JPS6128038B2 - - Google Patents

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Publication number
JPS6128038B2
JPS6128038B2 JP12900178A JP12900178A JPS6128038B2 JP S6128038 B2 JPS6128038 B2 JP S6128038B2 JP 12900178 A JP12900178 A JP 12900178A JP 12900178 A JP12900178 A JP 12900178A JP S6128038 B2 JPS6128038 B2 JP S6128038B2
Authority
JP
Japan
Prior art keywords
processing
liquid
pump
treatment
tank
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
JP12900178A
Other languages
Japanese (ja)
Other versions
JPS5554600A (en
Inventor
Mitsuhiro Sato
Takeshi Yano
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP12900178A priority Critical patent/JPS5554600A/en
Publication of JPS5554600A publication Critical patent/JPS5554600A/en
Publication of JPS6128038B2 publication Critical patent/JPS6128038B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は金属の陽極酸化処理装置に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a metal anodizing treatment apparatus.

処理槽中の処理液に被処理物を浸漬させて行う
金属の陽極酸化処理装置としては、例えば第3図
に示すように、無数の微細な通気孔を有する多孔
体31を処理槽32の底部に設けて該多孔体31
に連結された圧縮空気供給管33を通じコンプレ
ツサ34より供給される圧縮空気を該多孔体31
の通気孔から処理槽32中の処理液の底方部に噴
出させて処理液中に微細な気泡を形成させ、この
気泡によつて処理液を撹拌して処理効率を高める
ようにしたものが知られているが、従来のこの陽
極酸化処理装置における気泡の発生は加圧空気に
よるものとしているため、極微細な気泡を得難い
うえに処理液に浸漬された被処理物ハに対する気
泡の当り方がその底面においては極めて強いのに
対し側面においては弱く、また、上面においては
殆んど気泡が当らないという部分差が生じ、気泡
の当りかたが強い底面付近のイオン濃度は均一と
なるうえ冷却もよく行われるのに対し上方に行く
に従いイオン濃度が不均一で冷却もあまり行われ
なくなり、被処理物の表面に生成される酸化皮膜
の厚みや硬度に差が生じたり色むらの原因とな
る。しかも、この傾向は電流密度を大きくするほ
ど著しくなるので、あまり電流密度を上げること
ができず、そのため陽極酸化の処理時間を長く要
する等多くの問題点があつた。
As shown in FIG. 3, for example, as shown in FIG. 3, a metal anodic oxidation treatment apparatus in which the object to be treated is immersed in a treatment liquid in a treatment tank is used, for example, as shown in FIG. The porous body 31 is provided in
The compressed air supplied from the compressor 34 through the compressed air supply pipe 33 connected to the porous body 31
The processing liquid is ejected from the vent hole to the bottom of the processing liquid in the processing tank 32 to form fine bubbles in the processing liquid, and these bubbles agitate the processing liquid to improve processing efficiency. It is known that bubbles are generated in conventional anodizing processing equipment using pressurized air, which makes it difficult to obtain extremely fine bubbles, and it is also difficult to obtain very fine bubbles, as well as the way the bubbles hit the workpiece immersed in the processing solution. The ion concentration is extremely strong at the bottom, weaker at the sides, and hardly hit by bubbles at the top. Cooling is often performed, but as you move upwards, the ion concentration becomes uneven and cooling is not performed as much, which can cause differences in the thickness and hardness of the oxide film formed on the surface of the processed object and cause uneven color. Become. In addition, this tendency becomes more pronounced as the current density increases, so the current density cannot be increased too much, resulting in many problems such as requiring a long anodic oxidation process time.

本発明は前記のような問題点を解決する目的の
下に完成された金属の陽極酸化処理装置に関する
もので、以下、本発明を図示の実施例について詳
細に説明する。
The present invention relates to a metal anodic oxidation processing apparatus completed for the purpose of solving the above-mentioned problems.Hereinafter, the present invention will be described in detail with reference to the illustrated embodiments.

