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JPH0237437B2 - - Google Patents
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JPH0237437B2 - - Google Patents

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Publication number
JPH0237437B2
JPH0237437B2 JP57121424A JP12142482A JPH0237437B2 JP H0237437 B2 JPH0237437 B2 JP H0237437B2 JP 57121424 A JP57121424 A JP 57121424A JP 12142482 A JP12142482 A JP 12142482A JP H0237437 B2 JPH0237437 B2 JP H0237437B2
Authority
JP
Japan
Prior art keywords
coloring
electrolytic coloring
electrolysis
aluminum
electrolytic
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 - Lifetime
Application number
JP57121424A
Other languages
Japanese (ja)
Other versions
JPS5913095A (en
Inventor
Juji Hinota
Yoshiko Ooi
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.)
Fujisash Co Ltd
Original Assignee
Fujisash 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 Fujisash Co Ltd filed Critical Fujisash Co Ltd
Priority to JP12142482A priority Critical patent/JPS5913095A/en
Publication of JPS5913095A publication Critical patent/JPS5913095A/en
Publication of JPH0237437B2 publication Critical patent/JPH0237437B2/ja
Granted legal-status Critical Current

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  • 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又はアルミニウム合金の
電解着色法に関し、特に淡灰色の着色膜を安定し
て得ることができる電解着色法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an electrolytic coloring method for aluminum or an aluminum alloy, and particularly to an electrolytic coloring method that can stably obtain a pale gray colored film.

浅田法などとして知られるアルミニウム及びア
ルミニウム合金の電解着色法は、金属塩を含む電
解液中で電解することにより、陽極酸化皮膜の細
孔中に金属を析出させ、着色させるもので、析出
金属による光の吸収、更には光の干渉作用で色が
ついて見えるものであると考えられている。
The electrolytic coloring method for aluminum and aluminum alloys, known as the Asada method, involves electrolyzing in an electrolytic solution containing metal salts to precipitate metal into the pores of the anodic oxide film and coloring it. It is thought that the appearance of color is due to light absorption or even light interference.

従来、このようなアルミニウム及びアルミニウ
ム合金の電解着色法に用いる種々の電解着色液が
提案され、また交流をはじめとして種々の波形に
よる電解着色法も提案されているが、これらは短
時間で濃色化を計つたり、スローイング性を向上
させることを主な目的としており、淡色の着色膜
を安定して得るという点では十分なものではな
い。実際、現場生産において、淡色の電解着色膜
を得ようとしても十分な再現性がなく、淡色にお
ける着色の不安定性ということが電解着色法の大
きな問題点として指摘されていた。
In the past, various electrolytic coloring solutions have been proposed for use in such electrolytic coloring methods for aluminum and aluminum alloys, and electrolytic coloring methods using various waveforms, including alternating current, have been proposed, but these methods can produce deep colors in a short time. The main purpose of this method is to improve the throwing properties and to improve the throwing properties, but it is not sufficient in terms of stably obtaining a light colored film. In fact, in on-site production, even when attempting to obtain a light-colored electrolytically colored film, there is insufficient reproducibility, and the instability of coloring in light colors has been pointed out as a major problem with the electrolytic coloring method.

また従来、淡灰色の着色膜を確実に得る方法は
知られていなかつた。
Furthermore, until now, there has been no known method for reliably obtaining a light gray colored film.

本発明者らは、上記問題点を解決し、アルミニ
ウム又はアルミニウム合金の淡灰色の電解着色膜
を安定して得る方法につき鋭意研究を行なつた結
果、1サイクルにおいて10〜50msec(ミリ秒)の
負電流に対しその50〜500倍の正電流を印加した
波形によりニツケル塩を含む電解着色液を用いて
電解着色を行なうと、淡灰色の電解着色膜が安定
して再現性よく得られ、淡灰色の電解着色管理が
現場的にも極めて容易になつて、淡灰色という従
来殆んど見られない着色が可能になることを見い
出した。
The present inventors solved the above problems and conducted extensive research on a method for stably obtaining a pale gray electrolytically colored film of aluminum or aluminum alloy. When electrolytic coloring is performed using an electrolytic coloring solution containing nickel salt with a waveform in which a positive current that is 50 to 500 times that of a negative current is applied, a pale gray electrolytically colored film can be obtained stably and with good reproducibility. It has been discovered that gray electrolytic coloring management has become extremely easy on-site, and it has become possible to create pale gray, a color that has rarely been seen in the past.

