JPH0421757B2 - - Google Patents
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- JPH0421757B2 JPH0421757B2 JP59064397A JP6439784A JPH0421757B2 JP H0421757 B2 JPH0421757 B2 JP H0421757B2 JP 59064397 A JP59064397 A JP 59064397A JP 6439784 A JP6439784 A JP 6439784A JP H0421757 B2 JPH0421757 B2 JP H0421757B2
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- voltage
- acid
- film
- current
- aluminum
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Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、アルミニウム又はアルミニウム合金
の陽極酸化皮膜を、グレー系の色調に種々の金属
塩に基づく色調が重ね合わされた色調に均一に着
色する方法に関するものである。Detailed Description of the Invention (Industrial Application Field) The present invention uniformly colors an anodic oxide film of aluminum or an aluminum alloy to a gray tone overlaid with tones based on various metal salts. It is about the method.
(従来の技術)
いわゆる電流回復現象による発色皮膜を得る方
法としては、特開昭52−117844号公報及び雑誌
「金属表面技術」29、No.7355−360(1978)等に記
載のものが知れている。この方法は、硫酸、リン
酸等の酸性浴あるいは水酸化ナトリウム、リン酸
ナトリウム等のアルカリ性浴中で陽極酸化処理
し、透明な皮膜を形成した後、第1図に示すよう
な方法で、陽極酸化処理電圧V1を一度、0〜
3Vに低下させ、その後再び先の電圧よりも低い
電圧V2を印加するものである。その時、第2図
に示すように陽極酸化処理時の電流I1は一度、
0近傍に低下した後、徐々に流れはじめる(I
2)。このように、電流が回復し始めると、あら
かじめ形成された透明な皮膜即ち第3−1図に模
式的に示す皮膜は第3−2図に模式的に示す皮膜
のようになる。第3−1図において、アルミニウ
ム製素地1の表面には多孔性のアルマイト層2が
あり、層2は表面側に開口する多数の孔3を有し
ており、孔3の底面と素地1との間にはバリヤー
層4がある。第3−2図の皮膜では、皮膜の孔3
の底部に新しいより孔径の小さい孔が多数生成
し、孔3はいわゆる枝分れ構造となつている。こ
のため第3−2図の皮膜では、光が乱反射及び吸
収されて発色する。即ち第3−2図の皮膜はグレ
ー系の色調を有する発色皮膜となる。(Prior art) As a method of obtaining a colored film by the so-called current recovery phenomenon, methods described in Japanese Patent Application Laid-Open No. 117844/1984 and the magazine "Metal Surface Technology" 29, No. 7355-360 (1978) are known. ing. In this method, a transparent film is formed by anodizing in an acidic bath such as sulfuric acid or phosphoric acid or an alkaline bath such as sodium hydroxide or sodium phosphate, and then anodization is performed using the method shown in Figure 1. Oxidation treatment voltage V1 is set once to 0~
The voltage is lowered to 3V, and then a voltage V2 lower than the previous voltage is applied again. At that time, as shown in FIG. 2, the current I1 during anodizing treatment is once
After decreasing to around 0, it gradually begins to flow (I
2). Thus, when the current begins to recover, the previously formed transparent coating, ie the coating schematically shown in FIG. 3-1, becomes the coating schematically shown in FIG. 3-2. In Figure 3-1, there is a porous alumite layer 2 on the surface of an aluminum base 1, and the layer 2 has a large number of holes 3 that open on the surface side, and the bottom of the holes 3 and the base 1 are connected to each other. There is a barrier layer 4 between them. In the film shown in Figure 3-2, the hole 3 in the film
Many new pores with smaller diameters are generated at the bottom of the pores 3, and the pores 3 have a so-called branched structure. Therefore, in the film shown in FIG. 3-2, light is diffusely reflected and absorbed, resulting in color development. That is, the film shown in FIG. 3-2 is a colored film having a gray tone.
