JPS599639B2 - Oxidation treatment method for copper or copper alloy - Google Patents
Oxidation treatment method for copper or copper alloyInfo
- Publication number
- JPS599639B2 JPS599639B2 JP5175981A JP5175981A JPS599639B2 JP S599639 B2 JPS599639 B2 JP S599639B2 JP 5175981 A JP5175981 A JP 5175981A JP 5175981 A JP5175981 A JP 5175981A JP S599639 B2 JPS599639 B2 JP S599639B2
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- Japan
- Prior art keywords
- copper
- reaction
- sulfuric acid
- copper alloy
- oxide film
- 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.)
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Description
【発明の詳細な説明】
本発明は、銅または銅合金の酸化処理方法に関し、さら
に詳細には銅または銅合金の表面に電気絶縁性に優れた
緻密で密着性のよい酸化銅皮膜を形成させる銅または銅
合金の陽極酸化処理方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an oxidation treatment method for copper or copper alloy, and more specifically, for forming a dense copper oxide film with excellent electrical insulation and good adhesion on the surface of copper or copper alloy. The present invention relates to a method for anodizing copper or copper alloys.
従来より、各種の方法により銅または銅合金の表面に酸
化銅皮膜を形成させることは知られている。It has been known to form a copper oxide film on the surface of copper or copper alloys by various methods.
例えば、(a)銅または銅合金を80℃以上の水酸化ナ
トリウム電解液中で陽極酸化する方法などの高温のアル
カリ性溶液中での陽極酸化処理方法、または(b)銅ま
たは銅合金を亜塩素酸ナトリウムなどの酸化剤の存在下
において水酸化ナトリウムや水酸化カリウムなどのアル
カリ性溶液に浸漬して100℃程度の高温で酸化処理す
る方法などの化成薬品に浸漬する方法などが提案されて
いる。For example, (a) a method of anodizing copper or a copper alloy in a high-temperature alkaline solution, such as a method of anodizing copper or a copper alloy in a sodium hydroxide electrolyte at 80° C. or higher, or (b) a method of anodizing a copper or a copper alloy with chlorine chloride. Methods of immersion in chemical chemicals, such as a method of oxidizing at a high temperature of about 100° C. by immersing it in an alkaline solution such as sodium hydroxide or potassium hydroxide in the presence of an oxidizing agent such as sodium hydroxide, have been proposed.
しかしながら、これらの方法のうち、(a)の高温のア
ルカリ性溶液中での陽極酸化処理は、酸化反応を高温状
態で行なわせるため、反応装置を耐食性にする必要があ
ること、あるいは加熱のための設備を必要とするため設
備コストがかかること、また効果的な電流密度を維持す
るために電圧をコントロールする必要があることなど、
かなり国難なこと13゛多く、実用上は上述の(b)の
化成薬品溶液中に浸漬するだけで酸化処理の可能な、い
わゆるケミカルコンバージヨンコーティングの方が実用
例が多いようである。既に、本発明者等も、銅または銅
合金を過酸化水素に硝酸または硫酸を添加した水溶液中
に浸漬することにより、銅または銅合金表面に絶縁性、
可撓性および密着性の面で十分実用に耐える酸化銅皮膜
を形成する方法(特願昭54−129782号、特願昭
54−146179号、特願昭55−121570号)
を提案してきた。However, among these methods, (a) anodizing treatment in a high-temperature alkaline solution causes the oxidation reaction to take place at a high temperature, so it is necessary to make the reaction equipment corrosion-resistant, or the heating The equipment required is expensive, and the voltage needs to be controlled to maintain an effective current density.
There are many national problems, and in practice, so-called chemical conversion coatings, which can be oxidized by simply immersing them in a chemical chemical solution as described in (b) above, are more commonly used. The present inventors have already developed insulation properties on the surface of copper or copper alloy by immersing copper or copper alloy in an aqueous solution containing hydrogen peroxide and nitric acid or sulfuric acid.
