JPS609600B2 - Anodizing treatment method - Google Patents
Anodizing treatment methodInfo
- Publication number
- JPS609600B2 JPS609600B2 JP15254377A JP15254377A JPS609600B2 JP S609600 B2 JPS609600 B2 JP S609600B2 JP 15254377 A JP15254377 A JP 15254377A JP 15254377 A JP15254377 A JP 15254377A JP S609600 B2 JPS609600 B2 JP S609600B2
- Authority
- JP
- Japan
- Prior art keywords
- bubbles
- electrolyte
- frequency
- treatment method
- current density
- 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
Links
- 238000000034 method Methods 0.000 title claims description 16
- 238000007743 anodising Methods 0.000 title claims description 10
- 239000008151 electrolyte solution Substances 0.000 claims description 10
- 229910000838 Al alloy Inorganic materials 0.000 claims description 7
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 5
- 239000003792 electrolyte Substances 0.000 description 20
- 238000005868 electrolysis reaction Methods 0.000 description 10
- 239000010407 anodic oxide Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 241000124033 Salix Species 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 1
- 235000011613 Pinus brutia Nutrition 0.000 description 1
- 241000018646 Pinus brutia Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000002048 anodisation reaction Methods 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Landscapes
- Electrochemical Coating By Surface Reaction (AREA)
Description
【発明の詳細な説明】
本発明はアルミニウムまたはアルミニウム合金よりなる
成形品の陽極酸化処理法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of anodizing a molded article made of aluminum or an aluminum alloy.
アルミニウムまたはアルミニウム合金よりなる成形品の
陽極酸化処理法は電解液中に浸潰した被処理物を陽極と
するとともに該被処理物に対向させた鉛またはカーボン
を陰極として電解するのを普通とするが、電解時間を短
縮するため電流密度を高めると色むらや焼け(バーニン
グ)の現象を生じることとなる。In the anodizing treatment method for molded products made of aluminum or aluminum alloy, the object to be treated immersed in an electrolytic solution is used as an anode, and lead or carbon placed opposite the object to be treated is used as a cathode for electrolysis. However, if the current density is increased to shorten the electrolysis time, uneven coloring and burning will occur.
そこで、電解液を鷹拝させつつ電解を行うことにより電
流密度を高めても色むらや焼けの現象が生じることのな
いようにした陽極酸化処理法が種々提案されているが、
従来のこの種陽極酸化処理法による場合でも電流密度を
最高1私/d〆程度までしか高められず。電解時間の短
縮化が不充分で効率的な陽極酸化処理法とは云い難い。
本発明はこのような現状に鑑み開発された効率的な陽極
酸化処理法を目的として完成されたもので、アルミニウ
ムまたはアルミニウム合金よりなる成形品の陽極酸化処
理法において、電解液中に平均径が0.01〜4肋の無
数の微小な気泡を発生させて浮上するこの微小な気泡を
振動数10〜200ヘルツの振動により揺動させながら
高電流密度で電解することを特徴とするものである。Therefore, various anodic oxidation treatment methods have been proposed in which the electrolysis is carried out while the electrolytic solution is being fed, thereby preventing color unevenness and burning phenomena even if the current density is increased.
Even when using this type of conventional anodic oxidation treatment method, the current density can only be increased to a maximum of about 1 I/d. It is difficult to say that this is an efficient anodizing treatment method because the electrolysis time is insufficiently shortened.
The present invention was completed with the aim of providing an efficient anodizing treatment method developed in view of the current situation.In the anodizing treatment method for molded products made of aluminum or aluminum alloy, the average diameter is It is characterized by electrolyzing at a high current density while generating countless microscopic bubbles of 0.01 to 4 ribs and shaking these floating microbubbles with vibrations at a frequency of 10 to 200 Hz. .
