JPS58147592A - Method for pigmenting aluminum or aluminum alloy - Google Patents

Method for pigmenting aluminum or aluminum alloy

Info

Publication number
JPS58147592A
JPS58147592A JP2980282A JP2980282A JPS58147592A JP S58147592 A JPS58147592 A JP S58147592A JP 2980282 A JP2980282 A JP 2980282A JP 2980282 A JP2980282 A JP 2980282A JP S58147592 A JPS58147592 A JP S58147592A
Authority
JP
Japan
Prior art keywords
aluminum
film
coloring
treatment
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.)
Pending
Application number
JP2980282A
Other languages
Japanese (ja)
Inventor
Kazuo Chiba
千葉 和郎
Koji Mitamura
三田村 康二
Isao Takeuchi
竹内 庸
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.)
MA Aluminum Corp
Original Assignee
Mitsubishi Aluminum 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 Mitsubishi Aluminum Co Ltd filed Critical Mitsubishi Aluminum Co Ltd
Priority to JP2980282A priority Critical patent/JPS58147592A/en
Publication of JPS58147592A publication Critical patent/JPS58147592A/en
Pending legal-status Critical Current

Links

Landscapes

  • Electrochemical Coating By Surface Reaction (AREA)

Abstract

PURPOSE:To obtain a durable desired deep color in a short time, by forming an anodic oxide film on an Al material, subjecting the film to AC electrolytic treatment in an aqueous sulfuric acid soln. at low voltage, and pigmenting the film. CONSTITUTION:An anodic oxide film is formed on Al or an Al alloy, and the film is subjected to AC electrolytic treatment in an aqueous sulfuric acid soln. at about 3-20V anodic oxidation voltage which is below the electrolytic voltage during the formation of the anodic oxide film. After finishing the pretreatment, the film is washed, colored with a dye or an inorg. pigment, washed, and subjected to treatment for sealing the pores. By this method, even in case of a thin film having >=about 10mum thickness, a desired deep color with a superior hue and superior luster free from irregular color is obtd.

Description

【発明の詳細な説明】 の着色方法に係り、アルミニウム又はアルミニウム合金
に陽極酸化皮膜を形成した後、この陽極酸化皮膜を硫酸
水溶液中で約3〜20Vの一次電解電圧以下の電解電圧
で交流電解処理し、その後に着色処理を行なうことによ
って、例えば黒染のような濃色系の着色が色むらなく行
なえ、色調に優れた極ノて好ましいものとなり、しかも
生産性よく低コストで汀なえるアルミニウム又はアルミ
ニウム合金の着色方法を提供することを目的とする。
DETAILED DESCRIPTION OF THE INVENTION According to the coloring method, an anodic oxide film is formed on aluminum or an aluminum alloy, and then the anodic oxide film is subjected to AC electrolysis in an aqueous sulfuric acid solution at an electrolytic voltage lower than the primary electrolytic voltage of about 3 to 20 V. By processing and then coloring, it is possible to perform deep coloring, such as black dyeing, evenly, making it an extremely desirable product with excellent color tone. Moreover, aluminum can be washed with high productivity and at low cost. Another object of the present invention is to provide a method for coloring an aluminum alloy.

従来、アルミニウム又はアルミニウム合金(以下単にア
ルミニウムという)の着色は、一般VC染色又は無機顔
料による着色工程において濃色を得るには、(1)処理
液の溶質濃度を高める、(2)処理液の液温を高める、
(3)処理時間を長くするといった手段が考えられるが
、これらの手段には様々な問題がある。すなわち、(1
)の手段は、建浴切期には濃色系が得られやすいけれど
も、膜厚のわずかな違いがそのまま着色濃度に影響し、
色違いとなってあられれ、良好な所望のものが得られに
くい。
Conventionally, to color aluminum or aluminum alloy (hereinafter simply referred to as aluminum), in order to obtain a deep color in the general VC dyeing or coloring process with inorganic pigments, the following steps were taken: (1) increasing the solute concentration of the processing solution; (2) increasing the solute concentration of the processing solution; increase the liquid temperature,
(3) Measures such as lengthening the processing time can be considered, but these measures have various problems. That is, (1
) means that it is easy to obtain a deep color at the end of the bath build-up period, but slight differences in film thickness directly affect the color density;
Different colors appear, making it difficult to obtain a good desired product.

