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JPS5943559B2 - Electrolytic coloring method for aluminum or its alloy materials - Google Patents
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JPS5943559B2 - Electrolytic coloring method for aluminum or its alloy materials - Google Patents

Electrolytic coloring method for aluminum or its alloy materials

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Publication number
JPS5943559B2
JPS5943559B2 JP10357577A JP10357577A JPS5943559B2 JP S5943559 B2 JPS5943559 B2 JP S5943559B2 JP 10357577 A JP10357577 A JP 10357577A JP 10357577 A JP10357577 A JP 10357577A JP S5943559 B2 JPS5943559 B2 JP S5943559B2
Authority
JP
Japan
Prior art keywords
aluminum
electrolysis
coloring
electrolytic
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.)
Expired
Application number
JP10357577A
Other languages
Japanese (ja)
Other versions
JPS5437041A (en
Inventor
敏彦 佐藤
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.)
Nippon Light Metal Co Ltd
Original Assignee
Nippon Light Metal 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 Nippon Light Metal Co Ltd filed Critical Nippon Light Metal Co Ltd
Priority to JP10357577A priority Critical patent/JPS5943559B2/en
Publication of JPS5437041A publication Critical patent/JPS5437041A/en
Publication of JPS5943559B2 publication Critical patent/JPS5943559B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明はアルミニウム若しくはその合金材(以下、単に
アルミニウム材とする。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to aluminum or its alloy material (hereinafter simply referred to as aluminum material).

)の電解着色法に係り、詳しくは、陽極酸化処理後のア
ルミニウム材を金属塩を含む電解浴中で電解着色処理す
る際に、その着色電解中の陽極酸化皮膜明度とその容量
インピーダンスとが一定の関係にあることを利用するた
めに、予め、所定のアルミニウム材につきその一定の関
係を求めておき、その上で、アルミニウム材につき電解
中の容量インピーダンスを連続的に測定し、これを目安
として電解着色処理して常に一定の明度の陽極酸化皮膜
が得られる電解着色法に係る。従来から、アルミニウム
材の電解着色法として種々のものが提案実施されている
が、アルミニウム材をあらかじめ陽極酸化処理してから
、金属塩を含む電解浴中で直流電解、または交流電解し
て、陽極酸化皮膜の多孔層中に金属を析出させて、その
析出金属特有の色に陽極酸化皮膜を着色することが一般
に行なわれている。
) Regarding the electrolytic coloring method, in detail, when an aluminum material after anodizing treatment is electrolytically colored in an electrolytic bath containing a metal salt, the brightness of the anodic oxide film and its capacitive impedance during the coloring electrolysis are constant. In order to take advantage of this relationship, first find a certain relationship for a given aluminum material, then continuously measure the capacitive impedance of the aluminum material during electrolysis, and use this as a guide. It relates to an electrolytic coloring method that allows an anodized film of constant brightness to be obtained through electrolytic coloring. Various methods of electrolytic coloring of aluminum materials have been proposed and implemented in the past, but aluminum materials are anodized in advance and then subjected to direct current electrolysis or alternating current electrolysis in an electrolytic bath containing metal salts. It is a common practice to precipitate a metal in a porous layer of an oxide film, and then color the anodic oxide film in a color unique to the precipitated metal.