(発明が解決しようとする問題点)
上記の方法により得られた発色皮膜には、色調
が不均一性であるという欠点があつた。これは以
下の理由による。即ち、電流回復現象を得るため
の電圧が低く、第4−1図及び第4−2図に示す
ような、電解枠5および電解棒6を用いて平板の
処理材7を処理すると、端部7aと中央部7bと
で印加される電圧の差が生じるために、電流回復
速度が異なり発色の程度も異なるからである。(Problems to be Solved by the Invention) The colored film obtained by the above method had a drawback of non-uniform color tone. This is due to the following reasons. That is, when the voltage for obtaining the current recovery phenomenon is low and the flat plate material 7 is processed using the electrolytic frame 5 and the electrolytic rod 6 as shown in FIGS. 4-1 and 4-2, the edges This is because there is a difference in the voltages applied between the central portion 7a and the central portion 7b, resulting in different current recovery speeds and different degrees of color development.
本発明は、アルミニウム又はアルミニウム合金
の陽極酸化皮膜を、グレー系の色調に種々の金属
塩に基づく色調が重ね合わされた色調に均一に着
色することができる電解着色方法を提供すること
を目的とする。 SUMMARY OF THE INVENTION An object of the present invention is to provide an electrolytic coloring method that can uniformly color an anodic oxide film of aluminum or an aluminum alloy to a gray tone with tones based on various metal salts superimposed. .
(問題点を解決するための手段)
本発明のアルミニウム及びアルミニウム合金の
電解着色方法は、アルミニウム又はアルミニウム
合金材に、電解浴中にて陽極酸化処理を施して陽
極酸化皮膜を形成し、この陽極酸化皮膜に、上記
電解浴中にて上記陽極酸化処理の電圧を一度下げ
た後に上昇させて上記陽極酸化処理の電圧より低
い電圧を印加する電流回復処理を施して、上記陽
極酸化皮膜をグレー系の色調の発色皮膜とし、こ
の発色皮膜に対し、Sn、Ni、Co、Fe、Cu、Se、
Ag、Au、V、Mnの硫酸塩、酢酸塩、酒石酸塩
又はスルフアミン酸塩を含む金属塩と、ホウ酸、
酒石酸、クエン酸、スルフアミン酸、スルホサリ
チル酸又はクレゾールスルホン酸を含む酸又はそ
れらのアンモニウム塩からなるバリヤー型皮膜形
成剤とを含む電解着色液中にて、極性を正とする
直流又はパルスの電圧を印加し、更に極正を負と
する直流又はパルスの電圧、又は交流の電圧を印
加して電解着色処理を施して、上記発色皮膜を、
上記グレー系の色調に上記金属塩に基づく色調が
重ね合わされた色調に均一に着色することを特徴
とするものである。(Means for Solving the Problems) The method for electrolytically coloring aluminum and aluminum alloys of the present invention involves performing anodization treatment on aluminum or aluminum alloy materials in an electrolytic bath to form an anodized film, and then The oxide film is subjected to a current recovery treatment in which the voltage of the anodizing treatment is lowered once in the electrolytic bath and then increased to apply a voltage lower than the voltage of the anodizing treatment to give the anodized film a gray color. This coloring film has a color tone of Sn, Ni, Co, Fe, Cu, Se,
metal salts including sulfates, acetates, tartrates or sulfamates of Ag, Au, V, Mn; boric acid;
A direct current or pulse voltage with positive polarity is applied to an electrolytic coloring solution containing a barrier type film forming agent consisting of an acid containing tartaric acid, citric acid, sulfamic acid, sulfosalicylic acid, or cresol sulfonic acid, or an ammonium salt thereof. Then, apply a direct current or pulse voltage, or an alternating current voltage with polar positive as negative, to perform an electrolytic coloring treatment to form the colored film.
It is characterized in that it is uniformly colored to a color tone in which a color tone based on the metal salt is superimposed on the gray color tone.
本発明の方法が最も特徴とすることは、電流回
復処理によつてグレー系の色調の発色皮膜を得る
こと、及び種々の金属塩とバリヤー型皮膜形成剤
とを含む電解着色液中にてまず極性を正とする直
流又はパルスの電圧を印加することである。 The most characteristic feature of the method of the present invention is that it obtains a colored film with a gray tone by current recovery treatment, and that it is first coated in an electrolytic coloring solution containing various metal salts and a barrier type film forming agent. Applying a direct current or pulse voltage with positive polarity.