さらには、処理液の温度分布や攪拌具合によって着色具
合が大きな影響を受け、色むらが極めて起きやすいもの
となる。又、処理液が不安定で沈殿物を作りやすく、寿
命の短かいものであるといった欠点もある0又、(2)
の手段は、着色速度が早いので、その制御が困難でるり
、色違い及び色ムラが生じやすく、又着色工程時に封孔
作用が生じ、不均一な着色となりやすい。又、(3)の
手段は、生産性が極めて低く、工業的実施には全く適し
ていない。
Furthermore, the degree of coloring is greatly affected by the temperature distribution and stirring condition of the processing liquid, making color unevenness extremely likely to occur. In addition, there are disadvantages such as the processing liquid is unstable, tends to form precipitates, and has a short lifespan.
Since the coloring speed is fast in the above method, it is difficult to control the coloring rate, and it is easy to cause smearing, color difference, and color unevenness.Also, a pore sealing effect occurs during the coloring process, which tends to result in non-uniform coloring. Furthermore, the method (3) has extremely low productivity and is not suitable for industrial implementation at all.

又、アルミニウムの着色性を同上させる手段として、上
述の手段とは異なり、着色の行なわれるアルミニウム表
面層の特性を改質したものとすることが提案さ扛ており
、例えば(4)アルミニウムを凄惨酸化処理する際の電
解液温を高目にする、(5)電流密度を低目にする、(
6)電解液濃度を高目にする、(7)り流遊源又は脈流
の多い直流電源を用いるとい−)た手段が考えられるの
でるるか、これらの1段でも良好な着色アルミニウムは
得られない。
In addition, as a means to improve the colorability of aluminum, it has been proposed that, unlike the above-mentioned means, the characteristics of the aluminum surface layer where coloring is performed are modified.For example, (4) Increasing the electrolyte temperature during oxidation treatment, (5) lowering the current density, (
6) Increasing the concentration of the electrolyte, (7) Using a floating source or a DC power source with a lot of pulsating current, etc.) are possible, but it is possible to obtain good colored aluminum even with just one of these methods. I can't do it.

すなわら、例えば(41、(6) 、 (7)の手段で
は、アルミニウムの表面皮膜が著しく軟質なものとなり
、又表面皮膜生成効率が悪いので生産性が低く、特に(
7)の手段では電解中に皮膜剥離の現象が生じ、耐食性
の悪い皮膜となり、さらには黄味を帯びたものとなる欠
点がある。又、(5)の手段では、陽極酸化処理時間を
長く必要とし、その為生産性は著しく悪く、工業的実施
には適していない。
For example, in the methods (41, (6), and (7)), the aluminum surface film becomes extremely soft, and the surface film formation efficiency is low, resulting in low productivity.
The method 7) has the drawback that a phenomenon of film peeling occurs during electrolysis, resulting in a film with poor corrosion resistance, and furthermore, a yellowish tinge. Furthermore, the method (5) requires a long anodizing treatment time, resulting in extremely poor productivity and is not suitable for industrial implementation.