この電解着色法は一般に金属塩電解着色法と言われ、陽
極酸化皮膜の着色程度も比較的安定しており、このため
該着色法は広く実用化されているアルミニウム材の電解
着色法である。また、この方法は、電解浴中の金属を陽
極酸化皮膜中に析出させ、その金属によつて着色される
ため、その金属析出量は色の濃度に比例し、同一濃度の
陽極酸化皮膜を生成するには、析出金属量を制御する必
要がある。しかしながら、現在までのところでは、金属
塩電解着色法において析出金属量を一定に制御すること
は困難であつて、アルミニウム材の電解着色によつては
同一濃度にアルミニウム材を表面処理することは不可能
であり、表面処理後に、どうしても、肉眼で「色合わせ
」作業を必要としている。例えば、Aのアルミニウム材
を電解着色してAの程度に着色して表面処理してから、
これと同じ濃度にアルミニウム材を着色する場合は、ア
ルミニウム材を一旦着色し、電解槽から引上げる。その
後、このアルミニウム材をA程度に着色されたアルミニ
ウム材またはA程度の色見本に対比し、例えば淡色であ
ればアルミニウム材を再度電解槽中に浸漬して電解着色
し、再びアルミニウム材を引きあげて色合わせを行なう
ことが必要である。これに反し、アルミニウム材の着色
程度が色見本より濃色の場合は、アルミニウム材の表面
処理を再度、最初の工程からやりなおす必要がある。ま
た、色合せ作業はこのようにきわめてはん雑であるが、
元来色合せ自体が色感に頼るために誤差を生じ易いもの
で、このところから不良率が高く、コストアツプにもつ
らなり、この点も大きな問題になつている。本発明は上
記欠点の解決を目的とし、特に、陽極酸化処理後のアル
ミニウム材を金属塩を含む電解浴中で電解着色する際に
、電解中の陽極酸化皮膜の容量インピーダンスを制御し
て同一濃度の陽極酸化皮膜を生成する方法を提案するこ
とを目的とする。以下、本発明法について順次に説明す
る。
This electrolytic coloring method is generally referred to as a metal salt electrolytic coloring method, and the degree of coloring of the anodic oxide film is relatively stable, so this coloring method is a widely used electrolytic coloring method for aluminum materials. In addition, in this method, the metal in the electrolytic bath is precipitated into the anodic oxide film, which is colored by the metal, so the amount of metal deposited is proportional to the color concentration, producing an anodic oxide film with the same concentration. To achieve this, it is necessary to control the amount of precipitated metal. However, up to now, it has been difficult to control the amount of precipitated metal to a constant level in the metal salt electrolytic coloring method, and it is impossible to surface-treat aluminum materials to the same concentration depending on the electrolytic coloring of the aluminum material. However, after surface treatment, it is necessary to perform "color matching" with the naked eye. For example, after electrolytically coloring the aluminum material A to the degree A and surface treating it,
When coloring an aluminum material to the same concentration as this, the aluminum material is once colored and then pulled out from the electrolytic cell. Then, compare this aluminum material with an aluminum material colored to A grade or a color sample of A grade. For example, if the color is light, the aluminum material is immersed in the electrolytic bath again, electrolytically colored, and the aluminum material is pulled out again. It is necessary to perform color matching. On the other hand, if the degree of coloring of the aluminum material is darker than the color sample, it is necessary to perform the surface treatment of the aluminum material again from the first step. Also, although the color matching process is extremely complicated,
Since the color matching itself relies on the color sense, errors are likely to occur, which leads to high defective rates and increased costs, which is also a major problem. The present invention aims to solve the above-mentioned drawbacks, and in particular, when anodized aluminum material is electrolytically colored in an electrolytic bath containing a metal salt, the capacitance impedance of the anodic oxide film during electrolysis is controlled to maintain the same concentration. The purpose of this study is to propose a method for producing an anodic oxide film. The method of the present invention will be sequentially explained below.

まず、アルミニウム材を常法の通りに、例えば脱脂、水
洗、エツチング等の前処理をし、その後、アルミニウム
材を例えば直流電解等で陽極酸化皮膜を生成する。
First, the aluminum material is subjected to pretreatment such as degreasing, water washing, etching, etc. in a conventional manner, and then an anodized film is formed on the aluminum material by, for example, direct current electrolysis.

この前処理ならびに陽極酸化処理は常法の通りにその目
的が達成できればいずれの方法でも良く、当然電解条件
等も常法の通りに行なえば十分である。次に、上記の通
りアルミニウム材を陽極酸化処理後、金属塩を含む電解
浴中に浸漬し、そこにおいて電解して、その表面の陽極
酸化皮膜を着色するが、予め、試験的にアルミニウム材
を電解着色し、この際の陽極酸化皮膜の容量インピーダ
ンスと明度の間に存在する第2図に示す通りの関係を求
める。
This pretreatment and anodic oxidation treatment may be carried out by any conventional method as long as the purpose can be achieved, and of course it is sufficient if the electrolytic conditions etc. are also carried out in a conventional manner. Next, after anodizing the aluminum material as described above, it is immersed in an electrolytic bath containing metal salts and electrolyzed there to color the anodic oxide film on its surface. The film is electrolytically colored, and the relationship shown in FIG. 2 between the capacitance impedance and brightness of the anodic oxide film is determined.