金属塩は電解時に一方の電極のアルミニウム又
はアルミニウム合金の表面に生成した酸化皮膜中
の微細孔中に、金属、金属酸化物、金属の水和物
もしくはこれらの混合物を析出させて着色させる
ものであり、金属塩としては、例えばSn、Ni、
Co、Fe、Cu、Se、Ag、Au、V、Mn等の硫酸
塩、酢酸塩、酒石酸塩又はスルフアミン酸塩等が
挙げられる。 Metal salts are colored by precipitating metals, metal oxides, metal hydrates, or mixtures thereof into the micropores in the oxide film that forms on the surface of the aluminum or aluminum alloy of one electrode during electrolysis. Examples of metal salts include Sn, Ni,
Examples include sulfates, acetates, tartrates, and sulfamates of Co, Fe, Cu, Se, Ag, Au, V, Mn, and the like.
バリヤー型皮膜形成剤は、直流又はパルスの正
の電圧を印加した時に、バリヤー層厚さを変化さ
せる役割をするものであり、ホウ酸、酒石酸、ク
エン酸、スルフアミン酸、スルホサリチル酸又は
クレゾールスルホン酸を含む酸又はそれらのアン
モニウム塩が挙げられる。 Barrier-type film-forming agents have the role of changing the barrier layer thickness when a direct current or pulsed positive voltage is applied, and include boric acid, tartaric acid, citric acid, sulfamic acid, sulfosalicylic acid, or cresolsulfonic acid. or their ammonium salts.
電圧の印加は、上記電解着色液中にて、まず極
性を正とする直流又はパルスの電圧を印加し、続
いて極性を負とする直流又はパルスの電圧、又は
交流の電圧を印加して行なう。正の電圧印加にお
いて、電圧は好ましくは3V〜30V、電流密度は
好ましくは0.01A/dm2〜1.0A/dm2、通電時間
は好ましくは2秒〜60秒である。負の電圧印加に
おいて、電圧は好ましくは10V〜30V、電流密度
は好ましくは0.1A/dm2〜1.0A/dm2であり、
正の電圧及び通電時間を考慮しながら、負の電圧
又は交流電圧と通電時間とを様々に変えることに
より、種々の濃さの均一な着色皮膜が得られる。 The voltage is applied in the electrolytic coloring solution by first applying a direct current or pulse voltage with positive polarity, and then applying a direct current or pulse voltage with negative polarity, or an alternating current voltage. . When applying a positive voltage, the voltage is preferably 3V to 30V, the current density is preferably 0.01A/ dm2 to 1.0A/ dm2 , and the current application time is preferably 2 seconds to 60 seconds. In applying a negative voltage, the voltage is preferably 10V to 30V, the current density is preferably 0.1A/ dm2 to 1.0A/ dm2 ,
By varying the negative voltage or AC voltage and the current application time while taking into account the positive voltage and current application time, uniformly colored films with various densities can be obtained.
電解着色工程を終えた皮膜には好ましくは煮沸
水や蒸気等による封孔処理が施されるか、又は必
要に応じて塗装が施される。 After the electrolytic coloring process, the film is preferably subjected to a sealing treatment using boiled water, steam, etc., or painted as necessary.
(作用)
陽極酸化皮膜に電流回復処理を施すと、陽極酸
化皮膜はグレー系の発色皮膜となる。(Function) When the anodic oxide film is subjected to current recovery treatment, the anodic oxide film becomes a gray colored film.
正の電圧印加は、着色の均一化を行なわせるも
のであるが、これは次のような理由による。第5
図に模式的に示すように、電解着色浴8中にステ
ンレス等よりなる対極9に対向させて、アルミニ
ウムまたはアルミニウム合金よりなるワーク10
が配置されるとする。ワーク10は凹部11を有
している。ここでワーク10と対極9間にワーク
10を正とする電圧を印加すると、電解着色液中
に含まれるバリヤー型皮膜形成剤により、上記発
色皮膜のバリヤー層が改質される。このバリヤー
層厚さは、その形成剤の種類による印加電圧と厚
さとの相関関係(例えばホウ酸の場合は14オング
ストローム/V)において増減し、ワーク10の
うち対極9に最も近い端部12と、最も遠い凹部
11の底部13とを比較すると、電圧分布により
端部12の方が底部13よりも厚いバリヤー層が
形成される。 Application of a positive voltage makes the coloring uniform, and this is due to the following reasons. Fifth
As schematically shown in the figure, a workpiece 10 made of aluminum or an aluminum alloy is placed in an electrolytic coloring bath 8 facing a counter electrode 9 made of stainless steel or the like.