第1図は本発明の第1の実施例としての陽極酸
化処理装置を示すもので、1は槽壁にポンプ接続
口2を適数個配設するとともに底方部に循環用の
管路接続口3を設けた処理槽で、該処理槽1の外
部において管路接続口3に一端を接続させた管路
4の中間にはポンプ5を設けるとともに該管路4
の先方部は槽壁に沿い立ち上らせて外界空気の吸
引によつて無数の微細な気泡を通過処理液中に形
成させる水流ポンプ6の適数個を所要間隔下に取
付け、該水流ポンプ6の吐出管部7を前記ポンプ
接続口2に嵌挿固着して該吐出管部7の先端吐出
口を処理槽1中にセツトされた電極イ,ロの透孔
を介して被処理物に向けたものとしている。な
お、前記水流ポンプ6は管路4の先方部に配設さ
れた各分岐路に接続される給液口7′からポンプ
室8に臨んだ先端のノズル部9にわたる部分を先
細テーパー状の給液路10に形成するとともにポ
ンプ室8から吐出管部7の吐出口にわたる部分を
先拡きテーパー状の放液路11に形成し、さら
に、ポンプ室8内を吸気孔12を介して吸気管1
3に接続させたもので、ポンプ5を駆動させるこ
とにより処理槽1内の処理液が管路4および水流
ポンプ6を通じ再び処理槽1内に循環される間に
ノズル部9からの液流の噴出によりポンプ室8内
を減圧し、吸気管13、吸気孔12を通じ外界空
気をポンプ室8内に吸引して通過処理液に混合さ
せ、吐出管部7の先端吐出口からは無数の微細な
気泡を形成した処理液が被処理物に向け送られる
ものとしている。他方、第2図に示すものは本発
明の第2の実施例として表面積の比較的大きな被
処理物の陽極酸化処理装置を示すもので、前記第
1の実施例との相違点は前記第1の実施例におけ
るポンプ接続口2が処理槽1になく、処理槽1の
底方部の管路接続口3に一端を接続した管路4の
先方部が処理槽1の槽底を通じて処理槽1内に立
ち上らせてあつて該管路4の先方部の電極イの背
面位置に多数取付ける水流ポンプ6もその吐出管
部7の吐出口を斜上向きとするものと斜下向きに
するものの2種があり、吐出口を斜上向きとする
水流ポンプ6と斜下向きとする水流ポンプ6から
電極イの透孔を介してそれぞれ噴出される液流の
交叉点より外側に被処理物を位置させて外界空気
の吸引によつて無数の微細な気泡の形成された処
理液が吐出管部7の吐出口から被処理物の全表面
に略均等に送られるよう考慮されている。
Fig. 1 shows an anodizing treatment apparatus as a first embodiment of the present invention, in which a suitable number of pump connection ports 2 are arranged on the tank wall, and a circulation pipe is connected to the bottom part. A processing tank is provided with a port 3, and a pump 5 is provided in the middle of a pipe line 4 whose one end is connected to the pipe connection port 3 on the outside of the processing tank 1.
At the front end of the tank, an appropriate number of water jet pumps 6 are installed at required intervals to stand up along the tank wall and form countless fine bubbles in the passing treatment liquid by suctioning outside air. The discharge pipe part 7 of No. 6 is inserted and fixed into the pump connection port 2, and the distal end of the discharge pipe part 7 is connected to the object to be processed through the through holes of electrodes A and B set in the processing tank 1. It is aimed at Note that the water pump 6 has a tapered supply section extending from the liquid supply port 7' connected to each branch channel arranged at the front end of the pipe line 4 to the nozzle section 9 at the tip facing the pump chamber 8. A tapered liquid discharge passage 11 is formed in the part extending from the pump chamber 8 to the discharge port of the discharge pipe section 7, and an intake pipe is formed in the pump chamber 8 through the intake hole 12. 1
3, by driving the pump 5, the liquid flow from the nozzle section 9 is controlled while the processing liquid in the processing tank 1 is circulated back into the processing tank 1 through the pipe 4 and the water pump 6. The pressure inside the pump chamber 8 is reduced by the jetting, and outside air is sucked into the pump chamber 8 through the intake pipe 13 and the intake hole 12 and mixed with the passing treatment liquid. It is assumed that the processing liquid in which bubbles have been formed is sent toward the object to be processed. On the other hand, FIG. 2 shows a second embodiment of the present invention, which is an apparatus for anodizing a workpiece having a relatively large surface area, and the difference from the first embodiment is the first embodiment. In this embodiment, the pump connection port 2 is not in the processing tank 1, and the front end of the pipe line 4, one end of which is connected to the pipe connection port 3 at the bottom of the processing tank 1, is connected to the processing tank 1 through the bottom of the processing tank 1. There are also two types of water pumps 6, which are installed in large numbers on the back side of the electrode A at the front end of the pipe 4, with the discharge port of the discharge pipe 7 facing diagonally upward and the other having the discharge port facing diagonally downward. The object to be treated is positioned outside the intersection of the liquid streams ejected through the through holes of the electrode A from the water jet pump 6 whose discharge port is directed diagonally upward and the water jet pump 6 whose discharge port is directed diagonally downward. It is designed so that the processing liquid, in which countless fine bubbles are formed by suction of external air, is sent almost evenly to the entire surface of the object to be processed from the discharge port of the discharge pipe section 7.

