JPH0149797B2 - - Google Patents

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Publication number
JPH0149797B2
JPH0149797B2 JP3604785A JP3604785A JPH0149797B2 JP H0149797 B2 JPH0149797 B2 JP H0149797B2 JP 3604785 A JP3604785 A JP 3604785A JP 3604785 A JP3604785 A JP 3604785A JP H0149797 B2 JPH0149797 B2 JP H0149797B2
Authority
JP
Japan
Prior art keywords
plating
liquid
plated
flow
liquid flow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP3604785A
Other languages
Japanese (ja)
Other versions
JPS61195996A (en
Inventor
Koichi Kayane
Hiromichi Yoshida
Shigeo Hagitani
Norio Okabe
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.)
Hitachi Cable Ltd
Original Assignee
Hitachi Cable 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 Hitachi Cable Ltd filed Critical Hitachi Cable Ltd
Priority to JP3604785A priority Critical patent/JPS61195996A/en
Publication of JPS61195996A publication Critical patent/JPS61195996A/en
Publication of JPH0149797B2 publication Critical patent/JPH0149797B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

[産業上の利用分野] 本発明は、液流式めつき方法、特にストライプ
めつき条の高速めつきの方法に関するものであ
る。 [従来の技術] 従来、帯状導体等の全面めつき又はストライプ
状部分めつきでは、被めつき処理物を殆どめつき
槽中を浸漬走行させてめつきする方法や、液をわ
ずかに噴流させてめつきする方法が行われている
が、それでもめつき速度の向上には限界がある。
めつき速度を上げるため、めつき電流密度を増加
していくと、それがある値以上になるとめつき品
質が劣化し、実用できなくなる限界電流密度が存
在する。 この限界電流密度を向上する一つの方法とし
て、被めつき面にめつき液を高速で吹き付けて攪
拌する方法があるが、或る程度以上広いめつき面
になるとめつき液を全面均一に攪拌することが困
難となり、めつきむらを生じたり、部分的に品質
不良個所を生じたりする。 特に、帯状導体等の全面めつき又は、ストライ
プ状部分めつき等では、液中でのめつき液の攪拌
効果を上げるために、第4図に示すように、一般
的に一定形状を有するノズル孔(例えば、パイプ
4の長手方向に一定ピツチであけられた孔5)か
らめつき液を被めつき物15に対して噴射する方
法等が取られている。この噴射方式によると、め
つき液の直接当たる部分では攪拌効果が得られる
ため、限界電流密度を上げることができるが、被
めつき物の幅方向についてみた場合、噴射の当た
る部分と当たらない部分の差ができ易く、攪拌が
不均一になりやすい。従つて、めつき面積が広く
なつてもめつき液を全面均一に攪拌でき、めつき
むらを生ぜず限界電流密度を向上することができ
る高速めつきの開発が切望されている。 これらの諸問題を解決することができる高速め
つき法として、本出願人は、特許願昭和59年6月
8日の液流下式めつき方法(特願昭59−118682
号)を出願した。このめつき方法は、液流下式で
あるため、めつき面積が広くなつても、帯状体の
幅方向に対してめつき液を全面均一に攪拌でき、
めつきむらが生ぜず限界電流密度を向上すること
ができる有効なめつき方法の一つであるが、次の
ような問題点も持つている。 即ち、液流下方式で高速めつき液流を得るため
には、ヘツド差を大きく取る必要があるので、め
つき槽の構造が、従来の浸漬法に比べて大きくな
りめつき液量が増える。又、めつき液流速が速く
なると上部めつき槽液面からの空気の巻き込みが
増え、めつき液の劣化及びめつき品質に悪影響を
及ぼし易い欠点も持ち合わせているため、高電流
密度を得るための流速にやはり限界があつた。 [発明が解決しようとする問題点] 本発明の目的は、前記した従来技術の欠点を解
消し、めつきの高速化を図ることができる新規な
液流式めつき方法を提供することにある。 [問題点を解決するための手段] 本発明は被めつき処理物を、壁面によつて形成
されるめつき槽内の液管路中に配置してめつきを
行うに際し、前記液管路の軸線方向のめつき液流
と、前記軸線方向にほぼ直角をなす方向のめつき
液流との合成めつき液流を被めつき処理物に噴射
してめつきを行うことを特徴とする液流式めつき
方法を提供するものである。 ここで、前記被めつき処理物が、その広幅面を
ほぼ垂直状態に維持しながら前記液管路中を被め
つき処理物の長手方向に移動する帯状体である液
流式めつき方法であることが好ましい。 [発明の構成] 本発明の液流式めつき方法を図面に示す好適実
施例について詳細に説明する。本発明の液流式め
つき法を実施する装置は、第1めつき槽1内に設
置された流路壁3によつて構成される液管路18
を備える。この液管路18の流路壁3の壁面及
び/又は壁面近傍にはめつき液噴射孔5が設置さ
れている。このめつき液噴射孔5は、第1図に示
すように噴射用パイプ4の側壁にあけられた噴流
孔5でもよいし、第1図に示してはいないが液管
路18の流路壁3にあけられた噴射孔でもよい
し、又パイプ4及び流路壁3に噴射孔を同時に設
けてもよい。後述の噴射流9を実現できるもので
あればいかなる形式であつてもよい。 高速めつきを行うには、めつき面、特に第3図
に示すような部分めつき部17でめつき液をいか
に激しく攪拌させて、めつき面の拡散層を薄くす
るかが重要な手段になる。従来は、第4図に示す
ように、めつき槽1内に保持される被めつき処理
物15に対してめつき槽1内に設置されためつき
液噴射用パイプ4の噴射孔5から、めつき液を噴
射させる攪拌方式が用いられていたが、この攪拌
方式では攪拌力が液中で分散されやすく、高速め
つきに必要な十分な攪拌効果が得にくい。 本発明では、第1めつき槽1内に設けた流路壁
3により液管路18を構成し、液管路底部より一
定圧力の攪拌流8を液管路18内に供給し、同時
に流路壁3及び/又は流路壁3近傍にめつき液噴
射孔5を設け、攪拌流とほぼ直角方向に噴射流9
を供給し、この攪拌流8と噴射流9の合成された
めつき液流10を作り出し、めつき液流10の中
に被めつき処理物15をさらしてめつき速度を向
上させるものである。 第2図は、第1図の第1めつき槽の概略図を示
したものであるが、第2図のように流路壁3下方
にこのような攪拌流8用の容器14を設けてもよ
く、第1図のような液管路18を使用してもよ
い。合成されためつき液流10はめつき後第1め
つき槽に設けられためつき液流出口12から流出
するたる めつき液流を均一に循環させるために、第1図
に示すように、第2めつき槽2を設け、第1めつ
き槽に設けられためつき液流出口12からめつき
液を第2めつき槽2へオーバーフローさせ、第2
めつき槽2にプールし、第2めつき槽2底部と第
1めつき槽底部を管路11で連通し、管路11内
にポンプを設けてめつき液を循環させるのが好ま
しい。 攪拌流8は、第2めつき槽の底部からポンプ7
を経て液管路18に供給され、噴射液9は、第2
めつき槽底部から図示していない流路を経て噴射
用パイプ4にポンプを経て供給される。 第3図は、被めつき処理物15の断面図であ
