JP2000355795A - Surface treatment of aluminum and aluminum alloy - Google Patents

Surface treatment of aluminum and aluminum alloy

Info

Publication number
JP2000355795A
JP2000355795A JP11168221A JP16822199A JP2000355795A JP 2000355795 A JP2000355795 A JP 2000355795A JP 11168221 A JP11168221 A JP 11168221A JP 16822199 A JP16822199 A JP 16822199A JP 2000355795 A JP2000355795 A JP 2000355795A
Authority
JP
Japan
Prior art keywords
aqueous solution
electrolysis
aluminum alloy
acid
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.)
Pending
Application number
JP11168221A
Other languages
Japanese (ja)
Inventor
Masaaki Ono
雅章 小野
Hitoshi Niimura
仁 新村
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.)
Aisin Keikinzoku Co Ltd
Aisin Corp
Original Assignee
Aisin Seiki Co Ltd
Aisin Keikinzoku Co 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 Aisin Seiki Co Ltd, Aisin Keikinzoku Co Ltd filed Critical Aisin Seiki Co Ltd
Priority to JP11168221A priority Critical patent/JP2000355795A/en
Publication of JP2000355795A publication Critical patent/JP2000355795A/en
Pending legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Other Surface Treatments For Metallic Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To make it possible to form a normal coating film free of discoloration by chemically forming an anodically oxidized film on the surface of an aluminum alloy, electrically preparing the micropore structure of the film, depositing metal ions on the bottoms of micropores, neutralizing the inside of the micropores and subjecting the surface to cation electrodeposition coating by cathode deposition type acrylic resin coating. SOLUTION: The stage yields the oxidized film by an anodic oxidation treatment with DC or pulse waveforms by an aqueous solution containing at least >=1 kind of selected sulfuric acid, oxalic acid, chromic acid, phosphoric acid and aromatic sulfonic acid and executes an AC electrolysis with the same aqueous solution at lower voltage. In succession, the alloy is subjected to the AC electrolysis with the aqueous solution containing >=1 kind of Sn, Co, Ni, Cu and Fe, then to the AC electrolysis with the aqueous solution containing at least >=1 kind of ammonium acetate and ammonium sulfate. Finally, the aluminum alloy side is subjected to the DC electrolysis with the aqueous solution containing a cathode deposition type acrylic resin. The transparent coating film which maintains the color tones of multicolor electrolytic coloration and has excellent quality may be formed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明はアルミニウムおよび
アルミニウム合金(以下、アルミニウム合金という)の
表面処理方法に関し、特に電解着色法にて着色した陽極
酸化皮膜に、電着塗装した複合皮膜処理に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a surface treatment method for aluminum and an aluminum alloy (hereinafter, referred to as an aluminum alloy), and more particularly to a composite film treatment in which an anodized film colored by an electrolytic coloring method is electrodeposited.

【0002】[0002]

【従来の技術】アルミニウム合金製の押出形材や圧延材
を硫酸、リン酸、クロム酸、しゅう酸、芳香族スルホン
酸等の水溶液中にて陽極酸化皮膜を化成し、その後にス
ズ、ニッケル、コバルト等の金属イオンを含有する酸性
水溶液中にて交流電解して電解着色し、さらに一般に電
着塗装といわれているアクリル塗料系水溶性塗料中にて
電気泳動法にて塗膜形成させる工法が広く実施されてい
る。
2. Description of the Related Art Extruded and rolled aluminum alloy materials are formed into an anodic oxide film in an aqueous solution of sulfuric acid, phosphoric acid, chromic acid, oxalic acid, aromatic sulfonic acid, etc., and then tin, nickel, There is a method in which alternating current electrolysis is carried out in an acidic aqueous solution containing metal ions such as cobalt and electrolytic coloring is performed, and then a coating film is formed by electrophoresis in an acrylic paint-based water-soluble paint which is generally called electrodeposition coating. Widely implemented.

【0003】この電着塗装の方法には、製品を陽極にし
て陽極析出型電着塗料を用いて電解するアニオン電着塗
装(塗料がアニオンに電荷している)と、製品を陰極に
して陰極析出型電着塗料を用いて電解するカチオン電着
塗装(塗料がカチオンに電荷している)がある。
[0003] In this electrodeposition coating method, there are an anion electrodeposition coating in which a product is used as an anode and electrolysis is performed using an anodic deposition type electrodeposition paint (the paint is charged to an anion), and a product is used as a cathode and a cathode is used. There is a cationic electrodeposition coating (electrically charged cations) that performs electrolysis using a deposition type electrodeposition coating.