このように構成されたものは、在来の陽極酸化
処理装置と同様処理槽1内に処理液として所要量
の電解液を満たすとともにこの処理液中に電極
イ,ロをセツトし、例えばアルミニウム合金より
なる被処理物ハを該電極イ,ロに対向させて通電
して陽極酸化処理を行うものであるが、この処理
時においてポンプ5を駆動させれば、処理槽1中
の処理液の一部は処理槽1の底方部に設けられて
いる管路接続口3よりポンプ5、管路4を経て該
管路4の先方部の電極イ,ロの背面位置に配設さ
れている水流ポンプ6の給液口7′に送られ、先
細テーパー状の給液路10、ノズル部9、ポンプ
室8、内部を先拡きテーパー状の放液路11とし
た吐出管部7を経て被処理物ハに向けた吐出口を
通じ処理槽1内に循環されることとなる。ところ
が、この水流ポンプ6を通過して処理槽1に循環
される処理液はノズル部9から噴出される液流に
よつてポンプ室8内を減圧して吸気管13に接続
させた吸気孔12よりポンプ室8内に外界空気を
吸い込み、給液路10を経て吐出口より処理槽1
内に戻される際には外界空気の吸引によつて無数
の極めて微細な気泡が形成されたものとなつてお
り、しかも、水流ポンプ6の吐出口を電極イ,ロ
の透孔を介して被処理物ハに向けたものとしてあ
るから、陽極酸化処理を行ううえにおいて次のよ
うな特長がある。即ち、本発明においては、電極
の背面に設けられた水流ポンプ6により減圧状態
で気泡を発生させるため、気泡径の極めて小さな
微泡が多く形成され、直ちに処理液中に吐出され
る微泡の液中での上昇速度は遅いので微泡の数が
極めて多い点と相まち撹拌作用が大きく、また、
処理液を処理槽内へ循環流出させるためますます
処理槽内の処理液全体の撹拌が行われ、イオンの
供給がよいうえ冷却効率もよくてバーニングを起
こすことはなく、従つて、電流密度を上げること
ができて処理時間を短縮できる。さらに、処理槽
1に循環される処理液自身に無数の微泡を含むこ
とから、微泡が被処理物の表面に均一に当たる。
この原因は泡とくに2.0mm径以下の微泡は前記し
たように液中の上昇速度が遅いため、水流ポンプ
からの処理液の流れに乗つて被処理物の表面まで
到達しやすく、被処理物の表面近傍は無数の微泡
による乱流撹拌作用により境膜が破壊されて新し
い処理液が被処理物表面にもたらされるから、陽
極酸化処理効率が上がり、またイオン濃度が均一
となつて陽極酸化皮膜の厚さは各部で均一のもの
となり、さらに、被処理物の表面近傍は各部が均
一に冷却されるから電流密度を大きくしてもバー
ニングを生じることがなくて短時間で処理を終え
ることができる。なお、管路4の中間に設けられ
るポンプ5のポンプ圧は通常0.5〜10Kg/cm2程度と
し、また、水流ポンプ6によつて通過処理液中に
形成される気泡の大きさは処理目的に応じ若干相
違するが約0.01〜2mm程度の極めて小径のものが
効果的である。
In the device constructed in this way, the processing tank 1 is filled with a required amount of electrolyte as a processing solution, and electrodes A and B are set in this processing solution, similar to conventional anodizing processing equipment. Anodic oxidation treatment is performed by placing the object to be treated (C) facing the electrodes (A) and (B) and applying electricity to the object.If the pump 5 is driven during this treatment, part of the treatment liquid in the treatment tank 1 will be oxidized. In this section, water flows from a pipe connection port 3 provided at the bottom of the treatment tank 1, passes through a pump 5, a pipe 4, and is disposed on the back side of electrodes A and B at the front end of the pipe 4. The liquid is sent to the liquid supply port 7' of the pump 6, and passes through the tapered liquid supply path 10, the nozzle part 9, the pump chamber 8, and the discharge pipe part 7 with a tapered liquid discharge path 11 inside. The material to be processed is circulated into the processing tank 1 through the discharge port directed toward the material to be processed C. However, the processing liquid that passes through the water pump 6 and is circulated to the processing tank 1 is depressurized in the pump chamber 8 by the liquid flow ejected from the nozzle part 9, and then passes through the intake hole 12 connected to the intake pipe 13. The outside air is sucked into the pump chamber 8, passed through the liquid supply path 10, and then flows into the processing tank 1 from the discharge port.