る。第3図に示すような被めつき処理物15が、
その広幅面をほぼ垂直状態に維持しながら、長手
方向に移動する帯状体であり、この帯状体を第1
図の紙面に垂直方向に走行させつつめつきを行う
場合に本発明の効果が著しい。第3図では2条同
時にめつきする部分めつき用マスキングテープ1
6で一部を覆つた外観を図示してあるが部分めつ
きの態様はいかなるものでもよく、又被めつき処
理物15も帯状体に限定されることなく、線状
体、塊状態を用いてもよい。 [実施例] 次に具体的な実施条件に基づく本発明液流式め
つき方法の実施例を説明する。 被めつき処理物15としては、第3図に示す断
面形状の帯状体を用い、同図に示すマスキングテ
ープ16を用いて前処理後2条同時に片面部分銀
めつきを行つた。帯状体の寸法、形状は幅65mm、
厚さ0.5mmであり、ストライプ状部分めつき部1
7の幅は上下とも夫々8mmである。めつき条件
は、めつき液としてAgCN80g/、KCN100
g/のシアン化銀めつき液を用い、液温25℃で
銀めつきの厚さが1μmとなるようにめつきを行
つた。 ここで、比較例1として、上記と同じ条件でめ
つきを行い、但し、この場合第4図に示すように
めつき液噴射用パイプ4を用いると共に、前記め
つき液噴射用パイプ4により被めつき処理物15
のめつき面近傍におけるめつき液流速を1.0〜1.2
m/秒とした。 更に、比較例2として、やはり上記と同じ条件
でめつきを行い。但し、この場合第1図において
液管路18を用いるがめつき液噴射用パイプ4を
用いない方法でめつきを行うと共に、液管路18
内におけるめつき液流速を1.0〜1.2m/秒とし
た。 さて、本実施例においては、上記した条件に加
えて、比較例1及び2において用いられためつき
液噴射用パイプ(めつき面近傍におけるめつき液
流速1.0〜1.2m/秒)及び液管路18(めつき液
流速1.0〜1.2m/秒)の両方を用いて、第1図に
示す装置の中でめつきを行つた。 その結果を表1に示す。
[Industrial Field of Application] The present invention relates to a liquid flow plating method, particularly to a method for high-speed plating of striped plating strips. [Prior Art] Conventionally, in the case of full-surface plating or stripe-like partial plating of strip-shaped conductors, etc., there have been methods in which the object to be plated is immersed and run through a plating tank, or a method in which a liquid is slightly jetted is applied. Although a method of plating with a hand has been used, there is still a limit to the improvement of the plating speed.
When the plating current density is increased in order to increase the plating speed, there is a limit current density at which the plating quality deteriorates and becomes unpractical when it exceeds a certain value. One way to improve this limiting current density is to spray the plating liquid onto the surface to be plated at high speed and stir it, but if the plated surface is larger than a certain extent, it is necessary to uniformly stir the plating liquid over the entire surface. This may result in uneven plating or partial quality defects. In particular, for full-surface plating of strip-shaped conductors or striped partial plating, in order to improve the stirring effect of the plating solution in the solution, a nozzle with a fixed shape is generally used, as shown in Figure 4. A method has been adopted in which the plating liquid is injected onto the object to be plated 15 through holes (for example, holes 5 formed at a constant pitch in the longitudinal direction of the pipe 4). According to this injection method, the limiting current density can be increased because a stirring effect is obtained in the areas that are directly hit by the plating liquid, but when looking at the width direction of the object to be plated, there are areas that are hit by the jet and areas that are not hit by the jet. Differences may easily occur, and stirring tends to be uneven. Therefore, there is a strong need for the development of high-speed plating that can uniformly stir the plating liquid over the entire surface even if the plating area is increased, and that can improve the critical current density without causing uneven plating. As a high-speed plating method capable of solving these problems, the present applicant has proposed a liquid flow plating method (patent application No. 118682, filed on June 8, 1982).
No.) was filed. Since this plating method uses a liquid flow down method, even if the plating area is large, the plating liquid can be uniformly stirred over the entire surface in the width direction of the strip.