Method for forming a copper oxide film that is sufficiently practical in terms of flexibility and adhesion (Japanese Patent Application No. 1982-129782, Japanese Patent Application No. 54-146179, Japanese Patent Application No. 55-121570)
has been proposed.
これに対して、本発明者等は、過酸化水素と硫酸の混合
水溶液中で銅または銅合金を陽極酸化処理することによ
り、本発明者等が先に提案した前記特許出願に係る単な
る浸漬法だけでは得られなかつた優れた酸化銅皮膜が得
られ、ましてや従来知られている高温のアルカリ性水溶
液中での陽極酸化処理法では得られなかつた優れた特性
をもつ酸化銅皮膜が得られることを見い出し、本発明を
完成したものである。In contrast, the present inventors have proposed a simple immersion method according to the patent application previously proposed by the present inventors by anodizing copper or copper alloy in a mixed aqueous solution of hydrogen peroxide and sulfuric acid. It was discovered that an excellent copper oxide film could be obtained that could not be obtained by using the method alone, and furthermore, a copper oxide film with excellent properties that could not be obtained by the conventional anodizing treatment method in a high-temperature alkaline aqueous solution could be obtained. The heading completes the invention.
本発明の酸化処理方法の特徴は、銅または銅合金の表面
に電気絶縁性や密着性の優れた酸化銅皮膜を形成するた
め、銅または銅合金を過酸化水素と硫酸との混合水溶液
中で陽極酸化することである。The feature of the oxidation treatment method of the present invention is that copper or copper alloy is heated in a mixed aqueous solution of hydrogen peroxide and sulfuric acid in order to form a copper oxide film with excellent electrical insulation and adhesion on the surface of copper or copper alloy. It is anodized.
以下、本発明をさらに詳細に説明する。The present invention will be explained in more detail below.
本発明に用いられる銅または銅合金はまず脱脂、脱スケ
ールなどの前処理が施される。The copper or copper alloy used in the present invention is first subjected to pretreatment such as degreasing and descaling.
次いで前処理が施された銅または銅合金は過酸化水素と
硫酸の混合水溶液中に浸漬され酸化される。この混合水
溶液での銅または銅合金に対する化学反応は次のように
考えられる。被処理体が処理液に投入されると、前処理
済みの銅表面に対して混合水溶液中の過酸化水素が直ち
にアタツクして酸化反応が行われる(一次酸イ0。Next, the pretreated copper or copper alloy is immersed in a mixed aqueous solution of hydrogen peroxide and sulfuric acid to be oxidized. The chemical reaction of copper or copper alloy in this mixed aqueous solution is considered as follows. When the object to be treated is placed in the treatment solution, the hydrogen peroxide in the mixed aqueous solution immediately attacks the pretreated copper surface and an oxidation reaction takes place (primary acid 0).
引き続き硫酸によるエツチング作用が進行し、清浄で活
性な銅表面が現われる。これらの反応は銅表面を活性化
し、引き続く反応をスムーズに進行させるための活性化
反応、不働態化防止反応と呼ぷことができる。この反応
を反応式で表わせば以下のとうりとなる。続いて、二次
酸化反応が起こる。Subsequently, the etching action with sulfuric acid proceeds, revealing a clean and active copper surface. These reactions can be called activation reactions and passivation prevention reactions that activate the copper surface and allow subsequent reactions to proceed smoothly. This reaction can be expressed as a reaction formula as follows. Subsequently, a secondary oxidation reaction occurs.