Suppose that The work 10 has a recess 11. When a voltage is applied between the workpiece 10 and the counter electrode 9 with the workpiece 10 being positive, the barrier layer of the colored film is modified by the barrier type film forming agent contained in the electrolytic coloring liquid. The thickness of this barrier layer increases or decreases depending on the correlation between the applied voltage and the thickness depending on the type of forming agent (for example, 14 angstroms/V in the case of boric acid). , and the bottom 13 of the furthest recess 11, the voltage distribution creates a thicker barrier layer at the end 12 than at the bottom 13.
このようにバリヤー層厚さが対極に近い部分ほ
ど厚く、遠い部分ほど薄くなることによつて、電
気抵抗の差が生じる。このため続いて行なうワー
ク10側を負とする電圧、又は交流電圧を印加す
る際に、流れる電流が制御され、対極に近い端部
12より対極に遠い底部13の方が電流が流れや
すくなり、その結果、金属の析出が均一になる。 In this way, the barrier layer thickness is thicker in the portion closer to the counter electrode and thinner in the portion farther away, resulting in a difference in electrical resistance. Therefore, when applying a negative voltage or an alternating current voltage to the workpiece 10 side, the current flowing is controlled, and the current flows more easily in the bottom part 13 far from the counter electrode than in the end part 12 near the counter electrode. As a result, metal deposition becomes uniform.
従つて、グレー系の発色皮膜に対して種々の析
出金属に基づく均一な着色が施されることとな
り、陽極酸化皮膜はグレー系の色調に種々の金属
塩に基づく色調が重ね合わされた色調に均一に着
色されることとなる。 Therefore, the gray-colored film is uniformly colored based on various precipitated metals, and the anodic oxide film has a uniform color tone in which tones based on various metal salts are superimposed on the gray color. It will be colored.
このことはワーク10が平板のような場合でも
同様であり、第4−1図の処理材7の端部7aと
中央部7bとでは、端部7aの方に電流が集中し
やすくなり、その結果、着色が均一となる。 This is the same even when the workpiece 10 is a flat plate, and between the end portion 7a and the center portion 7b of the processing material 7 in Fig. 4-1, the current tends to concentrate toward the end portion 7a, and As a result, the coloring becomes uniform.
(実施例)
次に本発明による実施例及び従来の方法による
比較例を示す。(Example) Next, an example according to the present invention and a comparative example according to a conventional method will be shown.
比較例:いわゆる電流回復現象による方法
A1100P−H24材の平板(2000mm×4000mmの大
きさ)を、第4−1図及び第4−2図に示すよう
に吊つた。通常の前処理を行なつた後、硫酸150
g/、22℃中で、陽極酸化処理を行なつた。そ
の時の電圧は、第1図に従つてV1=15V、電流
は、第2図に従つてI1=2000Aであつた。30分間
処理し、1度電圧を0とした後、第1図における
V2を5Vとして、10分間通電した。その時の電
流は、第2図のI2として300Aであつた。その
結果、第4−1図において、処理材7の端部7a
はグレー色であり、処理材の中央部7bはやや淡
いグレー色であつた。即ち処理材7には不近一な
発色皮膜が形成された。Comparative Example: Method using so-called current recovery phenomenon A flat plate (2000 mm x 4000 mm) of A1100P-H24 material was hung as shown in Figures 4-1 and 4-2. After normal pretreatment, sulfuric acid 150
g/, anodizing treatment was carried out at 22°C. The voltage at that time was V1=15V according to FIG. 1, and the current was I1=2000A according to FIG. After processing for 30 minutes and setting the voltage to 0 once, V2 in FIG. 1 was set to 5V and electricity was applied for 10 minutes. The current at that time was 300A as I2 in Figure 2. As a result, in FIG. 4-1, the end 7a of the treated material 7
was gray in color, and the center portion 7b of the treated material was a slightly lighter gray color. In other words, an unsuitable colored film was formed on the treated material 7.