即ち、本発明者らの検討の結果では、例えば硫
酸電解によつて得たアルミニウム又はアルミニウ
ム合金の陽極酸化皮膜に対して電解着色を行なう
場合、この硫酸電解によつて生成したバリアー層
は硫酸に溶解作用があるのでバリアー層の抵抗に
バラツキが発生するが、このバラツキのあるバリ
アー層を有する陽極酸化皮膜に通常の交流電解法
による電解着色を行なうと、正電流によるバリア
ー層の修復作用はあるが、負電流も大きいため修
復が間に合わず、このため第1図に示したように
バリアー層1のバラツキに応じ析出金属2の高さ
にもバラツキが発生する(なお、図中3はアルミ
ニウム素地、4は孔壁、5は細孔である。)。
That is, according to the results of the studies conducted by the present inventors, for example, when electrolytically coloring an anodic oxide film of aluminum or aluminum alloy obtained by sulfuric acid electrolysis, the barrier layer formed by this sulfuric acid electrolysis is Due to the dissolving action, variations in the resistance of the barrier layer occur, but when an anodic oxide film with a barrier layer with such variations is electrolytically colored using the normal AC electrolysis method, the barrier layer can be repaired by the positive current. However, since the negative current is also large, the repair cannot be completed in time, and as a result, as shown in Figure 1, variations in the height of the deposited metal 2 occur depending on the variations in the barrier layer 1. , 4 is the pore wall, and 5 is the pore).

従つて、通常の交流電解法による電解着色にお
いては、析出金属の高さにバラツキが生じるの
で、光の干渉効果が少なくなり、これが電解着色
の淡色化を実現する上で大きな問題となる。これ
に対し、1サイクルにおいて負電流10〜50msec、
正電流をその50〜500倍とした波形を用いて電解
着色を行なつた場合、正電流が大きいのでバリア
ー層の修復が十分なされ、このため第2図に示し
たようにバリアー層1に殆んどバラツキがなく、
抵抗がほぼ一定になり、析出金属2の高さも一定
になるので、光の干渉効果が高くなることを知見
した。従つて、析出金属の高さを干渉膜とする干
渉効果による電解着色膜の淡色化において、この
ように正電流を負電流よりも大きくとることによ
つて、析出金属の高さが一定となり、干渉効果が
高くなるため、確実に安定して淡色の電解着色膜
を得ることができると共に、この場合ニツケル塩
を含む電解着色液を用いると、従来の方法では黄
金色が得られるものであるが、光の干渉が高くな
つて従来得られていない淡灰色の着色膜が得られ
ることを見出し、本発明をなすに至つたものであ
る。
Therefore, in electrolytic coloring using a normal AC electrolytic method, variations occur in the height of the deposited metal, which reduces the interference effect of light, which poses a major problem in realizing lightening of electrolytic coloring. On the other hand, in one cycle, the negative current is 10 to 50 msec,
When electrolytic coloring is performed using a waveform in which the positive current is 50 to 500 times the positive current, the barrier layer is sufficiently repaired because the positive current is large. There is no variation,
It has been found that since the resistance becomes almost constant and the height of the deposited metal 2 also becomes constant, the light interference effect becomes high. Therefore, in lightening an electrolytically colored film due to the interference effect using the height of the deposited metal as an interference film, by making the positive current larger than the negative current in this way, the height of the deposited metal becomes constant, Since the interference effect is enhanced, it is possible to reliably and stably obtain a light-colored electrolytically colored film, and in this case, if an electrolytic coloring solution containing nickel salt is used, a golden color can be obtained using conventional methods. The inventors discovered that a light gray colored film, which had not been obtained in the past, could be obtained due to increased light interference, leading to the present invention.

以下本発明につき更に詳しく説明する。 The present invention will be explained in more detail below.

本発明のアルミニウム又はアルミニウム合金の
電解着色法は、硫酸、シユウ酸などの電解液を用
いて得られた陽極酸化皮膜を更にニツケル塩を添
加した電解着色液で電解して電解着色を行なうに
当り、被処理物を電解着色液中で1サイクルにお
いて10〜50msecの負電流に対しその50〜500倍の
正電流を印加した波形を用いて電解することを特
徴とするものである。
The electrolytic coloring method for aluminum or aluminum alloys of the present invention involves electrolytically coloring an anodic oxide film obtained using an electrolytic solution such as sulfuric acid or oxalic acid by further electrolyzing it with an electrolytic coloring solution containing nickel salt. , the object to be treated is electrolyzed in an electrolytic coloring solution using a waveform in which a negative current of 10 to 50 msec and a positive current of 50 to 500 times the negative current are applied in one cycle.