本発明は電解液中に浸溝したアルミニウムまたはアルミ
ニウム合金よりなる成形品を被処理物としてこれを陽極
とするとともに被処理物に対向させた鉛またはカーボン
を陰極として電解を行う点において周知のこの種陽極酸
化処理法と同様であるが、本発明においては電解槽の底
部に例えば平均径0.0005側〜0.5肋程度の微小
な通気孔を無数に形成したセラミックス材または耐酸性
金属の多孔質暁絹材或いは合成樹脂の暁結多孔材等の多
孔質材よりなる散気筒や散気板その他の散気装置を設け
てこの散気装置より圧送供給される空気によって電解液
中に平均径が0.001〜4肋の微小な気泡を発生させ
ている点と、電磁式振動発生機や偏心回転振動機或いは
空圧振動機その他任意の振動機を被処理物固定治具に接
触させるか振動機の振動板を電解液中に浸済させる等の
手段により電解液中の被処理物または電解液に振動数1
0〜200ヘルツの振動を与えて電解液中に発生した前
記微小な気泡を揺動させながら浮上させる点に特徴があ
り、このような条件の電解液中において電解を行うこと
によって最高20A/dの程度まで電流密度を高めても
色むらや焼けの現象の生じることをなくし処理時間の短
縮化を可能とした点にある。The present invention utilizes a molded article made of aluminum or aluminum alloy immersed in an electrolytic solution as an object to be treated, and conducts electrolysis using this as an anode and lead or carbon facing the object as a cathode. Although it is similar to the seed anodization treatment method, in the present invention, a ceramic material or an acid-resistant metal is used in which countless minute ventilation holes with an average diameter of about 0.0005 to 0.5 ribs are formed at the bottom of the electrolytic cell. A diffuser tube, a diffuser plate, or other aeration device made of porous material such as porous silk material or synthetic resin porous material is provided, and the air supplied under pressure from the aeration device is used to disperse an average amount of air into the electrolyte. Micro bubbles with a diameter of 0.001 to 4 ribs are generated, and an electromagnetic vibration generator, eccentric rotation vibrator, pneumatic vibrator, or any other vibrator is brought into contact with the workpiece fixing jig. Or, by immersing the diaphragm of a vibrator in the electrolyte, the object to be treated in the electrolyte or the electrolyte has a frequency of 1.
The feature is that vibrations of 0 to 200 Hz are applied to cause the minute bubbles generated in the electrolyte to float while oscillating, and by performing electrolysis in the electrolyte under these conditions, a maximum of 20 A/d can be generated. Even if the current density is increased to such a degree, color unevenness and burning phenomena do not occur, and processing time can be shortened.
即ち、電解液中において発生して浮上する前記の微小な
気泡を振動数10〜200ヘルツの振動により揺動させ
てこの微小な気泡の浮上径路を撹乱させて電解液のすみ
ずみまで微小な気泡をゆきわたらせ、この揺動しながら
浮上する微小な気泡による損梓作用によって電解液をす
みずみまで蝿拝するから、電解液の温度が均一となり、
その結果、高電流密度で電解することによって被処理物
の一部分が発熱してもその高温部を電解液が冷却して低
い温度に下げ、焼けの発生を防止するから高電流密度で
短時間の電解により目的とする厚さの陽極酸化皮膜を生
成させうるものである。なおも電解液中において発生さ
せる微小な気泡の平均径を0.001〜4側としたのは
、通常は被処理物附近における平均径が4肌を超えると
気泡に働く浮力が大きく、電解液中を直線的に直上へ上
昇して彼処理物の表面近くを通過することが少なくも従
って、被処理物近くの電解液の蝿梓が弱くて電解液温を
均一化して冷却する効果が少ない。従って、気泡に働く
浮力が少なくて前記のような振動数の振動により振動し
ながら浮上して被処理物附近をよく蝿拝するよう気泡径
の上限は被処理物附近における平均径が約4側程度であ
り、また「気泡径の下限は微細なほどよいが、0.00
1柳未満の気泡は気泡発生上困難を伴うため被処理物附
近における平均径が0.001肌以上の気泡が一般的と
考えられるためである。他方、振動数を10〜200ヘ
ルツに限定する理由は、彼処理物附近における平均径が
4肌の気泡を電解液中に発生させながら電解を行った場
合に、10ヘルツ未満では気泡を含んだ電解液をゆるや
かに揺動させるのみで気泡の直上への上昇径路を潰乱さ
せるだけの揺動を与えることにならないから、気泡を電
解液のすみずみまでただよわせて液温を均一とする作用
がおこらず、また、振動数200ヘルツを超えると「振
動エネルギーが吸収されて熱に変化するのみで気泡は動
かされないから、気泡の直上方向への上昇径路を蝿乱さ
せるだけの揺動を与えることにならず「前記した振動数
10ヘルツ以下の場合と同機に局部的に高温化して焼け
を生じ、電流密度を高くして処理時間の短縮化をはかる
ことができないからである。なお、前記した平均径と振
動数との間には、実験的に相関が認められており、平均
律が小さいときには振動数の多いところに、平均律が大
きいときは振動数の少ないところに極大の効果を生じる
傾向が認められた。即ち、第2図にも直線X−Xとして
示したように「平均気泡径0.001側では振動数80
ヘルツ付近に、また、平均気泡径4側では振動数40ヘ
ルツ付近に極大の皮膜生成速度が得られている。実施例
Sio.25%以下、Feo.40%以下、Cuo.0
2%以下、Tio.02%以下、Mno.02%以下を
含むアルミニウム合金よりなる長さ20比吻、中5仇舷
、厚さ2肋の板材を長さ方向一端より5物舷および15
0側の位置で直角に折り曲げコ字型とした被処理物1を
第1図に示すように電源2に陽極として接続するととも
に鉛板を陰極3として電源に接続して彼処理物亀と対向
させ、被処理物1の固定治具4に電磁式の振動発生機5
を固定するとともに電解槽6の底部に微小な気泡を発生
する散気装置7を設け、硫酸20%、水80%からなる
電解液8を電解槽6中に満たして微小な気泡の平均径お