Although this is an effective plating method that can improve the critical current density without causing uneven plating, it also has the following problems. That is, in order to obtain a high-speed plating liquid flow with the liquid flow method, it is necessary to have a large head difference, so the structure of the plating tank is larger than that in the conventional dipping method, and the amount of plating liquid increases. In addition, when the plating liquid flow rate increases, air entrainment from the upper plating tank liquid level increases, which has the disadvantage that it tends to deteriorate the plating liquid and adversely affect the plating quality. Therefore, in order to obtain a high current density, There was still a limit to the flow velocity. [Problems to be Solved by the Invention] An object of the present invention is to provide a novel liquid flow plating method that can eliminate the drawbacks of the prior art described above and increase the speed of plating. [Means for Solving the Problems] The present invention provides that when plating is performed by arranging the object to be plated in a liquid pipe line in a plating tank formed by a wall surface, the liquid pipe line Plating is carried out by injecting a synthetic plating liquid flow, which is a plating liquid flow in the axial direction and a plating liquid flow in a direction substantially perpendicular to the axial direction, onto the object to be plated. A liquid flow plating method is provided. Here, in the liquid flow plating method, the object to be plated is a belt-like body that moves in the longitudinal direction of the object to be plated in the liquid pipe path while maintaining its wide side in a substantially vertical state. It is preferable that there be. [Structure of the Invention] A preferred embodiment of the liquid flow plating method of the present invention shown in the drawings will be described in detail. The apparatus for carrying out the liquid flow plating method of the present invention includes a liquid pipe line 18 configured by a flow passage wall 3 installed in a first plating tank 1.
Equipped with. A plating liquid injection hole 5 is installed on the wall surface and/or near the wall surface of the flow path wall 3 of this liquid pipe path 18 . The plating liquid injection hole 5 may be a jet hole 5 formed in the side wall of the injection pipe 4 as shown in FIG. The injection holes may be provided in the pipe 4 and the flow path wall 3 at the same time. It may be of any type as long as it can realize the jet flow 9 described later. In order to perform high-speed plating, it is important to violently stir the plating solution on the plating surface, especially in the partial plating section 17 as shown in FIG. 3, to thin the diffusion layer on the plating surface. become. Conventionally, as shown in FIG. 4, the object to be plated 15 held in the plating tank 1 is sprayed from the injection hole 5 of the plating liquid injection pipe 4 installed in the plating tank 1. A stirring method in which the plating liquid is sprayed has been used, but in this stirring method, the stirring force is easily dispersed in the liquid, making it difficult to obtain a sufficient stirring effect necessary for high-speed plating. In the present invention, the liquid pipe line 18 is configured by the flow passage wall 3 provided in the first plating tank 1, and the stirring flow 8 at a constant pressure is supplied into the liquid pipe line 18 from the bottom of the liquid pipe line, and the flow is simultaneously A plating liquid injection hole 5 is provided in the vicinity of the channel wall 3 and/or the channel wall 3, and a jet stream 9 is provided in the vicinity of the channel wall 3 and/or the channel wall 3.