実施例 1
比較例と同様の処理を行ない、不均一な発色皮
膜を得た後、水洗処理し、電解着色液として、硫
酸ニツケル100g/、ホウ酸40g/を用い、
第6図において、E1=20V、E2=16V、t1=4
秒、t2=2秒、t3=10秒、t4=60秒として、通電
した結果、第4−1図において、処理材の端部7
a、処理材の中央部7b共に、黄色味がかつたグ
レー色が得られた。Example 1 The same treatment as in Comparative Example was carried out to obtain a non-uniform colored film, which was then washed with water, using 100 g of nickel sulfate and 40 g of boric acid as the electrolytic coloring solution.
In Figure 6, E1=20V, E2=16V, t1=4
As a result of applying electricity for seconds, t2 = 2 seconds, t3 = 10 seconds, and t4 = 60 seconds, the end 7 of the treated material is shown in Figure 4-1.
A and the central portion 7b of the treated material both had a yellowish gray color.
なお第6図において、E1は正の極性の電圧、
E2は負の極性の電圧、t1,t3はそれぞれ電
圧E1,E2の昇圧時間、t2,t4はそれぞれ
電圧E1,E2の保持時間である。 In addition, in FIG. 6, E1 is a positive polarity voltage,
E2 is a voltage of negative polarity, t1 and t3 are boosting times of voltages E1 and E2, respectively, and t2 and t4 are holding times of voltages E1 and E2, respectively.
実施例 2
A6063S−T5の押出形材(第5図に示したよう
な凹部を有する)を、第7図のように吊つた。第
7図において、14は電解枠、14′は電解棒、
15は処理材、15aは処理材15の上部、15
bは中央部、15cは下部である。なお第8図は
第7図の側面図である。通常の前処理を行なつた
後、硫酸100g/、リン酸50g/、20℃中で
陽極酸化処理を行なつた後、電流回復処理を行な
つた。その時の条件は、第1図、第2図に従つ
て、V1=18V(通電時間30分)、V2=3V(通電時
間5分)、I1=3000A、I2=300Aであつた。この
結果、第7図の場所15a〜15cの色調は、1
5a=15cでグレー色、15bで淡いグレー色
であつた。さらに形材の凹部は、全体的に淡いグ
レー色であつた。Example 2 An extruded section of A6063S-T5 (having a concave portion as shown in FIG. 5) was hung as shown in FIG. 7. In Fig. 7, 14 is an electrolytic frame, 14' is an electrolytic rod,
15 is the treated material, 15a is the upper part of the treated material 15, 15
b is the center part, and 15c is the lower part. Note that FIG. 8 is a side view of FIG. 7. After carrying out the usual pretreatment, anodizing treatment was carried out at 20° C. with 100 g of sulfuric acid and 50 g of phosphoric acid, followed by current recovery treatment. The conditions at that time were V1 = 18V (current application time: 30 minutes), V2 = 3V (current application time: 5 minutes), I1 = 3000A, and I2 = 300A, as shown in Figs. 1 and 2. As a result, the color tone at locations 15a to 15c in FIG.
5a=15c had a gray color, and 15b had a light gray color. Furthermore, the concave portion of the profile was entirely light gray in color.
次に、実施例1と同様の電解着色液中で、第9
図において、直流の電圧E=15V、交流の電圧
(実効値)V=12Vとし、t1=10秒、t2=2秒、t3
=10秒、t4=30秒として、通電した結果、処理材
の色調は、15a〜15c及び形材の凹部とも
に、均一な赤味のあるグレー色が得られた。な
お、第9図において、t1は電圧Eの昇圧時間、
t2は電圧Eの保持時間、t3は電圧Vの昇圧時
間、t4は電圧Vの保持時間である。 Next, in the same electrolytic coloring solution as in Example 1, the ninth
In the figure, DC voltage E = 15V, AC voltage (effective value) V = 12V, t1 = 10 seconds, t2 = 2 seconds, t3
As a result of energizing with = 10 seconds and t4 = 30 seconds, the color tone of the treated material was a uniform reddish gray in both 15a to 15c and the concave portions of the profile. In addition, in FIG. 9, t1 is the boosting time of the voltage E,
t2 is the holding time of the voltage E, t3 is the boosting time of the voltage V, and t4 is the holding time of the voltage V.