When the air is returned to the inside, countless extremely fine bubbles are formed by the suction of outside air, and the discharge port of the water jet pump 6 is covered through the through holes of electrodes A and B. Since it is intended for the processing object C, it has the following features when performing anodizing treatment. That is, in the present invention, since bubbles are generated under reduced pressure by the water pump 6 installed on the back of the electrode, many microbubbles with extremely small bubble diameters are formed, and the microbubbles that are immediately discharged into the processing liquid are The rate of rise in liquid is slow, so the number of microbubbles is extremely large, and the stirring action is large.
In order to circulate and flow out the processing solution into the processing tank, the entire processing solution in the processing tank is increasingly agitated, and the supply of ions is good and the cooling efficiency is also good, so burning does not occur, and therefore the current density can be reduced. This can reduce processing time. Furthermore, since the processing liquid itself that is circulated in the processing tank 1 contains countless microbubbles, the microbubbles uniformly hit the surface of the object to be processed.
The reason for this is that bubbles, especially microbubbles with a diameter of 2.0 mm or less, rise slowly in the liquid as mentioned above, so they easily reach the surface of the object to be treated by riding the flow of treatment liquid from the water pump. Near the surface of the workpiece, the membrane is destroyed by the turbulent agitation action of countless microbubbles and a new treatment liquid is brought to the surface of the workpiece, increasing the efficiency of the anodizing process and making the ion concentration uniform, allowing the anodizing process to proceed smoothly. The thickness of the film is uniform in each part, and each part near the surface of the object to be treated is uniformly cooled, so even if the current density is increased, no burning occurs and the treatment can be completed in a short time. I can do it. The pump pressure of the pump 5 installed in the middle of the pipe line 4 is usually about 0.5 to 10 kg/cm 2 , and the size of the bubbles formed in the passing treatment liquid by the water pump 6 is determined according to the treatment purpose. Although it varies slightly depending on the situation, a very small diameter of about 0.01 to 2 mm is effective.

