JPS5927398B2 - Surface treatment method of copper or copper alloy or plated products with these metals - Google Patents

Surface treatment method of copper or copper alloy or plated products with these metals

Info

Publication number
JPS5927398B2
JPS5927398B2 JP53084783A JP8478378A JPS5927398B2 JP S5927398 B2 JPS5927398 B2 JP S5927398B2 JP 53084783 A JP53084783 A JP 53084783A JP 8478378 A JP8478378 A JP 8478378A JP S5927398 B2 JPS5927398 B2 JP S5927398B2
Authority
JP
Japan
Prior art keywords
copper
metals
surface treatment
plated products
treatment method
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
JP53084783A
Other languages
Japanese (ja)
Other versions
JPS5511184A (en
Inventor
哲男 前川
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP53084783A priority Critical patent/JPS5927398B2/en
Publication of JPS5511184A publication Critical patent/JPS5511184A/en
Publication of JPS5927398B2 publication Critical patent/JPS5927398B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 この発明は銅又は銅合金ある(・はこれらの金属による
鍍金品の表面処理法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a surface treatment method for plated products made of copper or copper alloys.

従来、例えば銅又は銅合金あるいはこれらの金属による
鍍金品の表面処理法、具体的には特に亜酸化銅法による
着色処理法としては、強力な酸化剤やアルカリを含む溶
液中で化学的な化成処理を行うかあるいはアルカリ溶液
中で行う陽極酸化処理法などが良く知られている。しか
しこれらの方法では一般に処理液の老化が激しく浴管理
が非常に困難である、このような処理液を通常60〜1
00℃の高温下で処理するためその作業性が低下する、
又かかる作業は作業者の熟練に負うところが多く作業の
進行及び仕上り品の良否などは作業者の優れた判断によ
り決められることが多く品質の均→ヒが困難であるばか
りでなく大量生産に不適当である、更に酸化剤及びアル
カリを使用していることにより耐蝕性に問題があり又変
色を生じ易いなど多くの欠点があつた。
Conventionally, surface treatment methods for copper, copper alloys, or plated products made of these metals, specifically coloring treatments using cuprous oxide, involve chemical conversion in a solution containing a strong oxidizing agent or alkali. Well-known methods include anodic oxidation treatment or anodization treatment performed in an alkaline solution. However, in these methods, the processing solution generally deteriorates rapidly and bath management is extremely difficult.
Processing at a high temperature of 00°C reduces workability.
In addition, such work depends largely on the skill of the worker, and the progress of the work and the quality of the finished product are determined by the worker's good judgment, which not only makes it difficult to maintain uniform quality but also makes mass production difficult. However, due to the use of oxidizing agents and alkalis, there were many drawbacks such as corrosion resistance and discoloration.

特に上記処理液が高濃度であることは近年の廃液公害上
の問題を著しくする恐れが高い。発明者等は銅及び銅合
金あるいはこれらの金属による鍍金品の酸化着色法に関
して上記の諸問題を解決すべく試験研究を重ね、電解質
濃度が0.05%以下でpHが6〜11である低濃度電
解液水溶液中で銅又は銅合金あるいはこれらの金属によ
る鍍金品をPR電解処理することによつてその表面に着
色化成皮膜が形成されることを見出しこの発明を完成す
るに至つたものである。
In particular, the high concentration of the treatment liquid is likely to exacerbate the recent waste liquid pollution problems. In order to solve the above-mentioned problems, the inventors have conducted repeated research and experiments on methods for oxidation coloring of copper, copper alloys, or plated products using these metals. The present inventors have discovered that a colored chemical conversion film is formed on the surface of copper, copper alloys, or plated products made of these metals by PR electrolytic treatment in a concentrated electrolyte solution, leading to the completion of this invention. .

即ちこの発明は、銅又は銅合金あるいはこれらの金属に
よる鍍金品を水溶液中でPR電解処理することにより該
金属あるいは鍍金品表面に金属亜酸化物皮膜を形成する
ようにした表面処理方法である。
That is, the present invention is a surface treatment method in which a metal suboxide film is formed on the surface of copper, copper alloy, or a plated product made of these metals by performing PR electrolytic treatment in an aqueous solution.