又、上記のような単なる陽極酸化処理ではなく、例えば
、アルミニウムに陽極酸化皮膜を形成した後、このアル
ミニウムを0.5〜2vの電解電圧で電解処理すること
により着色し、次いで塗料を・塗布乾燥させるといった
方法(特開昭51−I z6i目1号)、あるいはアル
ミニウムに陽極酸化皮膜を形成した後、このアルミニウ
ムを金属塩水浴液中で交流電解して電解着色を行ない、
次いで有憬染柘で染色するといった方法(特開昭52−
28.136 弓)の如く、染料又は顔料による着色処
理のN+J処理として、電解処理を2段階に分けて行な
う手段が提案されている。本発明者も、染料等による着
色に際して、電解処理を2段階に分けて行なう方法につ
いて種々の研究を行なった結果、2段階目の電解処理に
よって着色具合が大きな影響を受けることを見い出し、
前記公報における処理条件でハ層色具合が良好なものと
ならなかった。
Moreover, instead of simple anodizing treatment as described above, for example, after forming an anodized film on aluminum, this aluminum is colored by electrolytic treatment at an electrolytic voltage of 0.5 to 2 V, and then paint is applied. A method such as drying (Japanese Unexamined Patent Application Publication No. 1983-I Z6i No. 1), or after forming an anodic oxide film on aluminum, electrolytically coloring the aluminum by electrolyzing it in alternating current in a metal salt water bath solution,
Next, a method of dyeing with Yukinzome Tsuge (Japanese Patent Application Laid-Open No. 1973-
28.136), a means of carrying out electrolytic treatment in two stages has been proposed as N+J treatment of coloring treatment with dyes or pigments. The inventor of the present invention has also conducted various studies on methods of performing electrolytic treatment in two stages when coloring with dyes, etc., and has found that the degree of coloring is greatly affected by the second stage of electrolytic treatment,
The color quality of the layer C was not good under the processing conditions described in the above publication.

本発明者は、アルミニウムに所望の色調の染色又は無機
顔料による着色が行なえるようにするには、アルミニウ
ムにどのような前処理を施してふ・けばよいかを詳細に
実験した結果、2段階[」の電解処理は、その処理液と
して硫酸水溶液を用い、しかもその電解電圧は1段階目
の電解電圧より低く、かつ約:3〜20■の電圧で交流
電解することによ−、て、染色めるいは無機顔料による
着色が良好なものとなることを見い出したのである。
As a result of detailed experiments on what kind of pretreatment should be applied to aluminum in order to dye aluminum with a desired color tone or color it with inorganic pigments, the inventors found that: In the electrolytic treatment in step ['', an aqueous sulfuric acid solution is used as the treatment liquid, and the electrolytic voltage is lower than the electrolytic voltage in the first stage, and AC electrolysis is carried out at a voltage of about 3 to 20 μm. It was discovered that coloring using inorganic pigments is good for dyeing.

すなわち、アルミニウムに予備処理、すなわち?lIえ
は脱脂、水洗、エツチング、水洗、中和、水洗等の常法
の予備処理を行なった後、この予備処理さ7’tたアル
ミニウムに常法の陽極酸化処理によ、て約3〜15μm
厚の陽極酸化皮膜を形成した後、次にこの陽極酸化皮膜
の形成されたアルミニウムを、濃度が約50〜300g
/11の硫酸水溶液中で、温度が約10〜4σG1周波
数が約10〜100Hz1電流密度が約05〜4Aハt
r(、電解電圧が前段階の電解電圧よりも小さく、かつ
約3〜20Vの電圧で約1〜10分間交流電解処理をす
るといった前処理を行なっておくことにより、この前処
理の行なわ扛たアルミニウムを水洗した後、染料又は無
機顔料によって着色処理を行ない、その後水洗、封孔処
理を行なうアルミニウムの着色方法によれば、着色の色
調等に極めて優れた所望の着色が極めて生産性良く行な
えるものである。
Ie, pre-treatment on aluminum, ie? After carrying out conventional pretreatment such as degreasing, water washing, etching, water washing, neutralization, and water washing, the pretreated aluminum is subjected to a conventional anodizing treatment for about 3 to 30 minutes. 15μm
After forming a thick anodic oxide film, the aluminum on which this anodic oxide film has been formed is then heated to a concentration of about 50 to 300 g.
/11 sulfuric acid aqueous solution, temperature is about 10 to 4σG, frequency is about 10 to 100Hz, current density is about 05 to 4A.
This pretreatment can be carried out by performing a pretreatment in which the electrolysis voltage is lower than the electrolysis voltage in the previous step, and AC electrolysis treatment is performed for about 1 to 10 minutes at a voltage of about 3 to 20 V. According to the aluminum coloring method in which the aluminum is washed with water, then colored with a dye or inorganic pigment, and then washed with water and sealed, the desired coloration with extremely excellent color tone can be achieved with high productivity. It is something.