【0004】従来は、アルミニウム合金に陽極酸化皮膜
を化成し、連続的に電着塗装する場合にはアルミニウム
合金側を陽極にしたアニオン電着塗装でなければ正常な
塗膜が形成されないと考えられていた。
Conventionally, when an anodic oxide film is formed on an aluminum alloy and electrodeposition coating is performed continuously, it is considered that a normal coating film cannot be formed unless anion electrodeposition coating is performed with the aluminum alloy side as an anode. I was

【0005】その理由として、アルミニウム合金側を陰
極にすると、下地処理として化成した陽極酸化皮膜が水
溶液中の水素イオン(H+)のガス化により、皮膜破壊
が生じるためとされている。
[0005] The reason is that when the aluminum alloy side is used as a cathode, the anodized film formed as a base treatment is destroyed by gasification of hydrogen ions (H + ) in an aqueous solution.

【0006】しかし、アルミニウム合金に陽極酸化皮膜
を化成後に、該陽極酸化皮膜のポアー径等のポアー構造
を電解調整した後に、金属イオン含有水溶液中で電解着
色する、いわゆる多色電解着色法(3次電解着色法とも
いわれている)を採用後に、透明型アニオン電着塗装を
した場合には、陽極酸化皮膜の電解着色による色調が変
化してしまう技術的課題があった。
However, after forming an anodic oxide film on an aluminum alloy, the pore structure such as the pore diameter of the anodic oxide film is electrolytically adjusted, and then electrolytically colored in an aqueous solution containing metal ions. When the transparent anion electrodeposition coating is performed after adopting the secondary electrolytic coloring method), there is a technical problem that the color tone of the anodic oxide film changes due to the electrolytic coloring.

【0007】その理由として、多色電解着色法は、図1
の模式図に示したように、陽極酸化皮膜6中に析出した
金属イオン2にて反射した光路C2と、アルミニウム合
金表面にて反射した光路C1の干渉にて発色させる着色
法であり、アニオン電着塗装時にアルミニウム合金1が
陽極になり、金属イオンが一部溶出して干渉光が変化す
るためと考えられている。
The reason is that the multicolor electrolytic coloring method uses the method shown in FIG.
As shown in the schematic diagram of FIG. 3, a coloration method is used in which a color is formed by interference between the optical path C2 reflected by the metal ions 2 deposited in the anodic oxide film 6 and the optical path C1 reflected by the aluminum alloy surface. It is considered that the aluminum alloy 1 becomes an anode at the time of coating, metal ions are partially eluted, and interference light changes.

【0008】[0008]

【発明が解決しようとする課題】本発明が解決しようと
する課題は、アルミニウム合金に陽極酸化皮膜を化成
し、多色電解着色法にて電解着色した後に、透明型電着
塗装する方法において、変色がなく、正常な塗膜が形成
できるアルミニウム合金の表面処理方法の提供にある。
The problem to be solved by the present invention is to provide a method of forming an anodized film on an aluminum alloy, electrolytic coloring by a multicolor electrolytic coloring method, and then performing transparent electrodeposition coating. An object of the present invention is to provide a method for surface treatment of an aluminum alloy capable of forming a normal coating film without discoloration.

【0009】[0009]

【課題を解決するための手段】本発明に従ったアルミニ
ウム合金の表面処理方法は、次の工程を経る。
The method for treating the surface of an aluminum alloy according to the present invention includes the following steps.