実施例 3
A1200P−H24材の平板(3000mm×4000mmの大
きさ)を第4−1図のように吊つた。通常の前処
理を行なつた後、リン酸三ナトリウム50g/、
20℃中で陽極酸化処理を行なつた後、電流回復処
理を行なつた。その時の条件は、第1図、第2図
に従つて、V1=20V(通電時間30分)、V2=5V
(通電時間7分)、I1=4000A、I2=500Aであつ
た。この結果、処理材の色調は、7a:褐色がか
つたグレー色、7b:黄味のあるグレー色であつ
た。次に、電解着色液として、酢酸錫30g/、
ホウ酸30g/、トリエタノールアミン10g/
を用いて、第10図において、E1=14V、E2=
12V、t1=5秒、t2=5秒、t3=1秒、t4=5秒、
t5=1秒、n=60回として通電した。その結果、
処理材の色調は、7a,7bとも、均一なダーク
グレー色になつた。なお、第10図において、E
1は正の極性の電圧、E2は負の極性の電圧、t
1,t3は昇圧時間、t2,t4は電圧の保持時
間、t5は休止時間、nは反復回数である。Example 3 A flat plate (3000 mm x 4000 mm) made of A1200P-H24 material was hung as shown in Figure 4-1. After normal pretreatment, trisodium phosphate 50g/,
After anodizing at 20°C, a current recovery process was performed. The conditions at that time are V1 = 20V (energizing time 30 minutes), V2 = 5V according to Figures 1 and 2.
(Electrification time: 7 minutes), I1 = 4000A, I2 = 500A. As a result, the color tone of the treated material was 7a: brownish gray, 7b: yellowish gray. Next, as an electrolytic coloring solution, 30 g of tin acetate/
Boric acid 30g/, triethanolamine 10g/
In Fig. 10, E1=14V, E2=
12V, t1=5 seconds, t2=5 seconds, t3=1 second, t4=5 seconds,
Electricity was applied with t5=1 second and n=60 times. the result,
The color tone of the treated materials became uniform dark gray in both cases 7a and 7b. In addition, in Fig. 10, E
1 is a positive polarity voltage, E2 is a negative polarity voltage, t
1 and t3 are boosting times, t2 and t4 are voltage holding times, t5 is a rest time, and n is the number of repetitions.
(発明の効果)
以上のように本発明によれば、アルミニウム又
はアルミニウム合金の陽極酸化皮膜を、グレー系
の色調に種々の金属塩に基づく色調が重ね合わさ
れた色調に均一に着色することができる。しか
も、本発明による電解着色方法は工業的に採用す
ることが容易で均一な品質を有する製品を製造す
るのに適している。(Effects of the Invention) As described above, according to the present invention, it is possible to uniformly color an anodic oxide film of aluminum or an aluminum alloy to a tone in which tones based on various metal salts are superimposed on a gray tone. . Moreover, the electrolytic coloring method according to the present invention is easy to employ industrially and is suitable for producing products with uniform quality.
第1図は電流回復処理における電圧印加方法を
示すグラフ、第2図は電流回復処理における電流
の経時変化を示すグラフ、第3−1図は通常の陽
極酸化皮膜の模式図、第3−2図は電流回復処理
の陽極酸化皮膜の模式図、第4−1図は陽極酸化
処理工場における処理材の吊り方法の一例の概略
を示す正面図、第4−2図は第4−1図の側面
図、第5図は電解着色装置の模式図、第6図は電
解着色における電圧印加方法の一例を示すグラ
フ、第7図は陽極酸化処理工場における処理材の
吊り方法の別の例の概略を示す正面図、第8図は
第7図の側面図、第9図および第10図はそれぞ
れ電解着色における電圧印加方法の別の例を示す
グラフである。
Figure 1 is a graph showing the voltage application method in the current recovery process, Figure 2 is a graph showing the change in current over time in the current recovery process, Figure 3-1 is a schematic diagram of a normal anodic oxide film, and Figure 3-2 is a graph showing the voltage application method in the current recovery process. The figure is a schematic diagram of an anodized film during current recovery treatment, Figure 4-1 is a front view schematically showing an example of a method of suspending treated materials in an anodizing treatment factory, and Figure 4-2 is the same as that shown in Figure 4-1. A side view, FIG. 5 is a schematic diagram of an electrolytic coloring device, FIG. 6 is a graph showing an example of a voltage application method in electrolytic coloring, and FIG. 7 is a schematic diagram of another example of a method for suspending treated materials in an anodizing treatment factory. 8 is a side view of FIG. 7, and FIGS. 9 and 10 are graphs showing other examples of voltage application methods in electrolytic coloring.