なお、この際の電解着色処理とは電解浴中の金属イオン
を予め生成した陽極酸化皮膜の孔隙中に析出させて着色
させる処理のことを一般的に示し、通常の場合は、交流
電解で十分であるが、このほかに、直流電解、パルス電
解若しくはこれらの波形と交流との組合わせによる電解
等によつても着色できる。次に、以上の通りにアルミニ
ウム材を予備的に電解したのち、続いて、工業的にアル
ミニウム材を電解着色し、この際は、電解中の陽極酸化
皮膜の容量インピーダンスは後記の如く連続的に測定し
、その値が各アルミニウム材について先に求めた関係に
おいて予め定めた所望の明度に対応する値に達する迄電
解を連続的に行なう。
In addition, the electrolytic coloring treatment in this case generally refers to a treatment in which metal ions in an electrolytic bath are precipitated into the pores of a pre-generated anodic oxide film and colored. In normal cases, AC electrolysis is sufficient. However, in addition to this, coloring can also be achieved by direct current electrolysis, pulse electrolysis, or electrolysis using a combination of these waveforms and alternating current. Next, after preliminarily electrolyzing the aluminum material as described above, the aluminum material is then electrolytically colored industrially. At this time, the capacitive impedance of the anodic oxide film during electrolysis is continuously changed as described below. Electrolysis is continuously performed until the value reaches a value corresponding to a predetermined desired brightness based on the relationship previously determined for each aluminum material.

このようにアルミニウム材を電解着色すると、アルミニ
ウム材は常に所望の明度の色に均一に着色され、電解中
若しくはその後に何んら色合わせを行なう必要がない。
すなわち、予め陽極酸化皮膜を生成したアルミニウム材
を金属塩を含む水溶液中において交流電解すると、その
電解着色の進行とともに、電流波形は、第1図でイで示
す通りにひずんでくることが知られている。
When an aluminum material is electrolytically colored in this manner, the aluminum material is always uniformly colored to a desired brightness, and there is no need for any color matching during or after electrolysis.
In other words, it is known that when an aluminum material on which an anodic oxide film has been formed is subjected to alternating current electrolysis in an aqueous solution containing a metal salt, as the electrolytic coloring progresses, the current waveform becomes distorted as shown by A in Figure 1. ing.

また、このようにひずんだ電解電流は反応電流(フアラ
デ一電流)(第1図で口で示す)と、容量電流(第1図
でハで示す)との和から成つていることも知られている
。然るに、この反応電流は電解浴中の金属イオンや水素
イオンの還元反応速度に関連し、これらのもとにおける
変数であり、これに対し、電解時間が経過すると、容量
電流は変化するが、このように容量電流が変化するのは
、電解時間の長短によつて陽極酸化皮膜の孔隙中に析出
する金属析出量が変化するからである。このため、本発
明者は容量電流が金属の析出量に関係することに着目し
、具体的に容量電流の変化と陽極酸化皮膜の着色度合と
の関係を求めた。
It is also known that the electrolytic current distorted in this way is made up of the sum of the reaction current (Falade current) (indicated by C in Fig. 1) and the capacitive current (indicated by C in Fig. 1). ing. However, this reaction current is related to the reduction reaction rate of metal ions and hydrogen ions in the electrolytic bath, and is a variable under these.On the other hand, as the electrolysis time elapses, the capacitive current changes, but this The reason why the capacitance current changes is that the amount of metal deposited in the pores of the anodic oxide film changes depending on the length of the electrolysis time. Therefore, the present inventor focused on the fact that the capacitance current is related to the amount of metal precipitation, and specifically determined the relationship between the change in the capacitance current and the degree of coloration of the anodic oxide film.