【0010】第1工程:硫酸、芳香族スルホン酸、しゅ
う酸、クロム酸、リン酸のうち、少なくとも1種以上を
含む水溶液にて、直流またはパルス波形による陽極酸化
処理して陽極酸化皮膜を得る。 第2工程:硫酸、芳香族スルホン酸、しゅう酸、クロム
酸、リン酸のうち、少なくとも1種以上を含む水溶液に
て、第1工程における最終電圧よりも低い電圧にて交流
電解する。 第3工程:Sn、Co、Ni、Cu、Fe金属の塩を少
なくとも1種以上含む水溶液にて交流電解する。 第4工程:酢酸アンモニウム、硫酸アンモニウムのう
ち、少なくとも1種以上含む水溶液にて交流電解する。 第5工程:陰極析出型アクリル樹脂を含む水溶液にて、
アルミニウム合金側を陰極にて直流電解する。
First step: An anodic oxidation film is obtained by anodic oxidation using an aqueous solution containing at least one of sulfuric acid, aromatic sulfonic acid, oxalic acid, chromic acid and phosphoric acid by DC or pulse waveform. . Second step: AC electrolysis is performed with an aqueous solution containing at least one of sulfuric acid, aromatic sulfonic acid, oxalic acid, chromic acid, and phosphoric acid at a voltage lower than the final voltage in the first step. Third step: AC electrolysis is performed with an aqueous solution containing at least one or more salts of Sn, Co, Ni, Cu, and Fe metals. Fourth step: AC electrolysis is performed with an aqueous solution containing at least one of ammonium acetate and ammonium sulfate. Fifth step: In an aqueous solution containing a cathode deposition type acrylic resin,
DC electrolysis is performed on the aluminum alloy side at the cathode.

【0011】次に各工程について、詳細に説明する。Next, each step will be described in detail.

【0012】第1工程は、アルミニウム合金の表面に陽
極酸化皮膜を化成するのが目的である。従って、通常は
脱脂洗浄し、必要に応じてエッチング処理、酸洗処理等
が施され、当該アルミニウム合金を陽極にして鉛板、グ
ラファイト等を陰極にして、直流またはパルス波形にて
電解される。
The first step is to form an anodic oxide film on the surface of the aluminum alloy. Therefore, it is usually degreased and washed, and if necessary, subjected to etching treatment, pickling treatment and the like. Electrolysis is performed with a direct current or a pulse waveform using the aluminum alloy as an anode and a lead plate, graphite or the like as a cathode.

【0013】また、用いられる電解液としては、硫酸、
しゅう酸、クロム酸、リン酸、芳香族スルホン酸等の水
溶液が広く知られている。
The electrolyte used is sulfuric acid,
Aqueous solutions of oxalic acid, chromic acid, phosphoric acid, aromatic sulfonic acids and the like are widely known.

【0014】第2工程は、その後の電解着色にて干渉光
を生じさせるための陽極酸化皮膜のポアー径およびバリ
アー層厚みを調整することを目的とする。
The second step aims at adjusting the pore diameter of the anodic oxide film and the thickness of the barrier layer for generating interference light in the subsequent electrolytic coloring.

【0015】この皮膜調整方法としては各種提案されて
いるが、大きく分けてポアー底部ポアー径を拡大するタ
イプ(特開平6−49688号)と、ポアー底部を枝分
かれ状の微細孔にするタイプ(特許第2534805
号)の2種類がある。
There have been proposed various methods of adjusting the film. The method of broadly dividing the pore diameter at the bottom of the pore (JP-A-6-49688) and the method of forming the pore bottom at a branched fine hole (Patent) No. 2534805
No.).

【0016】ポアー底部の径を拡大するタイプにおいて
は、第1工程の陽極酸化皮膜を硫酸水溶液等の溶解性の
強い電解液を用いて、その後の皮膜調整液にリン酸水溶
液等の弱溶解性の電解液にて該底部のポアー径拡大およ
びバリアー層厚みを調整することになる。
In the type in which the diameter of the bottom of the pore is enlarged, the anodic oxide film in the first step is formed by using an electrolytic solution having a high solubility such as a sulfuric acid aqueous solution and then weakly dissolving a phosphoric acid aqueous solution or the like in the subsequent film adjusting solution. With this electrolytic solution, the pore diameter at the bottom is increased and the thickness of the barrier layer is adjusted.