この場合、この電解着色に用いる陽極酸化皮膜
としては特に制限されず、例えばアルミニウムや
アルミニウム合金を硫酸、シユウ酸等の通常の電
解液を用いて電解することによつて得られた皮膜
を用いることができる。本発明によれば、硫酸電
解による皮膜にみられるようなバリアー層の抵抗
にバラツキのある陽極酸化皮膜を用いても、バリ
アー層を修復してその抵抗を一定化し、これによ
つて析出金属の高さを一定化することにより安定
した淡色の電解着色膜を得ることができるので、
バリアー層の抵抗にバラツキのある陽極酸化皮膜
をも問題なく使用し得るものである。
In this case, the anodic oxide film used for this electrolytic coloring is not particularly limited, and for example, a film obtained by electrolyzing aluminum or aluminum alloy using a normal electrolyte such as sulfuric acid or oxalic acid may be used. Can be done. According to the present invention, even if an anodic oxide film is used in which the resistance of the barrier layer varies, as is the case with films produced by sulfuric acid electrolysis, the barrier layer can be repaired to make its resistance constant, and thereby the deposited metal can be fixed. By keeping the height constant, a stable light-colored electrolytically colored film can be obtained.
An anodic oxide film with variable resistance of the barrier layer can also be used without any problem.

なお、本発明において、使用するアルミニウ
ム、アルミニウム合金の種類は特に制限されな
い。
In the present invention, the type of aluminum or aluminum alloy used is not particularly limited.

本発明の電解着色法において、その電解着色液
としては、ニツケル塩を含む従来公知の電解着色
液を用いることができる。
In the electrolytic coloring method of the present invention, a conventionally known electrolytic coloring liquid containing a nickel salt can be used as the electrolytic coloring liquid.

電解着色を行なう場合は、上述したように1サ
イクルにおいて負電流を10〜100msec、正電流を
負電流の50〜500倍とした波形を用いるものであ
り、これによつてより確実に安定した淡灰色電解
着色膜が得られる。なお、電源は上記の波形が得
られるものであればいずれのものでもよい。
When performing electrolytic coloring, as mentioned above, a waveform in which the negative current is 10 to 100 msec and the positive current is 50 to 500 times the negative current is used in one cycle, which ensures more stable and pale coloring. A gray electrolytically colored film is obtained. Note that any power source may be used as long as the above waveform can be obtained.

その他の電解条件は特に制限されないが、電圧
は通常20V以上、特に20〜100Vとし、また電解
時間は1〜10分、特に3〜7分とすることが好ま
しい。この場合、従来の交流電解による電解着色
法においては、高電圧で処理すると水素ガスの発
生が多くなり、また電解着色液中の不純物塩素イ
オンの影響により、皮膜破壊になり易いので、通
常10〜15V程度(波高値14〜21V程度)の電圧で
着色を行つており、高電圧は採用し難いものであ
るが、本発明によれば高電圧で電解しても支障が
なく、正電圧(バリアー層修復電位)、負電位
(金属負電位)共に高電圧がとれるものである。
また、従来の交流電解の場合、30秒程度の短時間
で着色処理しているが、この場合1秒の違いが金
属析出量に大きく影響する。これに対し、本発明
においては、電解時間を長くすることができ、負
電流に対し正電流が多いのでバリアー層を十分か
つ確実に修復し得るものであり、また電解管理も
容易になるものである。従つて、本発明によれ
ば、上述したように高電圧がとれ、着色時間も長
くなるので、安定したしかも管理のし易い電解条
件において、安定した着色処理を行なうことがで
きる。例えば、硫酸電解によつて生成するバリア
ー層は約15V×10Åのバリアー層であるが、この
バリアー層を修復するに当つて、従来の交流電解
の場合に比べて本発明では高電圧がとれるためよ
り厚く修復し得、修復時間も長いので、バラツキ
の多い硫酸電解のバリアー層の影響をより確実に
少なくし得、抵抗を一定として安定した析出電位
で金属析出を行ない、各孔への金属析出量をより
確実に均一化して着色の安定化を計ることができ
るものである。
Other electrolysis conditions are not particularly limited, but the voltage is usually 20V or higher, particularly 20 to 100V, and the electrolysis time is preferably 1 to 10 minutes, particularly 3 to 7 minutes. In this case, in the conventional electrolytic coloring method using AC electrolysis, treatment at high voltage generates a large amount of hydrogen gas, and the film is likely to be destroyed due to the influence of impurity chlorine ions in the electrolytic coloring solution. Coloring is performed with a voltage of about 15 V (peak value of about 14 to 21 V), and high voltage is difficult to use, but according to the present invention, there is no problem even if electrolysis is performed at high voltage, and positive voltage (barrier High voltage can be obtained for both layer repair potential) and negative potential (metal negative potential).
Furthermore, in the case of conventional AC electrolysis, coloring is done in a short time of about 30 seconds, but in this case, a difference of 1 second can greatly affect the amount of metal deposited. On the other hand, in the present invention, the electrolysis time can be extended, and since there is more positive current than negative current, the barrier layer can be repaired sufficiently and reliably, and the electrolysis management is also easier. be. Therefore, according to the present invention, as described above, a high voltage can be applied and the coloring time can be lengthened, so that stable coloring can be performed under stable and easily manageable electrolytic conditions. For example, the barrier layer produced by sulfuric acid electrolysis is about 15V x 10Å, but when repairing this barrier layer, the present invention can use a higher voltage than conventional AC electrolysis. Since it can be repaired thicker and the repair time is longer, it is possible to more reliably reduce the influence of the barrier layer of sulfuric acid electrolysis, which has many variations, and to perform metal deposition at a stable deposition potential with a constant resistance, metal deposition in each hole. This makes it possible to more reliably equalize the amount and stabilize the coloring.