このところ、容量電流の変化によつて他の電解条件にあ
まり影響されることなく陽極酸化皮膜の着色度合は変化
した。また、更にこの関係について電解着色時の制御因
子と着色度合との関係を求めたところ、陽極酸化皮膜の
容量インピーダンス(以下、単に容量インピーダンスと
する。
Recently, the degree of coloring of the anodic oxide film changed due to changes in capacitance current without being significantly influenced by other electrolytic conditions. Further, regarding this relationship, when we determined the relationship between control factors during electrolytic coloring and the degree of coloring, we found that the capacitive impedance (hereinafter simply referred to as capacitive impedance) of the anodic oxide film.

)は該皮膜の着色度合(特に、明度)を第2図に示す通
りに比例すること、を知見した。そこで、本発明法にお
いては、電解着色中の容量インピーダンスが大きくなる
とともに、陽極酸化皮膜の明度は小さくなるために(明
度が小さい方が濃色化する)、電解中における陽極酸化
皮膜の着色度合は、その容量インピーダンスの値によつ
て決め、予め所望の容量インピーダンスを定めて電解中
に容量インピーダンスがその値になつたときに、電解を
停止する。
) was found to be proportional to the degree of coloration (particularly, brightness) of the film as shown in FIG. Therefore, in the method of the present invention, since the capacitive impedance during electrolytic coloring increases and the brightness of the anodic oxide film decreases (the lower the brightness, the darker the color), the degree of coloring of the anodic oxide film during electrolysis increases. is determined based on the value of the capacitive impedance, a desired capacitive impedance is determined in advance, and when the capacitive impedance reaches that value during electrolysis, the electrolysis is stopped.

このように電解すると、常に容量インピーダンスが一定
の陽極酸化皮膜が得られ、その着色度合が常に一定にな
り、電解後に何んらの色合わせを必要としない。
When electrolyzed in this manner, an anodic oxide film with a constant capacitance impedance is always obtained, the degree of coloration is always constant, and no color matching is required after electrolysis.

なお、この理由については未だ不明のところも多いが、
電解中において陽極酸化皮膜の着色度合は該皮膜の生成
度合よりむしろそのときの金属の析出量のほかにその態
様等によつて決まり、これらは容量インピーダンスであ
ると、定量的に容易に把握できるからであると思われる
Although there are still many unknown reasons for this,
The degree of coloring of the anodized film during electrolysis is determined by the amount of metal deposited at that time and its mode, rather than the degree of formation of the film, and these can be easily understood quantitatively as capacitive impedance. It seems to be from

また、以上の通りの電解時の容量インピーダンスと明度
の関係や、更に、その後に陽極酸化皮膜の容量インピー
ダンスを連続的に検出するときには、通常、第3図の通
りの構成に係る装置によれば容易に実施できる。
In addition, when detecting the relationship between capacitive impedance and brightness during electrolysis as described above, and furthermore, when continuously detecting the capacitive impedance of the anodic oxide film, the apparatus having the configuration shown in Fig. 3 is usually used. Easy to implement.

すなわち、第3図において符号1はトランス、2は電位
検出器、3は電解槽、4は電流検出器、5は同調検出器
、6は容量インピーダンス測定器である。
That is, in FIG. 3, reference numeral 1 is a transformer, 2 is a potential detector, 3 is an electrolytic cell, 4 is a current detector, 5 is a tuning detector, and 6 is a capacitive impedance measuring device.

従つて、この装置においては、例えば、予め陽極酸化処
理されたアルミニウム材を一方の極若しくは両極として
、その間にトランス1によつて、例えば交流電圧がかけ
られて交流電解が行なわれる。この電解時に両極間の電
圧は電位検出器2によつて測定され、電解時の電流は電
流検出器4によつて検出される。また、このように得ら
れる電流は、第1図においてイに相当する交流波形を示
し、このため、該電流は同期検出器5において容量電流
(第1図において口に相当)のみが分離され測定される
Therefore, in this device, for example, an aluminum material that has been anodized in advance is used as one or both poles, and an alternating current voltage is applied therebetween by the transformer 1 to perform alternating current electrolysis. During this electrolysis, the voltage between the two electrodes is measured by a potential detector 2, and the current during electrolysis is detected by a current detector 4. In addition, the current obtained in this way shows an AC waveform corresponding to A in Fig. 1, and therefore, only the capacitive current (corresponding to the opening in Fig. 1) is separated and measured in the synchronous detector 5. be done.