同、上記の電解処理工程において、−次の電剪処理液と
して硫酸水溶液を用いれば、同一の屯W(処理槽におい
て電源の切替を行なうのみですみ、極めて能率的に行な
えるものとなる。
Similarly, in the above-mentioned electrolytic treatment step, if a sulfuric acid aqueous solution is used as the next electroshear treatment solution, it is only necessary to switch the power supply in the same treatment tank, and the process can be carried out extremely efficiently.

そして、上記の工程において、二次の%M処理時の電圧
が小さすぎると、すなわち3■以1・ではこの電解処理
による効果があまり認めら71ず、次工程における染料
又は無機顔料等による着色が“イ(ましいものとならず
、逆に約20V以上の犬さな電圧では一次の電解処理に
よって形成された陽極酸化皮膜が破壊されてしまい、又
−次の電解処理電圧より大きい場合にも陽極酸化皮膜が
破壊さJすることになり、特に望ましい電解電圧は、−
次の寛解電圧以下で、かつ約10〜20Vであり、父、
−次の電解処理時の電流密度が小さすぎると、すなわち
05A/di以下ではこの電解処理による効果があ1 
 ゛り認められず、次工程における染料又は無機顔料等
による着色が望昔しいものとならず、逆に約1A/dm
”尉のものとなると陽極酸化皮膜が破壊さftてしまい
、次工程における染料又は無機顔料等による着色が望ま
しいものとならず、特に望ましい電流密度は約1〜35
A/CWであり、又、この二次の交流電解の処理時間は
望ましくは約2分以上行なえば充分であり、父、電解液
は、硫酸濃度が50,9/l以下でに電圧、電流の制御
が困難で二次の電解処理が効果的なものとならず、逆に
硫酸濃度が3009/lを越えると電圧、電流の制御が
困難のみならず、皮膜の特性が劣下し、次工程の染料又
は無機顔料等による着色が望ましいものとならず、特に
窒ましい硫酸水溶液の濃度は約100〜200g/lで
あり、父、二次の交流電解の処理時の液温は特に約15
〜25°′Cの範囲内で行なうことが次工程の染料又は
無機顔料等による着色に好ましいものとなることが判っ
た。
In the above step, if the voltage during the secondary %M treatment is too low, that is, in 3. However, if the voltage is higher than about 20V, the anodic oxide film formed by the first electrolytic treatment will be destroyed, and if the voltage is higher than the next electrolytic treatment, The anodic oxide film will also be destroyed, so the particularly desirable electrolytic voltage is -
Below the next remission voltage and about 10-20V, the father,
- If the current density during the next electrolytic treatment is too small, that is, below 05 A/di, the effect of this electrolytic treatment will be 1
1A/dm is not observed, and the coloring with dyes or inorganic pigments in the next process is not as desired.
If the current density is about 1 to 35 cm, the anodic oxide film will be destroyed and coloring with dyes or inorganic pigments in the next process will not be desirable.
A/CW, and the processing time of this secondary AC electrolysis is preferably about 2 minutes or more. On the other hand, if the sulfuric acid concentration exceeds 3009/l, it is not only difficult to control the voltage and current, but also the properties of the film deteriorate, making the next electrolytic treatment difficult. The coloring caused by dyes or inorganic pigments in the process is not desirable, and the concentration of the nitrous sulfuric acid aqueous solution is about 100 to 200 g/l, and the liquid temperature during the secondary AC electrolysis is particularly low. 15
It has been found that carrying out the process within the range of ~25°C is preferable for coloring with dyes or inorganic pigments in the next step.