Claims (1)
解浴中にて陽極酸化処理を施して陽極酸化皮膜を
形成し、この陽極酸化皮膜に、上記電解浴中にて
上記陽極酸化処理の電圧を一度下げた後に上昇さ
せて上記陽極酸化処理の電圧より低い電圧を印加
する電流回復処理を施して、上記陽極酸化皮膜を
グレー系の色調の発色皮膜とし、この発色皮膜に
対し、Sn、Ni、Co、Fe、Cu、Se、Ag、Au、
V、Mnの硫酸塩、酢酸塩、酒石酸塩又はスルフ
アミン酸塩を含む金属塩と、ホウ酸、酒石酸、ク
エン酸、スルフアミン酸、スルホサリチル酸又は
クレゾールスルホン酸を含む酸又はそれらのアン
モニウム塩からなるバリヤー型皮膜形成剤とを含
む電解着色液中にて、極性を正とする直流又はパ
ルスの電圧を印加し、更に極性を負とする直流又
はパルスの電圧、又は交流の電圧を印加して電解
着色処理を施して、上記発色皮膜を、上記グレー
系の色調に上記金属塩に基づく色調が重ね合わさ
れた色調に均一に着色することを特徴とするアル
ミニウム及びアルミニウム合金の電解着色方法。1 Aluminum or aluminum alloy material is anodized in an electrolytic bath to form an anodized film, and the voltage of the anodic oxidation is lowered once in the electrolytic bath and then increased. Then, a current recovery treatment is applied to apply a voltage lower than the voltage of the anodic oxidation treatment to make the anodic oxide film a gray colored film. ,Se,Ag,Au,
A barrier consisting of a metal salt containing V, Mn sulfate, acetate, tartrate or sulfamate, and an acid or ammonium salt thereof including boric acid, tartaric acid, citric acid, sulfamic acid, sulfosalicylic acid or cresol sulfonic acid. In an electrolytic coloring solution containing a mold film forming agent, apply a direct current or pulsed voltage with positive polarity, and then apply a direct current or pulsed voltage or alternating current voltage with negative polarity to electrolytically color the liquid. A method for electrolytic coloring of aluminum and aluminum alloys, characterized in that the colored film is uniformly colored in a color tone in which a color tone based on the metal salt is superimposed on the gray color tone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6439784A JPS60208497A (en) | 1984-03-30 | 1984-03-30 | Electrolytic coloring method of aluminum and aluminum alloy |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6439784A JPS60208497A (en) | 1984-03-30 | 1984-03-30 | Electrolytic coloring method of aluminum and aluminum alloy |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60208497A JPS60208497A (en) | 1985-10-21 |
JPH0421757B2 true JPH0421757B2 (en) | 1992-04-13 |
Family
ID=13257139
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6439784A Granted JPS60208497A (en) | 1984-03-30 | 1984-03-30 | Electrolytic coloring method of aluminum and aluminum alloy |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60208497A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0796720B2 (en) * | 1986-12-27 | 1995-10-18 | 昭和アルミニウム株式会社 | Method for electrolytically coloring aluminum materials |
JPS63166996A (en) * | 1986-12-27 | 1988-07-11 | Showa Alum Corp | Method for electrolytically coloring aluminum material |
JPS63166994A (en) * | 1986-12-27 | 1988-07-11 | Showa Alum Corp | Method for electrolytically coloring aluminum material |
JP2006233242A (en) * | 2005-02-22 | 2006-09-07 | Fujisash Co | Gray coloration method of aluminum alloy material and gray coloration aluminum alloy material |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6058315B2 (en) * | 1982-06-07 | 1985-12-19 | 株式会社日本アルミ | Multicolor electrolytic coloring method for aluminum and aluminum alloys |
-
1984
- 1984-03-30 JP JP6439784A patent/JPS60208497A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS60208497A (en) | 1985-10-21 |
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