また、上記の通りに電位検出器2によつて得られる電圧
は容量インピーダンス測定器6に入り、また、分離され
た容量電流は該測定器6に入るため、そこで電解中の容
量インピーダンスは数値比して求められる。これによる
と、第2図に示す傾向の関係を求めると共に、その後の
電解着色時にも該測定器6において容量インピーダンス
を連続的に測定し、その値が所望の明度に対応する値に
なつたときに電解を終了すれば、同明度に着色処理でき
る。また、上記のところでは交流電解の場合について説
明したが、これ以外の波形の電解、例えば、パルス波形
であつても、第3図の装置によつて容易に実施できる。
Further, as mentioned above, the voltage obtained by the potential detector 2 enters the capacitive impedance measuring device 6, and the separated capacitive current enters the measuring device 6, so that the capacitive impedance during electrolysis is determined by the numerical ratio. required. According to this, in addition to finding the trend relationship shown in FIG. 2, the capacitive impedance is also continuously measured with the measuring device 6 during subsequent electrolytic coloring, and when the value corresponds to the desired brightness, If electrolysis is completed at , coloring can be done to the same brightness. Furthermore, although the case of alternating current electrolysis has been described above, even electrolysis with a waveform other than this, for example, a pulse waveform, can be easily carried out using the apparatus shown in FIG.

また、第3図に示す装置によつて所定アルミニウム材に
つき容量インピーダンスと明度の関係を求めておき、こ
の関係にもとずいて第4図に示す装置を用いると、アル
ミニウム材は容易に一定明度に着色処理できる。
Furthermore, if the relationship between capacitive impedance and brightness is determined for a given aluminum material using the device shown in FIG. 3, and the device shown in FIG. Can be colored.

すなわち、第4図に示す装置では、容量インピーダンス
を予め所望値に設定しておくと、容量インピーダンスが
連続的に測定され、その値が所望値に達したときにアル
ミニウム材の着色処理が自動的に停止するものである。
In other words, in the device shown in Fig. 4, if the capacitive impedance is set to a desired value in advance, the capacitive impedance is continuously measured, and when the value reaches the desired value, the coloring process of the aluminum material is automatically performed. It is something that stops at.

従つて、第4図において破線Aで包囲されるところは、
第3図に示すところと同じ構成であつて、その同調検出
器5の出力側に比較器7を接続し、この比較器7におい
て予め選定された値と比較し、この差が零になつたとき
に、スイーツチ素子9が切られるよう構成する。
Therefore, the area surrounded by broken line A in Fig. 4 is
It has the same configuration as shown in Fig. 3, and a comparator 7 is connected to the output side of the tuning detector 5, and the comparator 7 compares it with a preselected value, and the difference becomes zero. At times, the sweet switch element 9 is configured to be turned off.

このように構成すると、電解槽3においてアルミニウム
材が所望の濃度まで着色されたときには、比較器7から
の零信号によつてスイツチ素子9がきられて、電解着色
が停止される。なお、第4図において、符号8は電流測
定器であつて、これによつて、所望色の容量インピーダ
ンスにおける容量電流を予め設定しておくことができる
。次に、実施例について説明する。
With this structure, when the aluminum material is colored to a desired concentration in the electrolytic bath 3, the switch element 9 is turned off by the zero signal from the comparator 7, and the electrolytic coloring is stopped. In FIG. 4, reference numeral 8 denotes a current measuring device, which allows the capacitive current at the capacitive impedance of a desired color to be set in advance. Next, examples will be described.

実施例 1 A1100アルミニウム材から成る板材を常法によつて
脱脂洗浄し、15%硫酸の電解浴中で常法によつて板材
の上に陽極酸化皮膜をほどこした。
Example 1 A plate made of A1100 aluminum material was degreased and cleaned by a conventional method, and an anodized film was applied on the plate by a conventional method in an electrolytic bath of 15% sulfuric acid.