これは、染料あるいは無機顔料等によるアルミニウムの
陽極酸化皮膜の着色は、陽極酸化皮膜の物理的及び化学
的特性、例えば陽極酸化皮膜の表向活性、物理的又は化
学的吸引力、マイクロポアの構造等によって大きな影響
を受けるのであるが。
The coloring of the anodic oxide film of aluminum with dyes or inorganic pigments is based on the physical and chemical properties of the anodic oxide film, such as the surface activity of the anodic oxide film, physical or chemical attraction, and the structure of the micropores. However, it is greatly influenced by

これらの因子が二次電解の条件によって大きな影響を受
け、本発明のような条件のもとて陽極酸化皮膜を処理す
ると、この処理された陽極酸化皮膜と染料又は無機顔料
との相互作用性が好ましいものとなり、この結果染料又
は無機顔料による着色が優れたものになると思われる。
These factors are greatly influenced by the conditions of secondary electrolysis, and when an anodic oxide film is treated under the conditions of the present invention, the interaction between the treated anodic oxide film and dyes or inorganic pigments is reduced. This is preferred and appears to result in superior coloration with dyes or inorganic pigments.

同、アルミニウムを前記本発明の処理工程、すなわち陽
極酸化皮膜を前記二次の電解処理条件で交流電解したも
のの断面を走査電子顕微鏡によって撮影した写真を示す
The same shows a photograph taken with a scanning electron microscope of a cross section of aluminum subjected to the treatment process of the present invention, that is, the anodic oxide film was subjected to AC electrolysis under the secondary electrolytic treatment conditions described above.

以下、本発明に係るアルミニウム又はアルミ−ニウム会
合の着色方法の具体的実施例について説明する。
Hereinafter, specific examples of the method for coloring aluminum or aluminum associations according to the present invention will be described.

実施例1 アルミニウム板(A 1050P−H24)を、まず7
6′法によって脱脂、エツチング、中和等の処理l二稈
によって予備処理する。
Example 1 An aluminum plate (A 1050P-H24) was first
Pretreatment is carried out by two culms, including degreasing, etching, and neutralization according to the 6' method.

次に、この予備処理されたアルミニウム板を、濃度が約
150.!?/lの硫酸水溶液を用いて、浴温約20”
G 、電流密度的1.3A/:覆、電圧約18Vの条件
で、陰極を鉛板として約25分間の陽極酸化処理を行な
い、アルミニウム板表面に約10μm厚の陽極酸化皮膜
を形成する。
Next, this pretreated aluminum plate was heated to a concentration of about 150. ! ? /l of sulfuric acid aqueous solution, the bath temperature is about 20"
Anodic oxidation treatment is carried out for about 25 minutes using a lead plate as a cathode under conditions of a current density of 1.3 A/2 and a voltage of about 18 V to form an anodic oxide film with a thickness of about 10 μm on the surface of the aluminum plate.

引き続いて、同浴液中で、電解電圧が約18V以トー、
電流密度が約4h7ch、z以下、浴温か約20°Cの
条件下で約3分間交流電解処理を行”なう。
Subsequently, in the same bath solution, the electrolytic voltage is about 18 V or higher,
AC electrolytic treatment was carried out for about 3 minutes under conditions of a current density of about 4h7ch, z or less, and a bath temperature of about 20°C.

上記のようにして処理されたアルミニウム板を水洗した
後、例えば60°Cの黒染液(実計製薬製の1“ACC
12濃度10Vl)中に約10分間浸漬処理して染色し
、次いで脱イオン沸騰水中で約20分間封孔処理をする
After washing the aluminum plate treated as described above with water, use a black dyeing solution (1" ACC manufactured by Jitsukei Pharmaceutical Co., Ltd.
12 (concentration 10 Vl) for about 10 minutes, and then sealed in deionized boiling water for about 20 minutes.