【0017】一方、ポアー底部に枝分かれ状の微細孔に
するタイプでは、陽極酸化処理電圧を第1工程時の処理
電圧に対して一定割合に低下させるか、交流電解処理等
にて皮膜調整することになるが、次の第3工程にて安定
的に各種色調を得るには、第1工程の最終電圧よりも低
い電圧にて交流電解するのが望ましい。図1に示すバリ
アー層4が均一になるからである。また、用いられる電
解液としては、硫酸、しゅう酸、クロム酸、リン酸、芳
香族スルホン酸等の水溶液が広く知られている。
On the other hand, in the type in which the pores are formed as branched micropores at the bottom of the pore, the anodic oxidation treatment voltage is reduced at a fixed rate with respect to the treatment voltage in the first step, or the film is adjusted by AC electrolytic treatment or the like. However, in order to stably obtain various color tones in the next third step, it is desirable to carry out AC electrolysis at a voltage lower than the final voltage in the first step. This is because the barrier layer 4 shown in FIG. 1 becomes uniform. Further, as the electrolytic solution to be used, aqueous solutions of sulfuric acid, oxalic acid, chromic acid, phosphoric acid, aromatic sulfonic acid and the like are widely known.

【0018】第3工程の電解着色工程は、Sn、Cu、
Ni、Co、Fe等の金属塩を含む水溶液中にて対極に
グラファイト、アルミニウム合金、ステンレススチール
等を用いて交流電解する。
In the third electrolytic coloring step, Sn, Cu,
In an aqueous solution containing a metal salt such as Ni, Co, and Fe, alternating current electrolysis is performed using graphite, an aluminum alloy, stainless steel, or the like as a counter electrode.

【0019】第4工程の電解中和工程は、第5工程とと
もに本発明の最も特徴となる部分であるが、その目的は
第1〜第3工程にて生じたポアー中の電解液を中和し、
次の第5工程にてカチオン塗装を可能にすることにあ
る。
The electrolytic neutralization step of the fourth step is the most characteristic part of the present invention together with the fifth step, and its purpose is to neutralize the electrolytic solution in the pores generated in the first to third steps. And
The object is to enable cationic coating in the next fifth step.

【0020】具体的には、酢酸アンモニウム、1〜10
g/l水溶液、望ましくは1〜5g/l水溶液を用い
て、電圧5〜20Vにて30〜300秒、望ましくは3
0〜180秒間交流電解処理をする。
Specifically, ammonium acetate, 1-10
g / l aqueous solution, preferably 1 to 5 g / l aqueous solution at a voltage of 5 to 20 V for 30 to 300 seconds, preferably 3
Perform AC electrolysis treatment for 0 to 180 seconds.

【0021】それぞれの条件未満では中和の効果が得ら
れず、上限を超えると陽極酸化皮膜が破壊するからであ
る。
This is because the neutralizing effect cannot be obtained if the conditions are less than the respective conditions, and the anodic oxide film is broken if the upper limit is exceeded.

【0022】または、硫酸アンモニウム1〜20g/
l、望ましくは5〜10g/l水溶液を用いて、その他
は上記と同様の条件にて交流電解処理する。
Or 1 to 20 g of ammonium sulfate /
1, preferably 5 to 10 g / l aqueous solution, and the other conditions are the same as above.

【0023】第5工程のカチオン電着塗装は、陰極析出
型アクリル塗料、具体的にはカチオン性アクリル共重合
樹脂とブロックイソシアネート型硬化剤を酢酸、乳酸等
の有機酸と水を、デイスパーやホモミキサーなどの混合
機にて混合して得られる。
The cationic electrodeposition coating in the fifth step is a cathodic deposition type acrylic coating, specifically, a cationic acrylic copolymer resin and a blocked isocyanate type curing agent are treated with an organic acid such as acetic acid and lactic acid and water with a disperser or a homogenizer. It is obtained by mixing with a mixer such as a mixer.

【0024】その際に、固形分が50〜250g/lに
なるように水の量を調整する。50g/l未満では塗膜
生成効率が低下し、250g/lを超えると、つきまわ
り性が低下するからである。
At this time, the amount of water is adjusted so that the solid content becomes 50 to 250 g / l. If the amount is less than 50 g / l, the efficiency of forming a coating film decreases, and if it exceeds 250 g / l, the throwing power decreases.

【0025】かかる水溶性塗料にて対極にグラファイト
を用いて、アルミニウム合金側を陰極にして電圧60〜
120V、望ましくは80〜100Vにて電解する。
The graphite is used as a counter electrode in such a water-soluble paint, and the voltage is 60 to
Electrolyze at 120V, preferably 80-100V.

【0026】100Vを超えると陽極酸化皮膜が破壊さ
れ、60V以下になると塗膜の生成が著しく遅くなるか
らである。
When the voltage exceeds 100 V, the anodic oxide film is destroyed, and when the voltage becomes 60 V or less, the formation of the coating film becomes extremely slow.