この発明における金属とは、上記銅の外、鉄、亜鉛、錫
又は銀あるいはこれらの合金を含むものである。
The metal in this invention includes iron, zinc, tin, silver, or an alloy thereof in addition to the above-mentioned copper.

上記PR電解とは直流と逆電流を交互に周期的に通じて
電解する方法で、物品は直流では陽極となり逆電流の場
合には陰極となる。又この発明では、電解液として後記
実施例の如く、電解質濃度が0.05%外下でpHが6
〜11である低濃度のものが用(・られる。
The above-mentioned PR electrolysis is a method of electrolyzing by alternately and periodically passing a direct current and a reverse current, and the article becomes an anode in the case of a direct current and a cathode in the case of a reverse current. In addition, in this invention, the electrolyte has an electrolyte concentration of about 0.05% and a pH of 6, as shown in the examples below.
A low concentration of ~11 is used.

具体的に水溶液中で例えば銅又は銅合金あるいはこれら
の金属の鍍金品をPR電解した場合に、先づ陽極では銅
が溶解して活性な面が露出され同時に発生期の酸素を生
ずる。
Specifically, when copper, copper alloys, or plated products of these metals are subjected to PR electrolysis in an aqueous solution, the copper first dissolves at the anode to expose the active surface, and at the same time generates nascent oxygen.

次に陰極に極性が移ると銅は変化せず水素を生ずる。従
つて直流と逆電流の切換周期が長い場合には電解脱脂の
場合と同じように溶解のみが起り酸化しな〜・o他方直
流と逆電流の切換周期を短かくすると陽極では溶解量が
非常に少なくなり発生期の酸素による酸化量が時間と共
に増加することになる。
Next, when the polarity is transferred to the cathode, the copper remains unchanged and produces hydrogen. Therefore, when the switching period between direct current and reverse current is long, only dissolution occurs and no oxidation occurs, as in the case of electrolytic degreasing.On the other hand, when the switching period between direct current and reverse current is shortened, the amount of dissolution at the anode becomes very large. The amount of oxidation caused by oxygen during the nascent stage increases with time.

即ち陽極では常時活性化された状態で酸化し、この酸化
が進行するにしたが(・、色調は褐色一青一黄金一赤一
紺色の如く変化する。直流と逆電流の切換周期、電流密
度及び電解時間などを適当に選定することによつてこの
色調を自由に選択することができるのである。この場合
用いる液組成は上記酸化条件には余り関係しない。
In other words, the anode is constantly oxidized in an activated state, and as this oxidation progresses, the color tone changes from brown to blue to golden to red to dark blue.The switching period of direct current and reverse current, current density, This color tone can be freely selected by appropriately selecting the electrolysis time, etc. In this case, the liquid composition used has little to do with the above-mentioned oxidation conditions.

以下この発明を実施例により具体的に説明する。の水溶
液中で液温25℃、電流密度0.1A/Dnl2の条件
にてPR電解(切換周期2秒)し、10分後に紺色に着
色した銅板を得た。
The present invention will be specifically explained below using examples. PR electrolysis (switching cycle: 2 seconds) was carried out in an aqueous solution at a liquid temperature of 25° C. and a current density of 0.1 A/Dnl2, and after 10 minutes, a dark blue colored copper plate was obtained.

実施例2 銅板を10%硫酸で酸洗し、水にて洗滌後、の水溶液中
で温度25℃、0.03A/Dm2の条件にてPR電解
処理(切換周期2秒)し、30分後に紺色に着色した銅
板を得た。
Example 2 A copper plate was pickled with 10% sulfuric acid, washed with water, and then subjected to PR electrolysis treatment (switching cycle: 2 seconds) in an aqueous solution at a temperature of 25°C and 0.03A/Dm2, and after 30 minutes. A copper plate colored dark blue was obtained.

実施例3 実施例2において電流密度を0.01A/Dm2とした
外は全く同様に行ない10分後に青色に着色した銅板を
得た。
Example 3 The same procedure as in Example 2 was repeated except that the current density was changed to 0.01 A/Dm2, and a copper plate colored blue was obtained after 10 minutes.