上述のようにして活性化された銅表面に過酸化水素から
発生した活性酸素による化学的酸化反応と、硫酸を電解
質としてこの硫酸の特質に基づく水の解離による水酸イ
オンの電気化学的酸化反応が重複して生じる。この場合
、上記の化学的酸化反応によるときはもちろんのこと、
電気化学的酸化反応により生成された銅化合物も、最終
的に安定な酸化銅として銅表面に皮膜を形成する。この
皮膜は緻密でかつ電気絶縁性などに非常に優れたもので
ある。すなわち、この皮膜が緻密でかつ電気絶縁性に非
常に優れているのは、過酸化水素の化学的酸化反応によ
る酸化銅がある程度、多孔質として生成されていく一方
で、硫酸の電解による電気化学的酸化反応による銅化合
物、例えば水酸化第二銅が粘着性に富む物質として上記
酸化銅の多孔質内などに滞留する如き状態で生成、充填
され、しかる後、酸化銅に変るため、両反応による酸化
銅が高密度でかつ厚目に生成されると、思われるからで
ある。またこの場合、過酸化水素による化学的酸化反応
が、硫酸による銅の陽極溶解を絶妙にセーブして、逆に
電気化学的酸化反応による陽極酸化をスムーズに導びく
役目をしているものと思われる。この反応を反応式で表
わせば以下のとうりである。以上のようにしてなる陽極
酸化処理後の酸化皮膜を実際に観察してみると、酸化皮
膜は酸化第二銅(CuO)からなる均一成分で構成され
ていることが観察され、化学的卦よび電気化学的の両反
応が酸化第二銅の形成に重畳効果をあげていることが判
る。また陽極側の銅の溶出も1時間×1ボルト当り数百
―以内であつた。次に溶液組成や陽極酸化条件について
説明する。A chemical oxidation reaction using active oxygen generated from hydrogen peroxide on the copper surface activated as described above, and an electrochemical oxidation reaction of hydroxide ions due to the dissociation of water based on the properties of sulfuric acid using sulfuric acid as an electrolyte. occur in duplicate. In this case, as well as the above chemical oxidation reaction,
The copper compound produced by the electrochemical oxidation reaction also forms a film on the copper surface as stable copper oxide. This film is dense and has excellent electrical insulation properties. In other words, the reason why this film is dense and has excellent electrical insulation properties is that while copper oxide is formed to some extent in a porous form through the chemical oxidation reaction of hydrogen peroxide, the electrochemical reaction caused by the electrolysis of sulfuric acid Copper compounds, such as cupric hydroxide, are generated and filled in the pores of the copper oxide as a highly sticky substance, and are then converted to copper oxide, so both reactions occur. This is because copper oxide is thought to be produced in a dense and thick manner. In this case, it is thought that the chemical oxidation reaction caused by hydrogen peroxide exquisitely prevents the anodic dissolution of copper by sulfuric acid, and conversely serves to smoothly guide the anodic oxidation caused by the electrochemical oxidation reaction. It will be done. This reaction can be expressed as a reaction formula as follows. When we actually observed the oxide film after the anodic oxidation treatment as described above, it was observed that the oxide film was composed of a uniform component consisting of cupric oxide (CuO), and the chemical It can be seen that both electrochemical reactions have a superimposed effect on the formation of cupric oxide. Further, the elution of copper from the anode side was within several hundred centimeters per hour x 1 volt. Next, the solution composition and anodic oxidation conditions will be explained.
混合水溶液中の過酸化水素の濃度は5〜50v01q6
が好ましい。5v01q6未満だと活性化のための上述
の反応式(1)で示される一次酸化反応が起りにくく、
その後の反応式(3)で示される二次酸化能力も少ない
ので、化学的酸化反応による酸化皮膜が生成せず、硫酸
の電解質としての作用に基づく電気分解が優先して起り
、その結果銅の溶出が多くなり、酸化皮膜の形成が難し
い。The concentration of hydrogen peroxide in the mixed aqueous solution is 5 to 50v01q6
is preferred. If it is less than 5v01q6, the primary oxidation reaction shown by the above reaction formula (1) for activation is difficult to occur,
Since the subsequent secondary oxidation capacity shown in reaction equation (3) is also small, no oxide film is formed by chemical oxidation reaction, and electrolysis based on the action of sulfuric acid as an electrolyte occurs preferentially, resulting in copper Elution increases, making it difficult to form an oxide film.