よび振動数を変えて陽極酸化処理を行った。That is, the above-mentioned minute bubbles generated and floating in the electrolytic solution are shaken by vibrations at a frequency of 10 to 200 hertz, and the floating path of these minute bubbles is disturbed, so that the minute bubbles are spread to every corner of the electrolyte. As the electrolyte is spread throughout the electrolyte, the temperature of the electrolyte becomes uniform and
As a result, even if a part of the object to be treated heats up due to electrolysis at a high current density, the electrolyte cools the high-temperature part and lowers it to a low temperature, preventing the occurrence of burns. It is possible to generate an anodic oxide film of a desired thickness by electrolysis. The reason why the average diameter of the micro bubbles generated in the electrolytic solution is set at 0.001 to 4 is because normally, when the average diameter near the object to be treated exceeds 4, the buoyancy acting on the bubbles becomes large, and the electrolytic solution The electrolyte rises directly above the object in a straight line and rarely passes near the surface of the object to be processed, so the electrolyte near the object is weak and has little effect on uniformizing the temperature of the electrolyte and cooling it. . Therefore, the upper limit of the bubble diameter is set so that the average diameter near the object to be processed is about 4, so that the buoyant force acting on the bubbles is small and the bubbles float while vibrating due to the vibrations at the above-mentioned frequency and fly close to the object to be processed. "The lower limit of the bubble diameter is the finer the better, but 0.00
This is because bubbles smaller than 1 willow are difficult to generate, and therefore bubbles with an average diameter of 0.001 or more in the vicinity of the object to be treated are considered to be common. On the other hand, the reason for limiting the frequency to 10 to 200 Hz is that when electrolysis is performed while generating bubbles with an average diameter of 4 skin in the electrolytic solution near the object to be treated, if the frequency is less than 10 Hz, the bubbles will not be included. By only gently shaking the electrolyte, the vibration will not be sufficient to disrupt the upward path of the bubbles, so the effect is to make the bubbles flow throughout the electrolyte and make the liquid temperature uniform. If this does not occur and the frequency exceeds 200 Hz, the vibrational energy is absorbed and converted into heat, but the bubbles are not moved, so the vibration is sufficient to disturb the upward path of the bubbles. This is because, as in the case where the vibration frequency is 10 hertz or less, the same machine locally becomes hot and burns, and it is not possible to shorten the processing time by increasing the current density. It has been experimentally confirmed that there is a correlation between the average diameter and the frequency of vibration, and when the equal temperament is small, the maximum effect is at the place where the frequency is high, and when the equal temperament is large, the maximum effect is at the place where the frequency is low. In other words, as shown in Figure 2 as a straight line X-X, a vibration frequency of 80
The maximum film formation rate was obtained near Hertz, and at a frequency of about 40 Hertz on the average bubble diameter side of 4. Example Sio. 25% or less, Feo. 40% or less, Cuo. 0
2% or less, Tio. 02% or less, Mno. A plate material made of an aluminum alloy containing 0.2% or less and having a length of 20 ratios, 5 sides in the middle, and 2 ribs in thickness is made of aluminum alloy with 5 sides and 15 sides from one end in the length direction.