次に、本発明装置を用いて行つた陽極酸化処理
方法の実験例を示す。
Next, an experimental example of an anodic oxidation treatment method performed using the apparatus of the present invention will be shown.

アルミニウム合金(JIS規格6063)よりなる500
mm×300mm×1mmの板を第3図に示したような装
置を用いた従来の処理方法と第1図に示すような
本発明装置を用いる処理方法により陽極酸化処理
を液組成、硫酸30W/V%、温度20℃、電流密度
20A/dm2、ノズル圧力3Kg/cm2、ノズル数40個/
セツトを2セツト、液循環量300/minという処
理条件により陽極酸化処理を行つた。この結果、
従来方法で得られた陽極酸化皮膜が上部と下部で
色むらを生じ、上部は灰色、下部は灰黒色を帯
び、渦電流膜圧計で膜厚を測定したところ、上部
の灰色を帯びた部分は53μm、下部の灰黒色を帯
びた部分は47μmで上下の差が6μmあつたのに
対し、本発明装置により陽極酸化処理して得られ
た皮膜は灰色で均一な色調を帯びており、膜厚を
測定したところ上部で51μm、下部で50μmと上
下部分が略均一であつた。
500 made of aluminum alloy (JIS standard 6063)
A mm x 300 mm x 1 mm plate was anodized using the conventional treatment method using the equipment shown in Figure 3 and the treatment method using the present invention equipment shown in Figure 1, using a liquid composition of sulfuric acid 30W/ V%, temperature 20℃, current density
20A/dm 2 , nozzle pressure 3Kg/cm 2 , number of nozzles 40/
The anodizing treatment was carried out under the following conditions: 2 sets and a liquid circulation rate of 300/min. As a result,
The anodic oxide film obtained by the conventional method has uneven color at the upper and lower parts, with the upper part being gray and the lower part being grayish-black.When the film thickness was measured with an eddy current film pressure meter, the grayish part at the top was 53μm, and the gray-black part at the bottom was 47μm, with a difference of 6μm between the top and bottom, whereas the film obtained by anodizing with the device of the present invention had a uniform gray tone, and the film thickness was 53μm. When measured, the upper and lower portions were approximately uniform, 51 μm at the top and 50 μm at the bottom.

本発明は前記説明によつて明らかなように、外
界空気の吸引によつて無数の微細な気泡を通過処
理液中に形成させる水流ポンプを電極の背面に設
け槽中の処理液を循環されるとともに被処理物に
向けこの気泡が形成された直後の処理液を直ちに
送るようにしたから、槽内の処理液は適度に撹拌
されるうえに水流ポンプにより還流された処理液
に含まれる無数の微細な気泡が各種の表面処理を
行ううえに極めて有効に作用するもので、処理時
間を著しく短縮することができるうえに優れた陽
極酸化処理結果の得られる金属の陽極酸化処理装
置として産業の発達に寄与することが極めて大き
いものである。
As is clear from the above description, the present invention is provided with a water jet pump on the back of the electrode that forms countless fine bubbles in the passing treatment liquid by suctioning outside air, and circulates the treatment liquid in the tank. At the same time, the treatment liquid immediately after the bubbles are formed is sent to the object to be treated, so the treatment liquid in the tank is moderately agitated, and the countless particles contained in the treatment liquid refluxed by the water pump are Fine bubbles are extremely effective in performing various surface treatments, and the industry has developed as a metal anodizing treatment device that can significantly shorten treatment time and provide excellent anodizing results. The contribution to this is extremely large.