また逆に50v01(f)を越えると、過酸化水素自体
の自然分解が激しく過酸化水素が無駄になり実用的でな
く、また硫酸の電気分解効率も低下してくるようである
。次に硫酸の濃度であるが、0.5〜6.0v01%が
好ましい。On the other hand, if it exceeds 50v01(f), the hydrogen peroxide itself will undergo rapid natural decomposition and will be wasted, making it impractical, and the efficiency of electrolysis of sulfuric acid will also decrease. Next, the concentration of sulfuric acid is preferably 0.5 to 6.0%.
0.5v01q6未満では銅表面への水素イオンのアタ
ツクが充分でなく、上述の反応式(2)で示される活性
化のためのエツチング作用と、二次酸化反応の一つとし
ての反応式(4)で示される電気化学的酸化である電気
分解による陽極酸化能力がなくなつて充分な銅の酸化皮
膜は生成されない。If it is less than 0.5v01q6, the attack of hydrogen ions on the copper surface is insufficient, and the etching action for activation shown in the above reaction formula (2) and the reaction formula (4) as one of the secondary oxidation reactions occur. ) is no longer capable of anodic oxidation by electrolysis, which is electrochemical oxidation, and a sufficient copper oxide film cannot be produced.
また逆に6v01%を越えると、エツチング反応が常に
優先して陽極酸化による効果も存在しなくなり、逆に陽
極溶解が激しくなる。尚、陽極酸化時の陰極はステンレ
スでもアルミニウム板でも鉛板でも構わない。On the other hand, if it exceeds 6v01%, the etching reaction will always take priority and the effect of anodic oxidation will no longer exist, and conversely, anodic dissolution will become more intense. Incidentally, the cathode during anodization may be made of stainless steel, aluminum plate, or lead plate.
次に陽極酸化時の電解電圧であるが、定電圧で処理する
のが好ましく、通常数ボルト、好ましくぱ5〜7ボルト
(ただし、過酸化水素濃度35v01%、硫酸濃度1〜
3V01q1)の場合)程度が最適と思われる。Next, regarding the electrolytic voltage during anodic oxidation, it is preferable to process at a constant voltage, usually several volts, preferably 5 to 7 volts (however, hydrogen peroxide concentration is 35v01%, sulfuric acid concentration is 1 to 1%).
3V01q1) seems to be optimal.
また、浴温度は5〜40℃が好ましい。5℃未満だと化
学的酸化反応が起りにく\なり効果的な皮膜の生成が無
く、逆に40℃を越えると過酸化水素の自然分解が著し
くなり皮膜生成の効率が悪くなるようである。Moreover, the bath temperature is preferably 5 to 40°C. If it is below 5℃, chemical oxidation reaction will not occur and effective film formation will not occur.On the other hand, if it exceeds 40℃, natural decomposition of hydrogen peroxide will become significant and the efficiency of film formation will deteriorate. .
また、本発明の一連の反応を進行させるに当つて、上述
の反応式(1),(2)で示される活性化のための反応
と、反応式(3),(4),(5)で示される酸化皮膜
生成反応を好ましくは区別して行えるよう例えば第1図
に示すように、電解槽1を通液性の隔膜2(例えばポリ
エチレン、塩化ビニルなど)で第1反応室3と第2反応
室4とに分割し、第1反応室3から第2反応室4へ移送
される銅または銅合金からなる線材5などをロール電極
6により通電して陽極とし、第2反応室4に板状の電極
7を設けて陰極とした陽極酸化処理装置を用いてもよい
。In addition, in proceeding with the series of reactions of the present invention, the activation reactions shown in the above-mentioned reaction formulas (1) and (2), and the reaction formulas (3), (4), and (5) For example, as shown in FIG. 1, the electrolytic cell 1 is separated by a liquid-permeable diaphragm 2 (e.g., polyethylene, vinyl chloride, etc.) to separate the first reaction chamber 3 and the second reaction chamber 3 so that the oxide film forming reaction shown in FIG. A wire rod 5 made of copper or copper alloy, which is transferred from the first reaction chamber 3 to the second reaction chamber 4, is energized by a roll electrode 6 to serve as an anode, and a plate is placed in the second reaction chamber 4. An anodic oxidation treatment apparatus may be used in which a shaped electrode 7 is provided and used as a cathode.
