JPS5884996A - Electrolytic coloring method for aluminum - Google Patents

Electrolytic coloring method for aluminum

Info

Publication number
JPS5884996A
JPS5884996A JP18323181A JP18323181A JPS5884996A JP S5884996 A JPS5884996 A JP S5884996A JP 18323181 A JP18323181 A JP 18323181A JP 18323181 A JP18323181 A JP 18323181A JP S5884996 A JPS5884996 A JP S5884996A
Authority
JP
Japan
Prior art keywords
aluminum
electrolytic coloring
coloring method
weakly acidic
sulfate
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.)
Granted
Application number
JP18323181A
Other languages
Japanese (ja)
Other versions
JPS6233318B2 (en
Inventor
Shoichi Tsuchiya
正一 土屋
Masayuki Sawaguchi
沢口 雅之
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.)
Nihon Kentetsu Co Ltd
Original Assignee
Nihon Kentetsu 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 Nihon Kentetsu Co Ltd filed Critical Nihon Kentetsu Co Ltd
Priority to JP18323181A priority Critical patent/JPS5884996A/en
Publication of JPS5884996A publication Critical patent/JPS5884996A/en
Publication of JPS6233318B2 publication Critical patent/JPS6233318B2/ja
Granted legal-status Critical Current

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Landscapes

  • Electrochemical Coating By Surface Reaction (AREA)

Abstract

PURPOSE:To form a superior colored film by supplying AC to anodic oxidized Al in a weakly acidic electrolytic soln. contg. nickel sulfate and stannous sulfate as principal coloring components. CONSTITUTION:A weakly acidic electrolytic soln. contg. 5-30g/l nickel sulfate and 3-10g/l stannous sulfate as principal coloring components is adjusted to 5-7pH (7 is not included). To the soln. may be added a proper amount of ammonium sulfate, boric acid or tartaric acid, and to increase the pH an aqueous ammonia soln. is used. AC is supplied to anodically oxidized Al in the electrolytic soln. to form a superior colored film while preventing decoloring and the aging of the coloring components and enhancing the throwing power.

Description

【発明の詳細な説明】 本発明は陽極酸化処理を施したアルミニウムまたはアル
ミニウム合金(以下アルミニウムと称する)の電解着色
法に関し、1らに具体的には着色浴として硫酸ニッケル
および硫酸第1ヌズを着色主成分として含有する弱酸性
電解液を用いるアルミニウムの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 aluminum alloy (hereinafter referred to as aluminum) that has been subjected to anodizing treatment. This invention relates to an electrolytic coloring method for aluminum using a weakly acidic electrolyte containing as a main coloring component.

アルミニウムを着色するには、従来、常法により陽極酸
化処理して酸化皮膜を形成したアルミニウムに、金属塩
を含有する着色浴中で交流通電して所望の着色皮膜を形
成する方法が一般に用いられて来た。
Conventionally, to color aluminum, a method is generally used in which the aluminum has been anodized to form an oxide film using a conventional method, and then an alternating current is applied in a coloring bath containing a metal salt to form the desired colored film. I came.

かかる着色浴として酸性着色浴が一般的であるが、比較
的優れたっき捷ゎり性をもたらすという長所を有する反
面、酸性度が高い(換言すればpHが低い)ことに基因
して着色後直ちに水洗いしないと色抜けを起したり、ま
だ浴管理も複雑である等の短所も秤っていることが知ら
れている。
Acidic coloring baths are commonly used as such coloring baths, but while they have the advantage of providing relatively excellent dispersibility, they are highly acidic (in other words, have a low pH) and cannot be used immediately after coloring. It is known that it also has disadvantages such as color fading if not washed with water and bath management is still complicated.

一方、特開昭49−28544等により、中性またはア
ルカリ性着色浴を用いるアルミニウムの電解着色法も提
案されているが、かかる中性またはアルカリ性着色浴は
水洗いしなくとも色抜けが殆んど生起しない利点を有す
るに4かかわらず、浴の老化速度が著°シ<速いため、
浴管理が難しいという欠点を有することが知られている
。−また、従来の酸性、中性および弱アルカリ性のpH
域の着色浴からはブロンズルブラツク系の色調が主体で
、他の色調を容易に得ることが難しい等の問題も依然と
して未解失であった。
On the other hand, an electrolytic coloring method for aluminum using a neutral or alkaline coloring bath has been proposed in JP-A-49-28544, etc., but such a neutral or alkaline coloring bath causes almost no color fading even without washing with water. Although it has no advantage, the aging rate of the bath is extremely fast.
It is known that bath management is difficult. - also conventional acidic, neutral and slightly alkaline pH
The coloring baths in the area mainly produced bronze-black tones, and problems such as the difficulty of easily obtaining other tones remained unresolved.