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

第1図は本発明の陽極酸化処理装置の第1の実
施例を示す一部切欠正面図、第2図は本発明の陽
極酸化処理装置の第2の実施例を示す一部切欠正
面図、第3図は従来の陽極酸化処理装置の一例を
示す一部切欠正面図である。 1:処理槽、6:外界空気の吸引によつて無数
の微細な気泡を通過処理液中に形成させる水流ポ
ンプ。
FIG. 1 is a partially cutaway front view showing a first embodiment of the anodizing treatment apparatus of the present invention, and FIG. 2 is a partially cutaway front view showing the second embodiment of the anodizing treatment apparatus of the present invention. FIG. 3 is a partially cutaway front view showing an example of a conventional anodizing treatment apparatus. 1: Processing tank; 6: Water pump that forms countless fine bubbles in the passing treatment liquid by suctioning outside air.

Claims (1)

【特許請求の範囲】[Claims] 1 処理槽1中にセツトされた電極イ,ロの背面
に、ポンプ5により循環される処理液を噴出する
ノズル部9と、ノズル部9から噴出される液流に
よる減圧を利用して外気を吸引する吸引孔12
と、吸引孔12から吸引された外気によつて形成
された無数の微細な気泡を含む処理液を吐出する
吐出管部7とを備えた水流ポンプ6を設けるとと
もに、該水流ポンプ6の吐出管部7の先端を電極
イ,ロの透孔を介して被処理物ハに向けたことを
特徴とする金属の陽極酸化処理装置。
1 A nozzle part 9 that spouts out the processing liquid circulated by the pump 5 is installed on the back side of the electrodes A and B set in the processing tank 1, and outside air is pumped out using the reduced pressure caused by the liquid flow jetted from the nozzle part 9. Suction hole 12 for suction
and a discharge pipe section 7 that discharges a processing liquid containing countless fine bubbles formed by the outside air sucked from the suction hole 12, and a discharge pipe of the water pump 6. A metal anodic oxidation processing apparatus characterized in that the tip of the part 7 is directed toward the object to be processed C through the through holes of the electrodes A and B.
JP12900178A 1978-10-18 1978-10-18 Surface treating apparatus of metal and others Granted JPS5554600A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12900178A JPS5554600A (en) 1978-10-18 1978-10-18 Surface treating apparatus of metal and others

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12900178A JPS5554600A (en) 1978-10-18 1978-10-18 Surface treating apparatus of metal and others

Publications (2)

Publication Number Publication Date
JPS5554600A JPS5554600A (en) 1980-04-21
JPS6128038B2 true JPS6128038B2 (en) 1986-06-28

Family

ID=14998681

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12900178A Granted JPS5554600A (en) 1978-10-18 1978-10-18 Surface treating apparatus of metal and others

Country Status (1)

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JP (1) JPS5554600A (en)

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Publication number Priority date Publication date Assignee Title
JPS5710872U (en) * 1980-06-21 1982-01-20
JPS6277489A (en) * 1985-09-30 1987-04-09 Nippon Mining Co Ltd Method for pickling metallic material
KR100876920B1 (en) 2006-09-21 2009-01-07 (주)티제이씨 Electrolysis tank for magnesium Anodizing film
JP5998314B2 (en) * 2015-01-05 2016-09-28 株式会社アサヒメッキ Surface treatment method of aluminum alloy
CN106119921B (en) * 2016-08-22 2018-01-23 竞陆电子(昆山)有限公司 PCB plating lines
CN106086977B (en) * 2016-08-23 2018-02-06 竞陆电子(昆山)有限公司 PCB plating lines supply the medicine circulatory system
CN106435682A (en) * 2016-11-11 2017-02-22 苏州胜禹材料科技股份有限公司 Aluminum plate anodic oxidation equipment and coloring process
JP6914073B2 (en) * 2017-03-28 2021-08-04 上村工業株式会社 Surface treatment equipment

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