実施例2 実施例1の交流電解処理の工程まで同様にしてアルミニ
ウム板を前処理し、この交流電解処理の行なわれたアル
ミニウム板を水洗した後、6σCの/ユウ酸第二鉄アン
モニウム溶液(濃度約10 Vl)甲に約5分間浸漬処
理して金色に着色し、その後脱イオン沸騰水中で約20
分間封孔処理をする。
Example 2 An aluminum plate was pretreated in the same manner as in Example 1 up to the step of AC electrolytic treatment, and after washing the aluminum plate subjected to AC electrolytic treatment with water, a 6σC/ferric ammonium oxalate solution (concentration Approximately 10 Vl) The instep is immersed for approximately 5 minutes to give it a golden color, and then soaked in deionized boiling water for approximately 20 Vl.
Seal the hole for a minute.

比鴫ヒと沙り 太施例1と同様なアルミニウム板を、実施例1と同様な
予備処理をした後、実施例1と同様な条件で約55分間
の陽極酸化処理を行なって約2(1,om Ijjの陽
極酸化皮膜を形成した後、前記実施例における交流電解
処理を行なわず、前記実施例と同様な黒染液あるいはシ
ュウ酸第二鉄アンモニウム浴液を用いて着色し、その後
脱イオン沸騰水中でホ′J20分間封孔処理する。
An aluminum plate similar to that of Example 1 was pretreated in the same manner as in Example 1, and then anodized for approximately 55 minutes under the same conditions as in Example 1. After forming the anodic oxide film of 1, om Ijj, the AC electrolytic treatment in the previous example was not carried out, but it was colored using the same black dyeing solution or ferric ammonium oxalate bath solution as in the previous example, and then desorbed. The hole was sealed in ionized boiling water for 20 minutes.

上記実施例及び比較例で得られた着色アルミ−ラム板の
着色具合を観察すると、上記実施例に係るものは比較例
のものよりも着色濃度が一定したものでアシ、着色ムラ
のない、極めて美麗なものであり、その色調にも優れた
ものであり、著しく好ましいものであった。又、上記実
施例に係るものは比較例に係るものに比べて光沢度にも
優iシたものであり、例えば光輝性の要求される用途に
Lし、じてバフ、化学研磨等の前処理によって得た尤θ
くを減少させることのないものでもあった。
Observing the degree of coloring of the colored aluminum-lamb plates obtained in the above Examples and Comparative Examples, it was found that those according to the above Examples had a more constant coloring density than those of the Comparative Examples, and had no reeds or uneven coloring. It was beautiful, had an excellent color tone, and was extremely desirable. In addition, the products according to the above examples are superior in gloss compared to those according to comparative examples, and can be used, for example, in applications requiring brightness, and can be used before buffing, chemical polishing, etc. Likelihood θ obtained by processing
It was also something that did not reduce the number of people.

又、上記実施例のようにして行なわれる青色に要する時
間は、比較例のようにして行なわれる着色に要する時間
の半分ですみ、生産性に著しく富んだものともなる。
Further, the time required for the blue coloring performed as in the above embodiment is half of the time required for coloring as performed in the comparative example, resulting in significantly higher productivity.

さらに、アルミニウム板の着色の耐久性について6JI
I ボすると、例えばテーバ摩耗減量、耐アルカリ性、
キャス試験、促進耐候性等の特性においても、本発明に
係るものは着色皮膜層が薄いにもかかわりずデく遜色な
く、例えばテーバ摩耗減量等の特性は約3倍程度も優れ
ており、極めて耐久性に冨んだものでもある。
Furthermore, regarding the durability of the coloring of aluminum plates, 6JI
I For example, Taber abrasion loss, alkali resistance,
In terms of properties such as the CAST test and accelerated weather resistance, the products according to the present invention are comparable despite having a thin colored film layer, and for example, properties such as Taber abrasion loss are about three times better, which is extremely It is also highly durable.