As shown in Fig. 1, the object to be processed 1 bent at a right angle into a U-shape is connected to a power source 2 as an anode, and a lead plate is connected to the power source as a cathode 3 to face the object to be processed. An electromagnetic vibration generator 5 is attached to the fixing jig 4 for the workpiece 1.
An aeration device 7 is installed at the bottom of the electrolytic cell 6 to fix the bubbles and generate minute bubbles. Anodizing was performed by changing the vibration frequency.
第2図のグラフにおいて、曲線A,B,Cは電解液中に
被処理物附近における平均径が夫々0.001肋「0.
01伽、4柳の微小な気泡を発生させつつ種々の振動を
与えながら電流密度20A/dめで電解したときの陽極
酸化皮膜の生成速度と振動数との関係を示すをもので、
点線部は焼けを生じた部分である。In the graph of FIG. 2, curves A, B, and C each have an average diameter of 0.001 "0.001" in the vicinity of the object to be treated in the electrolytic solution.
This shows the relationship between the generation rate of the anodic oxide film and the vibration frequency when electrolyzing at a current density of 20 A/d while generating various vibrations while generating 01 and 4 willow minute bubbles,
The dotted line area is the area where the burn occurred.
比較のため平均径0.01肌の微小な気泡を電解液中の
被処理物附近に発生させて電流密度1松/dめで電解し
たときの陽極酸化皮膜生成を記せば4.5山肌/分であ
り、また、微小な気泡を発生させることなく被処理物に
例えば振動数20キロヘルッの超音波振動を与えながら
、電流密度1船/dめで電解したときの皮膜生成速度を
託せば4.2仏肌/分である。ところが、グラフに示さ
れるように、例えば被処理物附近における微小な気泡の
平均径を0.001肌とし、かつ、この微小な気泡を振
動数120ヘルツの振動により振動させながら彼処理物
の表面において電流密度20A/dめの条件で電解した
ときの初期5分間の皮膜生成平均速度は8.8〆仇/分
であるから、本発明方法がいかに処理時間を短縮できる
方法であるかが明らかである。本発明は以上の説明によ
って明らかなように、電解液中に平均径が0.001〜
4柳の微小な気泡を発生させるとともに電解液中を浮上
するこの微小な気泡を振動数10〜200ヘルツの振動
により揺動させて微4・な気泡の浮上径路を櫨乱させな
がら電解するようにしたから、微小な気泡による鷹洋作
用によって電解液の温度はすみずみまで均一となり、そ
の結果、高電流密度で電解することにより被処理物の一
部分が発熱してもその高温部を電解液が冷却して低い温
度に下げ、焼けの発生を防止するから高電流密度で電解
することが可能となり、目的とする厚さの陽極酸化皮膜
を生成させるに必要な時間を約1/2にまで短縮できる
陽極酸化処理法として産業の発展に寄与するところが大
きいものである。For comparison, the anodic oxide film produced when microbubbles with an average diameter of 0.01 pores are generated near the object to be treated in the electrolytic solution and electrolyzed at a current density of 1 pine/d is 4.5 pores/min. Also, the film formation rate when electrolyzed at a current density of 1 ship/d while applying ultrasonic vibrations of a frequency of 20 kilohertz to the object to be treated without generating minute bubbles is 4.2. Buddha skin/minute. However, as shown in the graph, for example, if the average diameter of minute bubbles near the workpiece is set to 0.001, and the minute bubbles are vibrated with vibrations at a frequency of 120 Hz, the surface of the workpiece is When electrolyzing at a current density of 20 A/d, the average rate of film formation during the initial 5 minutes was 8.8 m/min, which clearly shows how the method of the present invention can shorten the processing time. It is. As is clear from the above description, the present invention has an average diameter of 0.001 to