本発明は上記のような従来の着色浴の欠点を解決するこ
とを目的として、さらに具体的には、硫酸ニッケルおよ
び硫酸第1スズを着色主成分とし、その電解着色浴を弱
酸性に調整維持し、色抜けと着色成分の老化防止をはか
り、つきまわり性を向上させ、さらに従来のブロンズル
ブラツク系の色調にダレイ系の色調をも加えた優れた着
色皮膜を生成するアルミニウムの′電解着色法を提供す
ることを主たる目的とする。
The present invention aims to solve the above-mentioned drawbacks of conventional coloring baths, and more specifically, the present invention uses nickel sulfate and stannous sulfate as main coloring components, and adjusts and maintains the electrolytic coloring bath to be slightly acidic. Electrolytic coloring of aluminum that prevents color fading and aging of coloring components, improves throwing power, and creates an excellent colored film that adds a dull color to the conventional bronze black color tone. The main purpose is to provide law.

従って、本発明のアルミニウムの電解着色法は陽極酸化
処理を施したアルミニウムに硫酸ニッケルおよび硫酸第
1スズを着色主成分とした弱酸性電解液中で交流通電を
行ない、添加金属塩独特の色調を得ることを特徴とする
Therefore, in the electrolytic coloring method of aluminum of the present invention, anodized aluminum is subjected to alternating current in a weakly acidic electrolyte containing nickel sulfate and stannous sulfate as main coloring components, thereby producing a color tone unique to added metal salts. It is characterized by obtaining.

上記弱酸性電解液のpHの範囲は目的とする色調やその
他の着色処理条件により変わり得るものであり、例えば
ダレイの色調を得る場合は、pH5〜7(但しpH7を
含まず)の範囲が望ましい。
The pH range of the weakly acidic electrolyte may vary depending on the desired color tone and other coloring processing conditions; for example, when obtaining a dull color tone, a pH range of 5 to 7 (excluding pH 7) is desirable. .

一方、上記弱酸性電解液中の硫酸ニッケルおよび硫酸第
1スズの濃度も、上記pH同様に目的とする色調やその
他の着色処理条件により変わり得るものであるが、一般
的にそれぞれ5〜30 P/Zおよび3〜10 P/l
eの範囲が望ましい。特に硫酸  ・第1スズを10 
ft/Zを越えて用いると、着色浴中に多量に沈澱する
ことKなるので望ましくない。
On the other hand, the concentrations of nickel sulfate and stannous sulfate in the weakly acidic electrolyte can also vary depending on the desired color tone and other coloring treatment conditions, similar to the pH above, but generally each is between 5 and 30 P. /Z and 3-10 P/l
A range of e is desirable. Especially sulfuric acid, stannous 10
If it is used in excess of ft/Z, a large amount of precipitation may occur in the coloring bath, which is undesirable.

また上記電解液は、さらに硫酸アンモニウム、はう酸お
よび酒石酸を必要に応じて適当量含有することができる
0さらに必要に応じて上記電解液を調整することも可能
であり、pHを上げる場合(即ち中性側に近づける場合
)はアンモニア水を加えることにより実施される。
Further, the electrolytic solution may further contain appropriate amounts of ammonium sulfate, halonic acid, and tartaric acid as necessary. Furthermore, the electrolytic solution can be adjusted as necessary, and when raising the pH (i.e. When approaching the neutral side), this is done by adding aqueous ammonia.

その他の電解着色条件、例えば交流電源電圧、周波数、
電流密度、通電時間および着色浴温等は通常のアルミニ
ウムの電解着色法において用いられている範囲から適宜
選択される。例えば、電圧として、16〜17Vの範囲
から選択するのが色調およびスポーリング発生防止の観
点から好ましい。
Other electrolytic coloring conditions, such as AC power voltage, frequency,
The current density, current application time, coloring bath temperature, etc. are appropriately selected from the ranges used in ordinary electrolytic coloring methods for aluminum. For example, it is preferable to select the voltage from the range of 16 to 17 V from the viewpoint of color tone and prevention of spalling.