次に、この板材にカーボ一材を対極とし、3%硫酸ニツ
ケル、3%ホウ酸ならびに2.5%硫酸アンモニウムを
含む水溶液から成る電解浴中において、第3図に示す装
置で12で交流電解着色をおこなつた。この結果、5分
程度の着色電解で板材の上には、濃いブロンズ色の陽極
酸化皮膜が得られた。また、この時に、容量インピーダ
ンスを測定器6で測定したところ、50サイクルにおい
ては、容量インピーダンスは135Ω/dであつた。次
に、上記のところのAllOOアルミニウム材から成る
板材を用いて、この板材についても、上記と同様に脱脂
洗浄、陽極酸化して、その後も同組成の着色電解浴中で
交流電解した。この場合、第3図の測定器6によつて5
0サイクルの容量インピーダンスを観察しつつ着色電解
を行なつて、その値が135Ω/dに達した時、通電を
停止し電解を終了した。
Next, this plate material was subjected to alternating current electrolytic coloring at 12 in the apparatus shown in Fig. 3 in an electrolytic bath consisting of an aqueous solution containing 3% nickel sulfate, 3% boric acid, and 2.5% ammonium sulfate, with a carbon material as a counter electrode. I did this. As a result, a deep bronze-colored anodic oxide film was obtained on the plate material by coloring electrolysis for about 5 minutes. Further, at this time, the capacitive impedance was measured with the measuring device 6, and the capacitive impedance was 135 Ω/d in 50 cycles. Next, using the plate material made of the AllOO aluminum material mentioned above, this plate material was also degreased, cleaned and anodized in the same manner as above, and then AC electrolyzed in a colored electrolytic bath having the same composition. In this case, the measuring device 6 of FIG.
Coloring electrolysis was performed while observing the capacitance impedance in the 0th cycle, and when the value reached 135Ω/d, the current supply was stopped and the electrolysis was completed.

このようにして板材の上に着色陽極酸化皮膜を生成した
ところ、その色は先に得られた板材の色と全く同じで、
更に、測色色差計で明度を測定したところいずれも26
.5であつて、濃度も完全に一致した。実施例 2実施
例1と同様な条件で、AllOOアルミ.ニウム材の板
材を第4図に示す装置において交流電圧を加えて、電解
着色を行なつた。
When a colored anodic oxide film was produced on the board in this way, the color was exactly the same as the color of the board previously obtained,
Furthermore, when I measured the brightness with a colorimeter, the brightness was 26.
.. 5, and the concentrations were also completely consistent. Example 2 Under the same conditions as Example 1, AllOO aluminum. An alternating current voltage was applied to the aluminum plate in the apparatus shown in FIG. 4 to electrolytically color the plate.

この場合は、所望色の濃度に対応する容量インピーダン
スのものにおける容量電流を予め電流測定器8に設定し
て置いた。この条件で交流電解して着色処理を行なつて
、同様検出器5で容量電流を検出しつつ、この値と設定
電流とを比較器7において比較し、その差が零になつた
時には、スイツチ素子9に信号を送つて自動的に電流し
や断し、電解着色を終了した。このようにして5回くり
かえして電解したところ、5回とも得られた色は同じだ
つた。以上詳しく説明した通り、本発明法は、金属塩を
含む電解浴中で着色電解する際に、そのときの着色若し
くは濃度の因子を容量インピーダンスとしてとらえて、
これを目安として着色処理するため、色合わせを必要と
しないほか、電解着色工程自体を電解槽外でコントロー
ルでき、その制御を自動化できる。また、このように正
確に着色度合をコントロールできるところから、製品の
不良化が防止でき、更に、電解着色時の省力化や、生産
性の向上も達成できる。
In this case, the capacitive current of a capacitive impedance corresponding to the desired color density was set in the current measuring device 8 in advance. Under these conditions, perform alternating current electrolysis and coloring, while similarly detecting the capacitance current with detector 5, compare this value with the set current in comparator 7, and when the difference becomes zero, switch A signal was sent to element 9 to automatically cut off the current and complete electrolytic coloring. When electrolysis was repeated five times in this manner, the color obtained was the same all five times. As explained in detail above, the method of the present invention, when carrying out colored electrolysis in an electrolytic bath containing a metal salt, considers the coloring or concentration factor at that time as capacitive impedance,
Since the coloring process uses this as a guide, there is no need for color matching, and the electrolytic coloring process itself can be controlled outside the electrolytic bath, making it possible to automate the process. Furthermore, since the degree of coloring can be accurately controlled in this way, it is possible to prevent product defects, and furthermore, it is possible to save labor during electrolytic coloring and improve productivity.