This method generates microscopic bubbles and shakes the microbubbles floating in the electrolyte with vibrations at a frequency of 10 to 200 Hz to disturb the floating path of the microbubbles while electrolyzing. As a result, the temperature of the electrolyte becomes uniform throughout due to the hawk effect caused by minute bubbles, and as a result, even if a part of the object to be treated generates heat due to electrolysis at a high current density, the electrolyte does not cover the high-temperature part. Since it is cooled to a low temperature and prevents burns, it is possible to electrolyze at a high current density, reducing the time required to generate an anodic oxide film of the desired thickness to approximately 1/2. As a possible anodizing treatment method, it will greatly contribute to the development of industry.
第1図は本発明方法の実施説明図、第2図は本発明方法
における陽極酸化皮膜生成速度と振動数との関係を示す
グラフである。
1:被処理物、2:電源「 3:陰極、4:固定治具、
5:振動発生機、6:電解槽、71:散気装置、8:電
解液。
第1図
第2図FIG. 1 is a diagram illustrating the implementation of the method of the present invention, and FIG. 2 is a graph showing the relationship between the rate of anodic oxide film formation and the frequency in the method of the present invention. 1: Processed object, 2: Power supply, 3: Cathode, 4: Fixing jig,
5: Vibration generator, 6: Electrolytic cell, 71: Diffuser, 8: Electrolyte. Figure 1 Figure 2
Claims (1)
品の陽極酸化処理法において、電解液中に平均径が0.
001〜4mmの無数の微小な気泡を発生させて浮上す
るこの微小な気泡を振動数10〜200ヘルツの振動に
より揺動させながら高電流密度で電解することを特徴と
する陽極酸化処理法。1. In an anodizing treatment method for molded products made of aluminum or aluminum alloy, an average diameter of 0.05 mm is added to the electrolytic solution.
An anodizing process characterized by generating countless minute bubbles of 0.001 to 4 mm and electrolyzing them at a high current density while shaking the floating minute bubbles with vibrations at a frequency of 10 to 200 hertz.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15254377A JPS609600B2 (en) | 1977-12-19 | 1977-12-19 | Anodizing treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15254377A JPS609600B2 (en) | 1977-12-19 | 1977-12-19 | Anodizing treatment method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5484840A JPS5484840A (en) | 1979-07-06 |
| JPS609600B2 true JPS609600B2 (en) | 1985-03-11 |
Family
ID=15542746
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15254377A Expired JPS609600B2 (en) | 1977-12-19 | 1977-12-19 | Anodizing treatment method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS609600B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6029493A (en) * | 1983-07-20 | 1985-02-14 | Pentel Kk | Manufacture of aluminum or aluminum alloy substrate having oxide film |
| JP3046594B1 (en) * | 1999-04-02 | 2000-05-29 | 日本テクノ株式会社 | Anodizing system for metals utilizing vibrating flow agitation |
-
1977
- 1977-12-19 JP JP15254377A patent/JPS609600B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5484840A (en) | 1979-07-06 |
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