a.
An insulator 10 is also inserted between the main counter electrode 3b and an electrolyte supply port 4c, and an electrolyte supply port 4d is provided in the same manner as described above in the middle of the main counter electrode 3b.
各電解液供給口では、電解処理液5は給液管]1より電
解液供給口4内に入り、ディストリビュータ12により
ドラムローラの幅方向全体に均一に分布するようキャビ
ティ13に入り、スリット14より電解槽15の中に噴
出される。これによって電解槽の中の電解液濃度の均−
性及び攪拌効果が良くなり電解効率か上Wするのである
。At each electrolyte supply port, the electrolytic treatment solution 5 enters the electrolyte supply port 4 through the supply pipe 1, enters the cavity 13 by the distributor 12 so as to be uniformly distributed over the entire width direction of the drum roller, and enters the cavity 13 through the slit 14. It is ejected into the electrolytic cell 15. This allows the electrolyte concentration in the electrolytic cell to become even.
This improves the electrolytic efficiency and stirring effect, leading to an increase in electrolytic efficiency.
実施例−1
第1図のような装置を用いて、電解液供給口を4a、4
b、4C,4dから電解液合計4000p、/minを
供給した。Example-1 Using the device shown in Figure 1, the electrolyte supply ports 4a, 4
A total of 4000 p/min of electrolyte solution was supplied from b, 4C, and 4d.
主対極:カーボン
補助対極:白金
ウェブとのその対極のクリアランス゛10mm主対極の
電解液条件: 液種 硝酸濃度 50g//!
温度 60°C
補助対極の電解液条件: 液種 硝酸濃度 50
g/ffi
温度 20’C
アルミウェブ巾 ]、 000 mm処理スピード
15m/min
周波数 100Hz
以上の条件で砂目立てを行ったところ、入口濃度50
g/C出口濃度48 g#2であり砂目も均一に生した
。Main counter electrode: Carbon Auxiliary counter electrode: Clearance between the counter electrode and the platinum web ゛10mm Main counter electrode electrolyte conditions: Liquid type Nitric acid concentration 50g//! Temperature: 60°C Electrolyte conditions for auxiliary counter electrode: Liquid type: Nitric acid concentration: 50
g/ffi Temperature 20'C Aluminum web width ], 000 mm Processing speed
When graining was carried out at a speed of 15m/min and a frequency of 100Hz or higher, the inlet concentration was 50%.
The g/C outlet concentration was 48 g#2, and grains were uniform.
比較例
実施例と同じ条件でFig2の装置で行い、電解液の供
給が2500ρ/ m i nが限界であり出口濃度も
40g/Eに低下し砂目も不均一であった。Comparative Example Comparison was carried out using the apparatus shown in Fig. 2 under the same conditions as in the example, and the electrolyte supply was limited to 2500 ρ/min, the outlet concentration was reduced to 40 g/E, and the grain was non-uniform.
上記実施例から明らかな様に、本発明の主対極の電解液
供給口を被処理材と対極との間の2ケ所以上に必要数設
けることによって電解効率が上昇し生産速度が上昇する
とともに金属ウェブの幅方向の砂Hの均一性が一層良化
し、品質向上にも寄与した。As is clear from the above examples, by providing the required number of electrolyte supply ports for the main counter electrode of the present invention at two or more locations between the material to be treated and the counter electrode, the electrolytic efficiency is increased, the production speed is increased, and the metal The uniformity of the sand H in the width direction of the web was further improved, contributing to improved quality.
第1図は本発明の電解処理装置の1実施例の側面図、第
2図は従来の電解処理装置の一例の側面図である。
1・・・金属ウェブ
2・・・ラジアル1′ラムローラ
3a、3b・・・主対極
4a
4b、4c・・・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・・
10・・・絶縁体 11
12・・・ディス1−リビュータ
13・・・キャビティ 14゜
・ダイオード
・・供給管
・・スリットFIG. 1 is a side view of one embodiment of the electrolytic treatment apparatus of the present invention, and FIG. 2 is a side view of an example of a conventional electrolytic treatment apparatus. 1... Metal web 2... Radial 1' ram roller 3a, 3b... Main counter electrode 4a 4b, 4c... Electrolyte supply port 5... Electrolyte treatment solution 6... Electrolyte discharge port 7. ... AC power supply 8 ... Auxiliary counter electrode 9 ... 10 ... Insulator 11 12 ... Dis 1-rebuter 13 ... Cavity 14° - Diode ... Supply tube ... Slit
Claims (1)
間に交番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、電解液供給口を該対極間の2ケ所以上に
設けることを特徴とする電解処理装置。An electrolytic treatment apparatus that performs electrochemical treatment by supplying an alternating current between a material to be treated and a counter electrode in an electrolytic treatment solution containing metal ions, the electrolytic solution supply ports being provided at two or more locations between the counter electrodes. An electrolytic treatment device characterized by being provided in.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63164907A JP2767699B2 (en) | 1988-07-04 | 1988-07-04 | Electrolytic treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63164907A JP2767699B2 (en) | 1988-07-04 | 1988-07-04 | Electrolytic treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0215198A true JPH0215198A (en) | 1990-01-18 |
JP2767699B2 JP2767699B2 (en) | 1998-06-18 |
Family
ID=15802131
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63164907A Expired - Fee Related JP2767699B2 (en) | 1988-07-04 | 1988-07-04 | Electrolytic treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2767699B2 (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52133839A (en) * | 1976-05-05 | 1977-11-09 | Hoechst Ag | Continuous electrolytic treating process for metal strip and apparatus therefor |
JPS5996294A (en) * | 1982-11-26 | 1984-06-02 | Nippon Steel Corp | Electrolytic surface treatment of strip |
JPS6017098A (en) * | 1983-07-08 | 1985-01-28 | Nippon Steel Corp | Electrolytic treating method of steel strip |
-
1988
- 1988-07-04 JP JP63164907A patent/JP2767699B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52133839A (en) * | 1976-05-05 | 1977-11-09 | Hoechst Ag | Continuous electrolytic treating process for metal strip and apparatus therefor |
JPS5996294A (en) * | 1982-11-26 | 1984-06-02 | Nippon Steel Corp | Electrolytic surface treatment of strip |
JPS6017098A (en) * | 1983-07-08 | 1985-01-28 | Nippon Steel Corp | Electrolytic treating method of steel strip |
Also Published As
Publication number | Publication date |
---|---|
JP2767699B2 (en) | 1998-06-18 |
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