【0027】また、電解時間は所定塗膜厚さに合わせて
設定することになり、塗膜厚さ20μmねらいの場合に
は2〜3分となる。
The electrolysis time is set in accordance with the predetermined coating film thickness. When the coating film thickness is 20 μm, it takes 2 to 3 minutes.

【0028】以上説明したように、従来、第1〜第3工
程後にカチオン電着塗装すると、陽極酸化皮膜が破壊し
てしまい、正常な電着塗装塗膜が得られなかったが、本
発明に係る第4工程にてポアー中の酸分を中和し、さら
に第5工程にて低電圧電解によるカチオン塗装をするこ
とで水素イオンのガス化を防止でき、陽極酸化皮膜が破
壊することなく、かつ、電解着色工程における金属イオ
ンが溶出することなく、外観意匠性、耐食性、耐候性、
耐水性に優れたアルミニウム合金の表面処理方法が得ら
れたものである。
As described above, conventionally, when the cationic electrodeposition was applied after the first to third steps, the anodic oxide film was destroyed, and a normal electrodeposition coating film could not be obtained. In the fourth step, the acid content in the pore is neutralized, and in the fifth step, gasification of hydrogen ions can be prevented by performing cation coating by low-voltage electrolysis, without breaking the anodized film. And, without elution of metal ions in the electrolytic coloring step, appearance design, corrosion resistance, weather resistance,
Thus, a surface treatment method for an aluminum alloy having excellent water resistance has been obtained.

【0029】なお、各工程間には充分な水洗工程を設
け、特に第5工程前には60〜80℃にて30〜600
秒の湯洗が望ましくなく、第5工程のカチオン塗装後に
は塗料口液にて洗浄後、純水水洗するのが望ましい。
A sufficient water washing step is provided between each step, especially before the fifth step at 60-80 ° C. for 30-600.
Second water washing is not desirable, and after the cationic coating in the fifth step, it is desirable to wash with a paint mouth liquid and then wash with pure water.

【0030】また、塗膜性能を充分に確保するために、
電着塗装後に160〜180℃にて10〜30分間焼き
付け乾燥させる。
Further, in order to ensure sufficient coating film performance,
After the electrodeposition coating, it is baked and dried at 160 to 180 ° C. for 10 to 30 minutes.

【0031】[0031]

【実施例】[実施例1]アルミニウム合金JIS A6
063S−T5、板厚3mm、幅30mm×長さ300
mmのアルミニウム合金板を工業用弱アルカリ洗剤にて
50℃×5分間洗浄し、水洗後、水酸化ナトリウム10
0g/l、50℃×3分間、エッチング処理し、水洗後
に硝酸150g/l、20℃×1分間酸洗し、水洗後に
硫酸200g/l、対極鉛極板、直流電圧14Vにて2
0℃×30分間、陽極酸化処理して10μmの陽極酸化
皮膜が得られた(第1工程)。
[Example 1] Aluminum alloy JIS A6
063S-T5, thickness 3mm, width 30mm x length 300
mm aluminum alloy plate was washed with an industrial weak alkaline detergent at 50 ° C. for 5 minutes, and after washing with water, sodium hydroxide 10
0 g / l, etching treatment at 50 ° C. × 3 minutes, washing with water, nitric acid 150 g / l, pickling with 20 ° C. × 1 minute, washing with water, sulfuric acid 200 g / l, counter electrode lead plate, DC voltage 14 V
Anodizing treatment was performed at 0 ° C. for 30 minutes to obtain a 10 μm anodic oxide film (first step).

【0032】次に、第2工程として、第1工程に用いた
陽極酸化処理槽にて交流電源を用いて5V、20℃×1
分間電解処理して、陽極酸化皮膜構造を調整した。
Next, as a second step, 5 V, 20 ° C. × 1 using an AC power source in the anodizing tank used in the first step.
The anodic oxide film structure was adjusted by electrolysis for minutes.