なお、電解着色の温度も特に制限されないが、
通常室温で行なわれる。
Note that the temperature of electrolytic coloring is not particularly limited, but
Usually carried out at room temperature.

以上詳述したように、本発明によれば、1サイ
クルにおいて10〜50msecの負電流に対しその50
〜500倍の正電流を印加した波形でニツケル塩を
含む電解着色液を用いて電解着色することによ
り、陽極酸化皮膜の各細孔に対する析出金属の析
出高さを可及的に均一化し得、これにより光の干
渉効果を高めて淡灰色の安定した着色膜を確実に
再現性よく得ることができ、また正電流に対し負
電流が少なく、高電圧をとれると共に、着色時間
を長くすることもできるので、淡灰色の着色管理
が容易になり、淡灰色という従来殆んど見られな
い着色を可能にするものである。
As detailed above, according to the present invention, for a negative current of 10 to 50 msec in one cycle, the 50 msec
By electrolytically coloring using an electrolytic coloring solution containing nickel salt with a waveform in which a positive current of ~500 times is applied, the height of the precipitated metal in each pore of the anodic oxide film can be made as uniform as possible, This enhances the light interference effect, making it possible to reliably obtain a light gray colored film with good reproducibility.In addition, the negative current is small compared to the positive current, allowing high voltage to be obtained, and also making it possible to extend the coloring time. This makes it easier to manage light gray coloring, and enables light gray coloring, which is rarely seen in the past.

以下、実施例と比較例を示し、本発明を更に具
体的に説明するが、本発明は下記の実施例に限定
されるものではない。
EXAMPLES Hereinafter, the present invention will be explained in more detail by showing examples and comparative examples, but the present invention is not limited to the following examples.

実施例 アルミニウム材としてA−6063−T5材を使用
し、常法に従つて脱脂、エツチング、中和処理を
行なつた後、硫酸浴を用いて直流電解し、無色の
陽極酸化皮膜を形成した。
Example A-6063-T 5 material was used as the aluminum material, and after degreasing, etching, and neutralization according to conventional methods, it was subjected to direct current electrolysis using a sulfuric acid bath to form a colorless anodic oxide film. did.

次に、下記組成の電解着色液を用い、下記の条
件で電解着色を行なつた。
Next, electrolytic coloring was carried out under the following conditions using an electrolytic coloring solution having the following composition.

液組成 NiSO4・6H2O 25g/ (NH42SO4 15 〃 H3BO3 15 〃 PH 4.5 電解条件 1サイクル 負電流 30msec 正電流 3sec 電 圧 35V 温 度 30℃ 電解時間 7min 得られた電解着色膜は淡灰色であり、またこの
電解着色膜につき電子顕微鏡で観察した結果は、
第2図に示したように各細孔への析出金属の高さ
は互にほぼ同一なものあつた。
Liquid composition NiSO 4・6H 2 O 25g/ (NH 4 ) 2 SO 4 15 〃 H 3 BO 3 15 〃 PH 4.5 Electrolysis conditions 1 cycle Negative current 30msec Positive current 3sec Voltage 35V Temperature 30℃ Electrolysis time 7min Obtained The electrolytically colored film is light gray, and the results of observing this electrolytically colored film with an electron microscope are as follows.
As shown in FIG. 2, the height of the deposited metal in each pore was almost the same.