以上の説明で明らかなように、本発明は上述の低濃度電
解液を用いたPR電解処理による着色被膜処理であり、
電解で発生する酸素に依存する酸化であるから、工業用
水を用℃・た処理が可能となること、下地との密着性が
向土し耐触性に優れるなど塗装前の下地処理などに好適
であり、処理液の変化が殆んどなく液の老化による液の
管理の困難性が解消されるなど従来法の問題を解決し、
更に切換周期、電流密度及び電解時間などの選定により
色調の管理が容易となり、又品質の均一化も可能であり
、特に廃液の処理が容易で公害上の問題発生の恐れが激
減するなどその工業上の利用価値は非常に大きい。
As is clear from the above explanation, the present invention is a colored film treatment by PR electrolysis using the above-mentioned low concentration electrolyte,
Since the oxidation depends on the oxygen generated by electrolysis, it can be treated with industrial water at ℃, and it has good adhesion to the substrate and excellent corrosion resistance, making it suitable for surface treatment before painting. This method solves the problems of conventional methods, such as almost no change in the processing solution and the difficulty in managing the solution due to aging of the solution.
Furthermore, by selecting the switching period, current density, electrolysis time, etc., color tone can be easily controlled and quality can be made uniform.In particular, it is easy to treat waste liquid, and the risk of pollution problems is drastically reduced, making it easier for the industry. The utility value of the above is extremely large.

Claims (1)

【特許請求の範囲】[Claims] 1 銅又は銅合金あるいはこれらの金属による鍍金品を
電解質濃度が0.05%以下でpHが6〜11である低
濃度電解液中でPR電解することにより、それらの表面
に金属亜酸化物皮膜を形成するようにしたことを特徴と
する銅又は銅合金あるいはこれらの金属による鍍金品の
表面処理法。
1. A metal suboxide film is formed on the surface of copper, copper alloy, or plated products made of these metals by performing PR electrolysis in a low-concentration electrolyte with an electrolyte concentration of 0.05% or less and a pH of 6 to 11. 1. A method for surface treatment of copper or copper alloys or plated products made of these metals, characterized by forming.
JP53084783A 1978-07-11 1978-07-11 Surface treatment method of copper or copper alloy or plated products with these metals Expired JPS5927398B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53084783A JPS5927398B2 (en) 1978-07-11 1978-07-11 Surface treatment method of copper or copper alloy or plated products with these metals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53084783A JPS5927398B2 (en) 1978-07-11 1978-07-11 Surface treatment method of copper or copper alloy or plated products with these metals

Publications (2)

Publication Number Publication Date
JPS5511184A JPS5511184A (en) 1980-01-25
JPS5927398B2 true JPS5927398B2 (en) 1984-07-05

Family

ID=13840286

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53084783A Expired JPS5927398B2 (en) 1978-07-11 1978-07-11 Surface treatment method of copper or copper alloy or plated products with these metals

Country Status (1)

Country Link
JP (1) JPS5927398B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57173988A (en) * 1981-04-20 1982-10-26 Matsushita Electric Ind Co Ltd Magnetic sensor
JPS61131429U (en) * 1985-02-01 1986-08-16
JPH06264518A (en) * 1993-03-16 1994-09-20 Ozawa Concrete Kogyo Kk Connection structure of plate material

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49123448A (en) * 1973-04-03 1974-11-26
JPS51144346A (en) * 1975-06-09 1976-12-11 Uemura Kogyo Kk Process for coloring copper and its alloy
JPS5248587A (en) * 1975-09-06 1977-04-18 Imris Pavel Ozone generator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49123448A (en) * 1973-04-03 1974-11-26
JPS51144346A (en) * 1975-06-09 1976-12-11 Uemura Kogyo Kk Process for coloring copper and its alloy
JPS5248587A (en) * 1975-09-06 1977-04-18 Imris Pavel Ozone generator

Also Published As

Publication number Publication date
JPS5511184A (en) 1980-01-25

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