【0033】本実施例では、第2工程にて第1工程の電
解液をそのまま用いたので、工程間の水洗を省略した
が、直流による陽極酸化の水溶液と交流電解の水溶液を
異なるものにした場合には、工程間に水洗を設けるのが
望ましい。
In the present embodiment, the electrolytic solution of the first step was used as it is in the second step, so that water washing between the steps was omitted. However, the aqueous solution of anodic oxidation by direct current and the aqueous solution of alternating current electrolysis were different. In this case, it is desirable to provide water washing between steps.

【0034】第3工程として、硫酸第一スズ10g/
l、酒石酸20g/l、硫酸15g/lを含む水溶液を
用いて交流電圧12V、25℃×60秒間電解着色する
と、グレー色の着色陽極酸化皮膜が得られた。
In the third step, stannous sulfate 10 g /
1, an aqueous solution containing tartaric acid 20 g / l and sulfuric acid 15 g / l was subjected to electrolytic coloring at an alternating voltage of 12 V at 25 ° C. for 60 seconds to obtain a gray colored anodic oxide film.

【0035】第4工程として、酢酸アンモニウム2g/
l水溶液中にて交流電圧10V、20℃×3分間電解中
和処理し、水洗後、脱イオン水を用いて70℃×3分間
湯洗洗浄した。
As the fourth step, 2 g of ammonium acetate /
The solution was subjected to electrolytic neutralization treatment in an aqueous solution at an alternating voltage of 10 V and 20 ° C. for 3 minutes, washed with water, and then washed with deionized water at 70 ° C. for 3 minutes.

【0036】第5工程として、カチオン塗料固型分15
0g/lにて直流電圧80V、25℃×3分間電解処理
した後に水洗し、160℃×20分間焼き付け乾燥した
結果、透明塗膜15μmが得られ、グレーの色調は全く
変化しなかった。
In the fifth step, the cationic paint solid component 15
After electrolysis at 0 g / l and DC voltage of 80 V at 25 ° C. for 3 minutes, the film was washed with water and baked and dried at 160 ° C. for 20 minutes. As a result, a transparent coating film of 15 μm was obtained, and the gray color did not change at all.

【0037】[実施例2]アルミニウム合金JIS A
5052P、板厚1.5mm、幅100mm×長さ20
0mmの板材をシンナー洗浄し、リン酸1100g/
l、硝酸30g/l含有水溶液にて98℃×60秒間化
学研磨処理した後に水洗し、硝酸150g/l水溶液に
て20℃×30秒酸洗した後に水洗し、硫酸100g/
l、スルホサリチル酸100g/l、アルミ不純物3g
/l含有水溶液にて、対極グラフアイト直流電流密度1
00A/m2、25℃×30分間陽極酸化処理をした。
最終電圧15Vにて10μmの陽極酸化皮膜が得られ
た。
Example 2 Aluminum Alloy JIS A
5052P, board thickness 1.5 mm, width 100 mm x length 20
0mm plate material is thinner washed and phosphoric acid 1100g /
l, an aqueous solution containing 30 g / l of nitric acid was subjected to a chemical polishing treatment at 98 ° C. for 60 seconds, and then washed with water.
l, sulfosalicylic acid 100 g / l, aluminum impurity 3 g
/ L aqueous solution, the counter electrode graphite DC current density 1
Anodizing treatment was performed at 00 A / m 2 at 25 ° C. for 30 minutes.
At a final voltage of 15 V, a 10 μm anodic oxide film was obtained.

【0038】次に、硫酸150g/lの水溶液にてグラ
ファイト板を対極に交流電圧4V×20℃×120秒電
解処理して皮膜調整した後に水洗した。
Next, the graphite plate was subjected to electrolytic treatment with an aqueous solution of 150 g / l sulfuric acid at the opposite electrode at an AC voltage of 4 V × 20 ° C. × 120 seconds to prepare a film, and then washed with water.

【0039】次に、硫酸ニッケル30g/l、ホウ酸3
0g/l水溶液にて交流電圧15V×25℃×60秒電
解着色すると、鮮やかなグリーンの色調が得られた。
Next, nickel sulfate 30 g / l, boric acid 3
When subjected to electrolytic coloring with an aqueous solution of 0 g / l at an alternating voltage of 15 V × 25 ° C. × 60 seconds, a vivid green color tone was obtained.