ここで10個の試料につきいずれも上記条件で電
解着色を行なつたが、いずれも互に同じ淡灰色を
有し、色合いのバラツキは生ぜず、再現性よく淡
色の電解着色膜を得ることができた。
Here, all 10 samples were electrolytically colored under the above conditions, and all of them had the same light gray color, with no variation in hue, and it was possible to obtain light-colored electrolytically colored films with good reproducibility. did it.

比較例 実施例と同様にして硫酸電解による陽極酸化皮
膜を形成した後、同一の電解着色液を用いて下記
条件で電解着色を行なつた。
Comparative Example After forming an anodized film by sulfuric acid electrolysis in the same manner as in the example, electrolytic coloring was performed using the same electrolytic coloring solution under the following conditions.

電解条件 交流電解 50Hz 電 圧 13V 温 度 30℃ 電解時間 30sec 得られた電解着色膜は黄金色であり、淡色は得
られなかつた。また、この電解着色膜につき電子
顕微鏡で観察した結果は、第1図に示したように
各細孔への析出金属の高さにバラツキのあるもの
であつた。
Electrolysis conditions AC electrolysis 50Hz Voltage 13V Temperature 30°C Electrolysis time 30sec The electrolytically colored film obtained was golden yellow and no light color was obtained. Further, as shown in FIG. 1, the electrolytically colored film was observed with an electron microscope, and the height of the deposited metal in each pore varied.

ここで、10個の試料につき電解着色を行なつた
結果は、黄味や黒色を帯びたり、濃淡に差がある
もので、その着色膜は色合いにバラツキがあるも
のであつた。
Here, the results of electrolytic coloring of 10 samples showed that the colored films had a yellowish or black tinge, and had different shading, and the colored films had variations in hue.

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

第1図は従来の交流電解による電解着色法を採
用した場合における陽極酸化皮膜細孔への金属析
出の状態を示す説明図、第2図は本発明法を採用
した場合における陽極酸化皮膜細孔への金属析出
の状態を示す説明図である。
Figure 1 is an explanatory diagram showing the state of metal deposition in the pores of the anodic oxide film when the conventional electrolytic coloring method using AC electrolysis is adopted, and Figure 2 is an explanatory diagram showing the state of metal precipitation in the pores of the anodic oxide film when the method of the present invention is adopted. It is an explanatory view showing the state of metal precipitation in

Claims (1)

【特許請求の範囲】[Claims] 1 アルミニウム又はアルミニウム合金を電解着
色するに際し、アルミニウム又はアルミニウム合
金を陽極酸化した後、ニツケル塩を含む電解着色
液中で1サイクルにおいて10〜50ミリ秒の負電流
に対しその50〜500倍の正電流を印加した波形に
より電解して、淡灰色の着色膜を得ることを特徴
とするアルミニウム又はアルミニウム合金の電解
着色法。
1. When electrolytically coloring aluminum or aluminum alloy, after anodizing the aluminum or aluminum alloy, in one cycle in an electrolytic coloring solution containing nickel salt, a positive current of 50 to 500 times the negative current of 10 to 50 milliseconds is applied. An electrolytic coloring method for aluminum or aluminum alloy, characterized in that a pale gray colored film is obtained by electrolysis using a waveform of applied current.
JP12142482A 1982-07-13 1982-07-13 Electrolytic pigmentation method of aluminum or aluminum alloy Granted JPS5913095A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12142482A JPS5913095A (en) 1982-07-13 1982-07-13 Electrolytic pigmentation method of aluminum or aluminum alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12142482A JPS5913095A (en) 1982-07-13 1982-07-13 Electrolytic pigmentation method of aluminum or aluminum alloy

Publications (2)

Publication Number Publication Date
JPS5913095A JPS5913095A (en) 1984-01-23
JPH0237437B2 true JPH0237437B2 (en) 1990-08-24

Family

ID=14810797

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12142482A Granted JPS5913095A (en) 1982-07-13 1982-07-13 Electrolytic pigmentation method of aluminum or aluminum alloy

Country Status (1)

Country Link
JP (1) JPS5913095A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63108551A (en) * 1986-10-27 1988-05-13 Nakamichi Corp Leader block pulling-out device

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5249408B2 (en) * 1972-11-21 1977-12-17
JPS5727953B2 (en) * 1974-02-07 1982-06-14
JPS5177547A (en) * 1974-12-28 1976-07-05 Riken Keikinzoku Kogyo Kk Aruminiumu moshikuhaaruminiumugokinzaino chakushokusankahimakuseiseiho

Also Published As

Publication number Publication date
JPS5913095A (en) 1984-01-23

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