上記線材5などを第1反応室3に送り込み、第2反応室
4から取り出すことにより、先ず第1反応室3では、主
に過酸化水素による一次酸化反応と硫酸によるエツチン
グ作用を生じさせ、隔膜2の通過後、第2反応室4で、
陽極である銅または銅合金の素材と陰極との間で二次酸
化を行わせる。このように区分することにより、各反応
での反応条件をより最適に設定することが可能となる。
例えば過酸化水素と硫酸の濃度について、第1反応室3
では比較的低く、第2反応室4では比較的高く保つよう
にしてもよい。以上のように本発明により酸化処理され
た銅または銅合金の酸化銅皮膜は、緻密で優れた電気絶
縁性、密着性を示し、本発明の酸化銅皮膜を有する銅ま
たは銅合金は線条体や複雑な形状をした物を含め、電気
絶縁材料として使用することができる。By feeding the wire 5 and the like into the first reaction chamber 3 and taking it out from the second reaction chamber 4, first, in the first reaction chamber 3, a primary oxidation reaction mainly using hydrogen peroxide and an etching action using sulfuric acid occur, and the diaphragm 2, in the second reaction chamber 4,
Secondary oxidation is performed between the copper or copper alloy material that is the anode and the cathode. By classifying in this way, it becomes possible to more optimally set the reaction conditions for each reaction.
For example, regarding the concentration of hydrogen peroxide and sulfuric acid, the first reaction chamber 3
In the second reaction chamber 4, the temperature may be kept relatively low, and in the second reaction chamber 4, it may be kept relatively high. As described above, the copper oxide film of copper or copper alloy that has been oxidized according to the present invention is dense and exhibits excellent electrical insulation and adhesion. They can be used as electrical insulating materials, including those with complex shapes.
特に線材の場合、酸化銅皮膜の膜厚1μm当り120〜
150ボルトの絶縁破壊耐圧を示し、例えばアクリル樹
脂などの適当な樹脂を被覆すれば、そのままマグネツト
ワィヤ一などとしての用途に使用することが可能である
。また酸化銅皮膜は耐食性を有しているので、本発明に
より処理された銅または銅合金は耐食性が要求される種
々の用途、例えば化学薬品などを取り扱う腐食性雰囲気
や300〜400℃になる酸化性高温雰囲気などに使用
されるマグネツトワイヤ一として用いることができる。
その他本発明の処理方法は電子材料の開発にも利用する
ことができる。〈実施例〉
20φの銅線をトリクレンで充分に脱脂後、35v01
(f)過酸化水素(工業用、日本パーオキサイド株製)
に硫酸を0.5,L2,3.4,5,6,7,8.10
v01%添加した水溶液を作り、室温でL2.3.4,
5.6.7,8.9,lO.l2.l4.l6ボルトの
定電圧をかけ、各々0.5.1.2,3.4.5分間陽
極酸化処理をした。Especially in the case of wire rods, 120 to 120 per μm of copper oxide film thickness
It exhibits a dielectric breakdown voltage of 150 volts, and if coated with a suitable resin such as acrylic resin, it can be used as it is as a magnet wire. In addition, since the copper oxide film has corrosion resistance, the copper or copper alloy treated according to the present invention can be used in various applications where corrosion resistance is required, such as in corrosive atmospheres handling chemicals and oxidation at temperatures of 300 to 400°C. It can be used as a magnet wire used in high temperature atmospheres.