【0040】次に、硫酸アンモニウム7g/l水溶液に
て10V×25℃×120秒交流電解にて中和処理をし
た後に水洗し、脱イオン水を用いて80℃×2分間湯洗
洗浄した。
Next, the resultant was subjected to a neutralization treatment with an aqueous solution of ammonium sulfate of 7 g / l at 10 V × 25 ° C. × 120 seconds by alternating current electrolysis, washed with water, and washed with deionized water at 80 ° C. × 2 minutes with hot water.

【0041】次に、実施例1と同液にて100V×2分
間電着塗装し、水洗、焼き付け乾燥した結果、グリーン
の色調が変色することなく12μmの正常な透明塗膜が
得られた。
Next, the same liquid as in Example 1 was applied by electrodeposition at 100 V × 2 minutes, washed with water and baked and dried. As a result, a normal transparent coating film of 12 μm was obtained without discoloration of the green color tone.

【0042】[実施例3]アルミニウム合金JIS A
1100S、板厚3mm、幅30mm×長さ300mm
の押出形材をアルコール脱脂し、水酸化ナトリウム50
g/l、40℃×3分間エッチング処理し、水洗後に硝
酸150g/l、20℃×1分間酸洗し、水洗後に飽和
しゅう酸水溶液25℃にてパルス波形を用いて20V×
30分間陽極酸化処理して、7μmの陽極酸化皮膜が得
られた(第1工程)。
Example 3 Aluminum Alloy JIS A
1100S, board thickness 3mm, width 30mm x length 300mm
Alcohol exfoliates the extruded shape of
g / l, etching treatment at 40 ° C. × 3 minutes, washing with water, pickling with nitric acid 150 g / l, 20 ° C. × 1 minute, washing with water, and then using a saturated oxalic acid aqueous solution at 25 ° C. and a pulse waveform of 20 V ×
Anodizing treatment was performed for 30 minutes to obtain an anodized film of 7 μm (first step).

【0043】第2〜第5工程工程は、実施例1と同様の
処理をした結果、半透明のグレー色調が得られた。
In the second to fifth process steps, the same processing as in Example 1 was performed, and as a result, a translucent gray tone was obtained.

【0044】[比較実施例]比較のために第1〜3工程
までを[実施例1]と同様に処理し、第4工程を省略し
て第5工程にて[実施例1]と同様のカチオン電着塗装
すると、陽極酸化皮膜が破壊し、正常な塗膜も得られな
かった。
[Comparative Example] For comparison, the first to third steps were treated in the same manner as in [Example 1], the fourth step was omitted, and the fifth step was the same as in [Example 1]. When cationic electrodeposition was applied, the anodic oxide film was broken, and a normal coating film could not be obtained.

【0045】[0045]

【発明の効果】本発明に係るアルミニウム合金の表面処
理方法によれば、多色電解着色の色調を維持しつつ、品
質に優れた透明塗膜が化成できた。
According to the surface treatment method for an aluminum alloy according to the present invention, a transparent coating film having excellent quality can be formed while maintaining the color tone of the multicolor electrolytic coloring.

【0046】塗膜の密着性評価において、40℃×50
0時間、脱イオン水に浸漬後、碁盤目付着試験を実施し
た結果、100目マス当たり、はがれ0であった。
In the evaluation of the adhesion of the coating film, 40 ° C. × 50
After immersion in deionized water for 0 hour, a cross-cut adhesion test was carried out. As a result, no peeling occurred per 100 squares.

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

【図1】本発明における多色電解着色の原理を示す模式
図を示す。
FIG. 1 is a schematic view showing the principle of multicolor electrolytic coloring in the present invention.

【符号の説明】[Explanation of symbols]

1 アルミニウム合金 2 ポアー底部に析出した金属イオン 3 ポアー 4 バリアー層 5 透明塗膜 6 陽極酸化皮膜 C1、C2 光路 DESCRIPTION OF SYMBOLS 1 Aluminum alloy 2 Metal ion deposited at the bottom of pore 3 Pore 4 Barrier layer 5 Transparent coating film 6 Anodized film C1, C2 Optical path