A plating liquid stream 10 is created by combining the stirring stream 8 and the jet stream 9, and the object to be plated 15 is exposed to the plating liquid stream 10 to improve the plating speed. FIG. 2 shows a schematic diagram of the first plating tank shown in FIG. 1, but as shown in FIG. Alternatively, a liquid conduit 18 as shown in FIG. 1 may be used. After plating, the synthesized plating liquid flow 10 flows out from the plating liquid outlet 12 provided in the first plating tank. A plating tank 2 is provided, and the plating liquid is caused to overflow from the plating liquid outlet 12 provided in the first plating tank to the second plating tank 2.
It is preferable to pool the plating liquid in the plating tank 2, to communicate the bottom of the second plating tank 2 and the bottom of the first plating tank through a pipe line 11, and to provide a pump in the pipe line 11 to circulate the plating liquid. The stirring flow 8 is passed from the bottom of the second plating tank to the pump 7.
The injected liquid 9 is supplied to the liquid pipe line 18 through the second
It is supplied from the bottom of the plating tank through a flow path (not shown) to the injection pipe 4 via a pump. FIG. 3 is a sectional view of the plated object 15. As shown in FIG. The coated material 15 as shown in FIG.
It is a belt-shaped body that moves in the longitudinal direction while maintaining its wide side in a nearly vertical state, and this belt-shaped body is
The effect of the present invention is remarkable when pinning is performed while traveling perpendicularly to the plane of the drawing. Figure 3 shows masking tape 1 for partial plating where two strips are plated at the same time.
Although the partially covered appearance is shown in 6, any form of partial plating may be used, and the plated object 15 is not limited to a band-like object, but may be a linear object or a lump-like object. Good too. [Example] Next, an example of the liquid flow plating method of the present invention will be described based on specific implementation conditions. A strip having the cross-sectional shape shown in FIG. 3 was used as the plated object 15, and after pretreatment, two strips were partially silvered on one side at the same time using masking tape 16 shown in the same figure. The dimensions and shape of the strip are 65mm wide.
The thickness is 0.5mm, and the striped part plating part 1
The width of No. 7 is 8 mm at the top and bottom. The plating conditions are AgCN80g/, KCN100 as plating liquid.
Plating was carried out using a silver cyanide plating solution of 1.5 g/g at a solution temperature of 25.degree. C. so that the thickness of the silver plating was 1 .mu.m. Here, as Comparative Example 1, plating was carried out under the same conditions as above, except that in this case, as shown in FIG. 4, the plating liquid injection pipe 4 was used, and the Plated product 15
Set the plating liquid flow rate near the plating surface to 1.0 to 1.2.
m/sec. Furthermore, as Comparative Example 2, plating was performed under the same conditions as above. However, in this case, in FIG.
The flow rate of the plating liquid in the chamber was 1.0 to 1.2 m/sec. Now, in this example, in addition to the above-mentioned conditions, the plating liquid injection pipe used in Comparative Examples 1 and 2 (plating liquid flow rate 1.0 to 1.2 m/sec near the plating surface) and the liquid pipe line Plating was carried out in the apparatus shown in FIG. 1 using both No. 18 (plating liquid flow rate 1.0 to 1.2 m/sec). The results are shown in Table 1.