In addition, the processing method of the present invention can also be used for the development of electronic materials. <Example> After thoroughly degreasing a 20φ copper wire with Triclean, 35v01
(f) Hydrogen peroxide (industrial use, manufactured by Nippon Peroxide Co., Ltd.)
Add sulfuric acid to 0.5, L2, 3.4, 5, 6, 7, 8.10
Make an aqueous solution with v01% added, L2.3.4, at room temperature.
5.6.7, 8.9, lO. l2. l4. A constant voltage of 16 volts was applied, and anodization was performed for 0.5, 1.2, and 3.4.5 minutes, respectively.
この処理後、水洗、乾燥した試料についてその酸化皮膜
の一層分(約0.3〜1.2μm)の電気絶縁破壊耐圧
を測定したところ、実用的諸条件下に卦いて、第2図な
いし第4図に示すような結果を得た。尚、陰極はステン
レス板を用いた。また、第1図の硫酸濃度の変化による
絶縁破壊耐圧の場合は、参考までに35v0101)過
酸化水素と種々濃度の硫酸との混合水溶液中に10分間
浸漬のみしたときに形成される酸化銅皮膜の絶縁破壊耐
圧値も書き加えた。尚、各図に卦いて、絶縁破壊耐圧の
測定値はn=3とし、その上下限を縦方向の矢印で示し
、その平均値を黒丸または白丸で示した。After this treatment, the electrical breakdown voltage of one layer (approximately 0.3 to 1.2 μm) of the oxide film was measured on the sample after washing and drying. The results shown in Figure 4 were obtained. Note that a stainless steel plate was used as the cathode. In addition, in the case of dielectric breakdown voltage due to changes in sulfuric acid concentration shown in Figure 1, please refer to 35v0101) Copper oxide film formed when immersed for 10 minutes in a mixed aqueous solution of hydrogen peroxide and sulfuric acid at various concentrations. Also added the dielectric breakdown voltage value. In each figure, the measured values of the dielectric breakdown voltage were set to n=3, the upper and lower limits thereof are shown by vertical arrows, and the average value is shown by a black circle or a white circle.
上記各図によると、先ず、第2図に卦いて、本発明の酸
化銅皮膜が単に浸漬のみしたものに対し、絶縁破壊耐圧
がかなり高く、硫酸濃度を最適値に設定すると、120
〜150ボルトにも達することがわかる。According to each of the above figures, first of all, as shown in Fig. 2, the dielectric breakdown voltage of the copper oxide film of the present invention is considerably higher than that of the one simply immersed, and when the sulfuric acid concentration is set to the optimum value,
It can be seen that the voltage reaches ~150 volts.
また、第3図から極間電圧が4〜7ボルト程度に卦いて
、高い絶縁破壊耐圧が得られることがわかる。また、第
4図に卦いて陽極酸化時間は0.5〜2分程度が最も好
ましいことがわかる。また35(fl)過酸化水素水に
硫酸を0.0.5,3,6,10v0.11(I)で添
加した水溶液を作り、これに2.0φの銅線を浸漬させ
、極間電圧を1,5,8.12Vとし、電解時間を0.
5.1,2,5分として陽極酸化した場合の試料につい
て、自己径巻付後の線材の表面状態を粉ふき、クラツク
の発生などから観察した結果を示すと次表の如くであつ
た。Further, from FIG. 3, it can be seen that the voltage between electrodes is about 4 to 7 volts, and a high dielectric breakdown voltage can be obtained. Moreover, it can be seen from FIG. 4 that the most preferable anodic oxidation time is about 0.5 to 2 minutes. In addition, an aqueous solution was prepared by adding sulfuric acid to 35 (fl) hydrogen peroxide solution at 0.0.5, 3, 6, 10v0.11 (I), and a 2.0φ copper wire was immersed in this solution, and the voltage between electrodes was were set to 1, 5, and 8.12V, and the electrolysis time was set to 0.