ヒ述の如く、本発明に係るアルミニウム又はアルミニウ
ム合金の着色方法は、アルミニウム又はアルミニウム合
金に陽極酸化皮膜を形成した後、硫酸水浴液中において
前記陽極酸化皮膜形成時の電解電圧より小さくかつ約3
〜20Vの陽極酸化電圧で交流電解処理を行ない、その
後着色処理を施すものであるので、陽極酸化皮膜の膜厚
が薄くても、例えば従来のように約20μm厚といった
ような厚膜でなく、約10μm厚以下の薄膜でも、所望
の濃色系で、色調及び光沢にすぐれ、かつ着色ムラのな
い着色が行なえるようになり、しかもこのようにして得
られた着色の耐久性は極めて良好であり、さらには薄膜
でも所望の濃色系の着′色が汀なえるので着色処理に要
する時間は極めて短がいものとなり、生産性良く低コス
トで行なえる等の特長を有する。
As mentioned above, the method for coloring aluminum or aluminum alloy according to the present invention is to form an anodic oxide film on aluminum or aluminum alloy, and then use the electrolytic voltage lower than that at the time of forming the anodic oxide film in a sulfuric acid water bath solution to
Since alternating current electrolysis treatment is performed at an anodizing voltage of ~20V and then coloring treatment is applied, even if the thickness of the anodic oxide film is thin, it is not as thick as the conventional method, for example, about 20 μm thick. Even with a thin film of approximately 10 μm or less in thickness, it is now possible to color the desired deep color, with excellent tone and gloss, and with no uneven coloring, and the durability of the coloring obtained in this way is extremely good. Furthermore, since the desired deep coloration can be achieved even with a thin film, the time required for the coloring treatment is extremely short, and it has the advantage of being highly productive and low cost.

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

図面は、本発明に係るアルミニウム又はアルミニウム合
金の着色方法において実施される交流電解処理を行なっ
たアルミニウムの組織の几f?電子顕微鏡写真である。 特許出願人  三菱アルミニウム株式会+1代理人 宇
 高 克 己 ☆−2
The drawing shows the structure of aluminum that has been subjected to AC electrolytic treatment carried out in the method for coloring aluminum or aluminum alloy according to the present invention. This is an electron micrograph. Patent applicant: Mitsubishi Aluminum Co., Ltd. +1 Agent: Katsumi Utaka☆-2

Claims (1)

【特許請求の範囲】[Claims] アルミニウム又はアルミニウム合金に陽極、酸化皮gを
形成した後、硫酸水溶液中において前記陽極酸化皮膜形
成時の電解電圧より小さくかつ約3〜20Vの陽極酸化
電圧で又流電屑処理を行ない、その後着色処理を施す乙
とを特徴とするアルミニウム又はアルミニウム合金の着
色方法。
After forming an anode and an oxide film g on aluminum or an aluminum alloy, galvanic debris treatment is performed again in an aqueous sulfuric acid solution at an anodizing voltage of about 3 to 20 V, which is lower than the electrolytic voltage at the time of forming the anodic oxide film, and then colored. A method for coloring aluminum or aluminum alloy, characterized by applying a treatment.
JP2980282A 1982-02-27 1982-02-27 Method for pigmenting aluminum or aluminum alloy Pending JPS58147592A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2980282A JPS58147592A (en) 1982-02-27 1982-02-27 Method for pigmenting aluminum or aluminum alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2980282A JPS58147592A (en) 1982-02-27 1982-02-27 Method for pigmenting aluminum or aluminum alloy

Publications (1)

Publication Number Publication Date
JPS58147592A true JPS58147592A (en) 1983-09-02

Family

ID=12286140

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2980282A Pending JPS58147592A (en) 1982-02-27 1982-02-27 Method for pigmenting aluminum or aluminum alloy

Country Status (1)

Country Link
JP (1) JPS58147592A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59173294A (en) * 1983-03-23 1984-10-01 Pilot Pen Co Ltd:The Electrolytic coloration of aluminum or its alloy
JPS60110895A (en) * 1983-11-21 1985-06-17 Nippon Alum Mfg Co Ltd:The Electrolytic coloring method of aluminum and aluminum alloy
JPH0593296A (en) * 1991-09-30 1993-04-16 Yoshida Kogyo Kk <Ykk> Colored aluminum or aluminum alloy and its coloring method
US7347592B2 (en) 2005-07-14 2008-03-25 Hewlett-Packard Development Company, L.P. Light source for a projection system having a light absorption layer
JP2015017327A (en) * 2013-07-08 2015-01-29 深▲セン▼富泰宏精密工業有限公司 Method of surface-treating aluminum and aluminum alloy and aluminum product