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 少なくとも次の工程を経るアルミニウム
合金の表面処理方法。 (1)アルミニウム合金の表面に陽極酸化皮膜を化成す
る陽極酸化処理工程。 (2)陽極酸化皮膜の微細ポアー構造の電解調整工程。 (3)金属イオンを該微細ポアー底部に析出させる電解
着色工程。 (4)該微細ポアー内を中和する電解中和工程。 (5)陰極析出型アクリル樹脂塗料を用いたカチオン電
着塗装工程。
1. A method for treating a surface of an aluminum alloy through at least the following steps. (1) Anodizing step of forming an anodized film on the surface of the aluminum alloy. (2) An electrolytic adjustment step of a fine pore structure of the anodic oxide film. (3) An electrolytic coloring step of depositing metal ions on the bottom of the fine pores. (4) An electrolytic neutralization step for neutralizing the inside of the fine pore. (5) A cationic electrodeposition coating process using a cathode deposition type acrylic resin coating.
JP11168221A 1999-06-15 1999-06-15 Surface treatment of aluminum and aluminum alloy Pending JP2000355795A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11168221A JP2000355795A (en) 1999-06-15 1999-06-15 Surface treatment of aluminum and aluminum alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11168221A JP2000355795A (en) 1999-06-15 1999-06-15 Surface treatment of aluminum and aluminum alloy

Publications (1)

Publication Number Publication Date
JP2000355795A true JP2000355795A (en) 2000-12-26

Family

ID=15864040

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2000355795A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005036315A (en) * 2003-06-19 2005-02-10 Toyo Roki Mfg Co Ltd Method of forming oxide film on aluminum or aluminum alloy
JP2009228064A (en) * 2008-03-24 2009-10-08 Furukawa-Sky Aluminum Corp Aluminum material and method of manufacturing the same
WO2010038943A2 (en) * 2008-09-30 2010-04-08 주식회사 케이씨씨 Resin composition for cation electrodeposition paint with excellent inner permeability, containing aromatic sulfonic acid and urethane functional rheology modifier
CN101205621B (en) * 2006-12-21 2010-10-06 北京北方微电子基地设备工艺研究中心有限责任公司 Method for cleaning aluminium parts
WO2015021771A1 (en) * 2013-08-15 2015-02-19 嘉兴兴禾汽车零部件有限公司 Hole sealing method with anodic oxidation for aluminium or aluminium alloy component for vehicle
CN114959828A (en) * 2022-06-16 2022-08-30 东莞市新东明科技有限公司 Aluminum alloy anode process

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005036315A (en) * 2003-06-19 2005-02-10 Toyo Roki Mfg Co Ltd Method of forming oxide film on aluminum or aluminum alloy
CN101205621B (en) * 2006-12-21 2010-10-06 北京北方微电子基地设备工艺研究中心有限责任公司 Method for cleaning aluminium parts
JP2009228064A (en) * 2008-03-24 2009-10-08 Furukawa-Sky Aluminum Corp Aluminum material and method of manufacturing the same
WO2010038943A2 (en) * 2008-09-30 2010-04-08 주식회사 케이씨씨 Resin composition for cation electrodeposition paint with excellent inner permeability, containing aromatic sulfonic acid and urethane functional rheology modifier
WO2010038943A3 (en) * 2008-09-30 2010-07-01 주식회사 케이씨씨 Resin composition for cation electrodeposition paint with excellent inner permeability, containing aromatic sulfonic acid and urethane functional rheology modifier
KR101005297B1 (en) 2008-09-30 2011-01-04 주식회사 케이씨씨 Resin composition for cathodic electrodeposition coating with good throw power comprising aromatic sulfonic acid and urethane-fuctional rheology control agent
WO2015021771A1 (en) * 2013-08-15 2015-02-19 嘉兴兴禾汽车零部件有限公司 Hole sealing method with anodic oxidation for aluminium or aluminium alloy component for vehicle
EP2873753A4 (en) * 2013-08-15 2016-09-07 Jiaxing Xinghe Automotive Parts Co Ltd Hole sealing method with anodic oxidation for aluminium or aluminium alloy component for vehicle
US20160273123A1 (en) * 2013-08-15 2016-09-22 Jiaxing Xinghe Automotive Parts Co., Ltd. An anodization sealing process for an aluminum or aluminum alloy element for vehicles
US9771663B2 (en) 2013-08-15 2017-09-26 Jiaxing Xinghe Automotive Parts Co., Ltd. Anodization sealing process for an aluminum or aluminum alloy element for vehicles
CN114959828A (en) * 2022-06-16 2022-08-30 东莞市新东明科技有限公司 Aluminum alloy anode process

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