5. Regarding the samples anodized for 1, 2, and 5 minutes, the surface condition of the wire rod after self-diameter winding was wiped with powder and observed from the occurrence of cracks, etc. The results are shown in the following table.
この表によると、電気特性と共に、外観や密着性の面か
らも適正な浴組成、陽極酸化条件が存在することがわか
る。以上説明したように本発明の銅または銅合金の酸化
処理法は、銅または銅合金を過酸化水素5〜50v01
q11卦よび硫酸0.5〜6.0v01(f)を含む混
合水溶液中で陽極酸化処理するものであるため、従来法
による酸化銅皮膜に比べて、格段の絶縁破壊耐圧を有す
る緻密で密着性の優れた酸化皮膜を生成することができ
る。According to this table, it can be seen that there are appropriate bath compositions and anodizing conditions in terms of not only electrical properties but also appearance and adhesion. As explained above, the oxidation treatment method for copper or copper alloy of the present invention is to oxidize copper or copper alloy to 5 to 50v01 of hydrogen peroxide.
Because it is anodized in a mixed aqueous solution containing q11 trigrams and sulfuric acid 0.5 to 6.0v01(f), it has a dense and adhesive coating with much higher dielectric breakdown voltage than copper oxide coatings made by conventional methods. can produce an excellent oxide film.
しかも非常に短時間でかつ室温付近の処理温度で酸化処
理できるため、製造コストも安くて済む。また処理温度
が低くてよいことは反応装置の腐食が少なくて済むなど
の利点もある。さらに定電圧処理を行うことにより、電
圧コントロール操作がし易いなどの利点もある。Moreover, since the oxidation treatment can be performed in a very short time and at a treatment temperature near room temperature, the manufacturing cost is also low. Furthermore, the fact that the treatment temperature can be low has the advantage that corrosion of the reactor can be reduced. Further, by performing constant voltage processing, there are also advantages such as ease of voltage control operation.
第1図は本発明方法を適用して有用な処理装置の概略を
示す説明図、第2図ないし第4図は本発明方法により得
た酸化銅皮膜に卦いて絶縁破壊耐圧と硫酸濃度、陽極酸
化極間電圧卦よび陽極酸化時間との関係を示すグラフ図
である。Fig. 1 is an explanatory diagram showing the outline of a useful processing apparatus applying the method of the present invention, and Figs. 2 to 4 show the dielectric breakdown voltage, sulfuric acid concentration, anode FIG. 2 is a graph diagram showing the relationship between oxidizing electrode voltage and anodic oxidation time.
Claims (1)
び硫酸0.5〜6.0vol%を含む混合水溶液中で陽
極酸化処理し、酸化銅皮膜を形成させることを特徴とす
る銅または銅合金の酸化処理方法。1. Copper or copper alloy which is characterized by anodizing copper or copper alloy in a mixed aqueous solution containing 5 to 50 vol% hydrogen peroxide and 0.5 to 6.0 vol% sulfuric acid to form a copper oxide film. Oxidation treatment method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5175981A JPS599639B2 (en) | 1981-04-08 | 1981-04-08 | Oxidation treatment method for copper or copper alloy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5175981A JPS599639B2 (en) | 1981-04-08 | 1981-04-08 | Oxidation treatment method for copper or copper alloy |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57169100A JPS57169100A (en) | 1982-10-18 |
| JPS599639B2 true JPS599639B2 (en) | 1984-03-03 |
Family
ID=12895867
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5175981A Expired JPS599639B2 (en) | 1981-04-08 | 1981-04-08 | Oxidation treatment method for copper or copper alloy |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS599639B2 (en) |
-
1981
- 1981-04-08 JP JP5175981A patent/JPS599639B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57169100A (en) | 1982-10-18 |
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