【表】 表1から明らかなように、本実施例のめつき方
法においては、比較例1及び2と比べ、電流密度
30A/dm2までめつきむら及び焼けが発生せず、
良好にめつきされていることが分る。又、めつき
の厚さについても、比較例1及び2と比べてバラ
ツキが小さく、めつき面近傍においてめつき液が
均一に攪拌されていることが分る。 [発明の効果] 本発明の液流式めつき方法は互いに略直角方向
の噴射流と攪拌流の両方向のめつき流内でめつき
が行われるので、めつき面に対する攪拌が均一化
し、めつきむらを生ぜず、めつき電流密度が向上
する。 このような、両方向めつき流であるため、単一
攪拌流に比べてめつき速度を向上させることがで
きる。 又、めつき液面ヘツド差による液流下式では、
流速が速くなると、液面から空気の巻き込みが多
くなり、めつき液の劣化、ガスの発生、めつきむ
ら等が起り易くなるが、本発明の強制された2方
向のめつき流による液流下式めつき方法によれ
ば、これらの欠点を取り除くことができ、めつき
作業が安定化する。
[Table] As is clear from Table 1, the plating method of this example has a higher current density than Comparative Examples 1 and 2.
No unevenness or burning occurs up to 30A/ dm2 ,
It can be seen that it is well plated. It can also be seen that the variation in the plating thickness is smaller than in Comparative Examples 1 and 2, and the plating liquid is uniformly stirred in the vicinity of the plating surface. [Effects of the Invention] In the liquid flow plating method of the present invention, plating is performed within the plating flow in both directions, the jet flow and the agitation flow, which are substantially perpendicular to each other. Plating current density is improved without causing uneven plating. Since the flow is directed in both directions, the plating speed can be improved compared to a single stirring flow. In addition, in the liquid flow type using the plating liquid level head difference,
As the flow rate increases, more air is drawn in from the liquid surface, which tends to cause deterioration of the plating liquid, generation of gas, uneven plating, etc. According to the formula plating method, these drawbacks can be eliminated and the plating work can be stabilized.