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5348945A (en) * 1976-10-15 1978-05-02 Kobe Steel Ltd Dyeing process for anodized coating of aluminum or aluminum alloy
JPS5635795A (en) * 1979-08-30 1981-04-08 Tateyama Alum Kogyo Kk Coloring method for aluminum or aluminum alloy

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5348945A (en) * 1976-10-15 1978-05-02 Kobe Steel Ltd Dyeing process for anodized coating of aluminum or aluminum alloy
JPS5635795A (en) * 1979-08-30 1981-04-08 Tateyama Alum Kogyo Kk Coloring method for aluminum or aluminum alloy

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59173294A (en) * 1983-03-23 1984-10-01 Pilot Pen Co Ltd:The Electrolytic coloration of aluminum or its alloy
JPS6327440B2 (en) * 1983-03-23 1988-06-02 Pilot Pen Co Ltd
JPS60110895A (en) * 1983-11-21 1985-06-17 Nippon Alum Mfg Co Ltd:The Electrolytic coloring method of aluminum and aluminum alloy
JPS633038B2 (en) * 1983-11-21 1988-01-21 Nippon Aluminium Mfg
JPH0593296A (en) * 1991-09-30 1993-04-16 Yoshida Kogyo Kk <Ykk> Colored aluminum or aluminum alloy and its coloring method
US7347592B2 (en) 2005-07-14 2008-03-25 Hewlett-Packard Development Company, L.P. Light source for a projection system having a light absorption layer
JP2015017327A (en) * 2013-07-08 2015-01-29 深▲セン▼富泰宏精密工業有限公司 Method of surface-treating aluminum and aluminum alloy and aluminum product

Similar Documents

Publication Publication Date Title
CN102424999B (en) A kind of aluminium alloy anode oxide film electrolytic the treatment process of black
US3669856A (en) Process for the production of colored protective coatings on articles of aluminum or aluminum alloys
KR100695530B1 (en) Multicolor formation method of aluminum surface
JPH05125589A (en) Improved electrolytic method for coloring anodized aluminum
US3989605A (en) Method for continuous electrolytic coloring of aluminum articles
JPS58147592A (en) Method for pigmenting aluminum or aluminum alloy
JPS6210299A (en) Formation of colored coated film for titanium or titanium alloy
US4180443A (en) Method for coloring aluminum
JPS63312998A (en) Electrolytic coloration of anodic oxidized aluminum
US4632735A (en) Process for the electrolytic coloring of aluminum or aluminum alloys
US4179342A (en) Coating system method for coloring aluminum
EP0015279B1 (en) Coating system
JP2004018901A (en) Surface treatment method for magnesium material product
JP2953474B2 (en) Electrolytic treatment of aluminum and aluminum alloy
JPH10265996A (en) Anodic oxidation treatment of aluminum or its alloy with good alkaline corrosion resistance
JP2007239057A (en) Partly colored magnesium body, method of manufacturing the same and intermediate body
JP2001329397A (en) Coloration method for aluminum and aluminum alloy
TWI623651B (en) Dyeing method for micro-arc processing of metal workpiece
KR950000313B1 (en) Method for impartation of blue color to aluminum or aluminum alloy
JPS6210297A (en) Formation of coated film of titanium or titanium alloy
CN1118022A (en) Method for production of stainless steel with colour mirrorlike surface
JPH0841684A (en) Electrolytic pigmentation of anodic oxidation coating film of speeding-up of electrolytic pigmentation treatment
US3634214A (en) Electrolytic bath to be used for electrolytically anodizing aluminum or aluminum alloy to form a colored oxide coating and method for anodizing said metal
JPS58161796A (en) Method for coloring anodic oxide film of aluminum or aluminum alloy
JPS6360119B2 (en)