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

第1図は本発明法において電解時の電流波形の解析態様
の説明図、第2図は本発明法における容量インピーダン
スと明度との関係の一例を示すグラフ、第3図ならびに
第4図はそれぞれ本発明法を実施する装置の一例の回路
図である。 符号、1・・・・・・トランス、2・・・・・・電位検
出器、3・・・・・・電解槽、4・・・・・・電流検出
器、5・・・・・・同調検出器、6・・・・・・容量イ
ンピーダンス測定器、7・・・・・・比較器、8・・・
・・・電流測定器、9・・・・・・スイツチ素子。
Figure 1 is an explanatory diagram of the analysis aspect of the current waveform during electrolysis in the method of the present invention, Figure 2 is a graph showing an example of the relationship between capacitive impedance and brightness in the method of the present invention, Figures 3 and 4 are respectively 1 is a circuit diagram of an example of a device implementing the method of the present invention; FIG. Code, 1...Transformer, 2...Potential detector, 3...Electrolytic cell, 4...Current detector, 5... Tuning detector, 6... Capacitive impedance measuring device, 7... Comparator, 8...
...Current measuring device, 9...Switch element.

Claims (1)

【特許請求の範囲】[Claims] 1 予め陽極酸化処理されたアルミニウム若しくはその
合金材を金属塩を含む電解浴中において電解着色処理す
る際に、まず、アルミニウム若しくはその合金材を予備
的に電解着色処理して、その予備処理時の陽極酸化皮膜
の容量インピーダンスと陽極酸化皮膜明度との関係を求
めた後、アルミニウム若しくはその合金材を連続的に電
解着色処理すると共に、その間の陽極酸化皮膜の容量イ
ンピーダンスを連続的に求め、その容量インピーダンス
が前記関係において所望明度に対応する容量インピーダ
ンスに達したところで電解着色処理を終了させることを
特徴とするアルミニウム若しくはその合金材の電解着色
法。
1. When subjecting pre-anodized aluminum or its alloy material to electrolytic coloring in an electrolytic bath containing a metal salt, first the aluminum or its alloy material is preliminarily electrolytically colored; After determining the relationship between the capacitive impedance of the anodic oxide film and the brightness of the anodic oxide film, the aluminum or its alloy material is continuously electrolytically colored, and the capacitive impedance of the anodic oxide film during that time is continuously determined. An electrolytic coloring method for aluminum or its alloy material, characterized in that the electrolytic coloring process is terminated when the impedance reaches a capacitance impedance corresponding to a desired brightness in the above relationship.
JP10357577A 1977-08-31 1977-08-31 Electrolytic coloring method for aluminum or its alloy materials Expired JPS5943559B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10357577A JPS5943559B2 (en) 1977-08-31 1977-08-31 Electrolytic coloring method for aluminum or its alloy materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10357577A JPS5943559B2 (en) 1977-08-31 1977-08-31 Electrolytic coloring method for aluminum or its alloy materials

Publications (2)

Publication Number Publication Date
JPS5437041A JPS5437041A (en) 1979-03-19
JPS5943559B2 true JPS5943559B2 (en) 1984-10-23

Family

ID=14357578

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10357577A Expired JPS5943559B2 (en) 1977-08-31 1977-08-31 Electrolytic coloring method for aluminum or its alloy materials

Country Status (1)

Country Link
JP (1) JPS5943559B2 (en)

Also Published As

Publication number Publication date
JPS5437041A (en) 1979-03-19

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