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

第1図は本発明の液流下めつき方法の断面図で
ある。第2図は、第1めつき槽の他の実施例を示
す断面図である。第3図は、被めつき処理物の断
面図である。第4図は、従来例めつき方法の断面
図である。 1:第1めつき槽、2:第2めつき槽、3:流
路壁、4:噴射用パイプ、5:めつき液噴射孔、
6:めつき液、7:ポンプ、8:攪拌流、9:噴
射流、19:めつき液流、11:管路、12:め
つき液流出口、13:陽極電極、14:噴射流用
容器、15:被めつき処理物、16:マスキング
テープ、17:部分めつき部、18:液管路。
FIG. 1 is a sectional view of the liquid flow down plating method of the present invention. FIG. 2 is a sectional view showing another embodiment of the first plating tank. FIG. 3 is a sectional view of the coated product. FIG. 4 is a sectional view of a conventional plating method. 1: first plating tank, 2: second plating tank, 3: channel wall, 4: injection pipe, 5: plating liquid injection hole,
6: Plating liquid, 7: Pump, 8: Stirring flow, 9: Jet flow, 19: Plating liquid flow, 11: Pipe line, 12: Plating liquid outlet, 13: Anode electrode, 14: Container for jet flow , 15: Plated product, 16: Masking tape, 17: Partially plated portion, 18: Liquid pipe line.

Claims (1)

【特許請求の範囲】 1 被めつき処理物を、壁面によつて形成される
めつき槽内の液管路中に配置してめつきを行うに
際し、前記液管路の軸線方向のめつき液流と、前
記軸線方向にほぼ直角をなす方向のめつき液流と
の合成めつき液流を被めつき処理物に噴射してめ
つきを行うことを特徴とする液流式めつき方法。 2 前記被めつき処理物が、その広幅面をほぼ垂
直状態に維持しながら前記液管路中を被めつき処
理物の長手方向に移動する帯状体である特許請求
の範囲第1項に記載の液流式めつき方法。
[Scope of Claims] 1. When plating is performed by placing the object to be plated in a liquid pipe line in a plating tank formed by a wall surface, plating in the axial direction of the liquid pipe line is performed. A liquid flow plating method characterized in that plating is performed by injecting a synthetic plating liquid flow of a liquid flow and a plating liquid flow in a direction substantially perpendicular to the axial direction onto the object to be plated. . 2. The object to be plated is a belt-shaped object that moves in the longitudinal direction of the object to be plated in the liquid pipe while maintaining its wide side in a substantially vertical state. Liquid flow plating method.
JP3604785A 1985-02-25 1985-02-25 Liquid flow-down type plating method Granted JPS61195996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3604785A JPS61195996A (en) 1985-02-25 1985-02-25 Liquid flow-down type plating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3604785A JPS61195996A (en) 1985-02-25 1985-02-25 Liquid flow-down type plating method

Publications (2)

Publication Number Publication Date
JPS61195996A JPS61195996A (en) 1986-08-30
JPH0149797B2 true JPH0149797B2 (en) 1989-10-26

Family

ID=12458795

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3604785A Granted JPS61195996A (en) 1985-02-25 1985-02-25 Liquid flow-down type plating method

Country Status (1)

Country Link
JP (1) JPS61195996A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003514125A (en) * 1999-11-09 2003-04-15 シーメンス アクチエンゲゼルシヤフト Equipment for electrolytically processing plate-shaped workpieces, especially printed wiring boards
JP6127726B2 (en) * 2013-02-27 2017-05-17 住友金属鉱山株式会社 Plating equipment
CN112501664B (en) * 2020-11-24 2022-04-22 深圳明阳芯蕊半导体有限公司 PCB electroplating method and PCB electroplating equipment

Also Published As

Publication number Publication date
JPS61195996A (en) 1986-08-30

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