通電時間も目的とする色調や他の着色条件によりさまざ
まに変り得るものであるが、通常1〜10分間が適当で
あ、る。周波数は通常の交流電源をそのまま利用するの
が簡便であり、従って50Hzまたは<5OHzである
。さらに対極としては、従来の電解着色法と同様に、カ
ーボン、スズ、ニッケル板等が利用される0 本発明の電解着色法によれば、従来のブロンズルブラツ
ク系の色調の他、今まで簡単に得ることができなかった
ダレイ色の着色が可能になった。
Although the current application time can vary depending on the desired color tone and other coloring conditions, 1 to 10 minutes is usually appropriate. It is convenient to use a normal AC power source as is, and therefore the frequency is 50Hz or <5OHz. Further, as a counter electrode, carbon, tin, nickel plate, etc. are used as in the conventional electrolytic coloring method. According to the electrolytic coloring method of the present invention, in addition to the conventional bronze color tone, It is now possible to create dull colors that were previously unavailable.

さらに本発明の方法において用いる弱酸性着色浴は従来
の酸性着色浴と比べ耐食性およびつきまわり性に優れ、
且つ中性、弱アルカリ性着色浴よりも耐老化性に優れた
特長を持っていることが判明した。
Furthermore, the weakly acidic coloring bath used in the method of the present invention has superior corrosion resistance and throwing power compared to conventional acidic coloring baths,
In addition, it was found to have superior aging resistance than neutral or weakly alkaline coloring baths.

次に本発明の実施例を示す。Next, examples of the present invention will be shown.

実施例 1 アルミニウム板を常法に従い前処理した後、150 P
/Jの硫酸浴中で直流電解し、14μmの陽極酸化皮膜
を形成した。
Example 1 After pre-treating an aluminum plate according to a conventional method, 150 P
Direct current electrolysis was carried out in a sulfuric acid bath of 14 μm to form an anodic oxide film of 14 μm.

次いで、下記組成およびpHの電解着色浴中でカーボン
を対極とし、15Vで5分間交流電解を行なったところ
、均一なブロンズの着色アルミニウムが得られた。
Next, alternating current electrolysis was performed at 15 V for 5 minutes in an electrolytic coloring bath having the following composition and pH using carbon as a counter electrode, and a uniform bronze colored aluminum was obtained.

浴組成:硫酸第1スズ     61/!硫酸ニツケル
    15P/l。
Bath composition: stannous sulfate 61/! Nickel sulfate 15P/l.

酒石酸       20 P/i 硫酸アンモニウム  20 ?−/l。Tartaric acid 20 P/i Ammonium sulfate 20? -/l.

ほう酸    20 f/1 浴pH:      5.5 実施例 2 実施例1と同様にアルミニウム板を前処理および陽極酸
化処理して14μmの陽極酸化皮膜を形成した。
Boric acid 20 f/1 Bath pH: 5.5 Example 2 An aluminum plate was pretreated and anodized in the same manner as in Example 1 to form an anodic oxide film of 14 μm.

次いで実施例1で用いた電解着色浴中、カーボンを対極
とし、17Vで105+間交流電解を行なったところ、
均一なブラックの着色アルミニウムが得られた。
Next, in the electrolytic coloring bath used in Example 1, carbon was used as a counter electrode, and AC electrolysis was performed at 17 V for 105+.
A uniform black colored aluminum was obtained.

実施例 3 実施例1および2と同様に20μmの陽極酸化皮膜を形
成したアルミニウム板を実施例2で用いた電解着色浴中
、15Vで2分間交流電解したところ、均一なグレイの
着色アルミニウムが得られた。
Example 3 An aluminum plate on which a 20 μm anodic oxide film was formed in the same manner as in Examples 1 and 2 was subjected to alternating current electrolysis at 15 V for 2 minutes in the electrolytic coloring bath used in Example 2, and a uniform gray colored aluminum was obtained. It was done.

上記実施例にて使用した電解着色浴を分析したところ、
実質的に老化は生起していないことが認められた。また
、それぞれの着色アルミニウムを電解着色処理完了の後
、直ちに水洗することなく、そのまま放置したが、いず
れの実施例においても殆んど色抜けが認められなかった
Analysis of the electrolytic coloring bath used in the above examples revealed that
It was observed that virtually no aging occurred. In addition, after the completion of the electrolytic coloring treatment, each colored aluminum was left as it was without immediately washing with water, but almost no color fading was observed in any of the examples.

Claims (1)

【特許請求の範囲】 (1)、陽極酸化処理を施したアルミニウムに硫酸ニッ
ケルおよび硫酸第1スズを着色主成分とした弱酸性電解
液中で交流通電を行ない、添加金属塩独特の色調を得る
ことを特徴とするアルミニウムの電解着色法。 (り、特許請求の範囲第1項に記載の電・解着色法にお
いて、前記弱酸性電解液はpH5〜7(pH7を含まず
)の範囲であるアルミニウムの電解着色法。 (3)、特許請求の範囲第1項に記載の電解着色法にお
いて、前記弱酸性電解液中の硫酸ニッケルおよび硫酸第
1スズの濃度は、それぞ−れ5〜3011/I、、およ
び6〜10 fll13の範囲であるアルミニウムの電
解着色法。 (4)、特許請求の範囲第1〜6項のいずれか1項に記
載の電解着色法において、前記弱酸性電解液はさらに硫
酸アンモニウム、はう酸および酒石酸を含有するアルミ
ニウムの電解着色法。 (9,特許請求の範囲第1〜4項のいずれか1項に記載
の電解着色法において、前記弱酸性電解液はサラニアン
モニア水を含有し、とのアンモニア水によりpH調整さ
れているアルミニウムの電解着色法。
[Claims] (1) Anodized aluminum is subjected to alternating current in a weakly acidic electrolyte containing nickel sulfate and stannous sulfate as main coloring components to obtain a color tone unique to added metal salts. An electrolytic coloring method for aluminum characterized by: (2) In the electrolytic coloring method according to claim 1, the weakly acidic electrolyte has a pH in the range of 5 to 7 (excluding pH 7). (3), Patent In the electrolytic coloring method according to claim 1, the concentrations of nickel sulfate and stannous sulfate in the weakly acidic electrolyte are in the range of 5 to 3011/I and 6 to 10 fl13, respectively. An electrolytic coloring method for aluminum. (4) In the electrolytic coloring method according to any one of claims 1 to 6, the weakly acidic electrolyte further contains ammonium sulfate, malic acid, and tartaric acid. (9) In the electrolytic coloring method according to any one of claims 1 to 4, the weakly acidic electrolyte contains salanium ammonia water, and Electrolytic coloring method for pH-adjusted aluminum.
JP18323181A 1981-11-16 1981-11-16 Electrolytic coloring method for aluminum Granted JPS5884996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18323181A JPS5884996A (en) 1981-11-16 1981-11-16 Electrolytic coloring method for aluminum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18323181A JPS5884996A (en) 1981-11-16 1981-11-16 Electrolytic coloring method for aluminum

Publications (2)

Publication Number Publication Date
JPS5884996A true JPS5884996A (en) 1983-05-21
JPS6233318B2 JPS6233318B2 (en) 1987-07-20

Family

ID=16132071

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18323181A Granted JPS5884996A (en) 1981-11-16 1981-11-16 Electrolytic coloring method for aluminum

Country Status (1)

Country Link
JP (1) JPS5884996A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5313587A (en) * 1976-07-22 1978-02-07 Kopp Erich Rotaryytype apparatus for manufacturing cotton pellet
JPS5441547A (en) * 1977-07-28 1979-04-02 Helms William R Load resisting inlet device and supporting device
JPS5536278A (en) * 1978-09-08 1980-03-13 Diafoil Co Ltd Colored polyester film
JPS5536720A (en) * 1978-09-07 1980-03-14 Aida Eng Ltd Method of measuring accuracy of gear

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5313587A (en) * 1976-07-22 1978-02-07 Kopp Erich Rotaryytype apparatus for manufacturing cotton pellet
JPS5441547A (en) * 1977-07-28 1979-04-02 Helms William R Load resisting inlet device and supporting device
JPS5536720A (en) * 1978-09-07 1980-03-14 Aida Eng Ltd Method of measuring accuracy of gear
JPS5536278A (en) * 1978-09-08 1980-03-13 Diafoil Co Ltd Colored polyester film

Also Published As

Publication number Publication date
JPS6233318B2 (en) 1987-07-20

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