JPS6360119B2 - - Google Patents
Info
- Publication number
- JPS6360119B2 JPS6360119B2 JP9283081A JP9283081A JPS6360119B2 JP S6360119 B2 JPS6360119 B2 JP S6360119B2 JP 9283081 A JP9283081 A JP 9283081A JP 9283081 A JP9283081 A JP 9283081A JP S6360119 B2 JPS6360119 B2 JP S6360119B2
- Authority
- JP
- Japan
- Prior art keywords
- coloring
- paint
- colored
- film
- treated
- 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
Links
- 238000004040 coloring Methods 0.000 claims description 54
- 238000000034 method Methods 0.000 claims description 37
- 239000000463 material Substances 0.000 claims description 34
- 229910052782 aluminium Inorganic materials 0.000 claims description 27
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 24
- 238000000576 coating method Methods 0.000 claims description 24
- 239000011248 coating agent Substances 0.000 claims description 23
- 238000005868 electrolysis reaction Methods 0.000 claims description 18
- 238000007598 dipping method Methods 0.000 claims description 6
- 238000004043 dyeing Methods 0.000 claims description 4
- 229910000838 Al alloy Inorganic materials 0.000 claims description 3
- 239000003929 acidic solution Substances 0.000 claims description 2
- 229920003002 synthetic resin Polymers 0.000 claims description 2
- 239000000057 synthetic resin Substances 0.000 claims description 2
- 239000003973 paint Substances 0.000 description 42
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 20
- 239000010407 anodic oxide Substances 0.000 description 13
- 238000004042 decolorization Methods 0.000 description 10
- 238000010422 painting Methods 0.000 description 10
- 239000002904 solvent Substances 0.000 description 10
- 238000001035 drying Methods 0.000 description 8
- 238000007743 anodising Methods 0.000 description 7
- 229910000906 Bronze Inorganic materials 0.000 description 6
- 239000010974 bronze Substances 0.000 description 6
- KUNSUQLRTQLHQQ-UHFFFAOYSA-N copper tin Chemical compound [Cu].[Sn] KUNSUQLRTQLHQQ-UHFFFAOYSA-N 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 5
- 229920005989 resin Polymers 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- JPJALAQPGMAKDF-UHFFFAOYSA-N selenium dioxide Chemical compound O=[Se]=O JPJALAQPGMAKDF-UHFFFAOYSA-N 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- -1 aluminum ions Chemical class 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004070 electrodeposition Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 2
- 239000004327 boric acid Substances 0.000 description 2
- 229910000960 colored gold Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229910000365 copper sulfate Inorganic materials 0.000 description 2
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000003618 dip coating Methods 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 2
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 2
- 238000007591 painting process Methods 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000004381 surface treatment Methods 0.000 description 2
- 229920001187 thermosetting polymer Polymers 0.000 description 2
- FAKFSJNVVCGEEI-UHFFFAOYSA-J tin(4+);disulfate Chemical compound [Sn+4].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O FAKFSJNVVCGEEI-UHFFFAOYSA-J 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241001364904 Phyllocladus toatoa Species 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000002048 anodisation reaction Methods 0.000 description 1
- UMEAURNTRYCPNR-UHFFFAOYSA-N azane;iron(2+) Chemical compound N.[Fe+2] UMEAURNTRYCPNR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006103 coloring component Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000011253 protective coating Substances 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
- 229910000368 zinc sulfate Inorganic materials 0.000 description 1
- 229960001763 zinc sulfate Drugs 0.000 description 1
Landscapes
- Application Of Or Painting With Fluid Materials (AREA)
- Electrochemical Coating By Surface Reaction (AREA)
Description
【発明の詳細な説明】
この発明は、アルミニウム又はアルミニウム合
金(以下両者を単にアルミニウムと呼称)の模様
着色処理方法に関するもので、その目的は、陽極
酸化皮膜形成後のアルミニウムに模様着色を施す
場合、前後二回の着色工程の間に独自の処理工程
を介在させて着色を行なうことにより、アルミニ
ウムの表面にコーナー部分と他の部分とで色調の
異なる模様着色皮膜が得られる新規なアルミニウ
ムの模様着色処理方法を提供することにある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for coloring aluminum or aluminum alloy (hereinafter simply referred to as aluminum) in a pattern, and its purpose is to color pattern aluminum after an anodic oxide film has been formed. By interposing a unique treatment process between the two coloring processes, a new aluminum pattern is created that creates a patterned colored film on the surface of the aluminum with different tones in the corners and other parts. An object of the present invention is to provide a coloring treatment method.
従来、アルミニウムの陽極酸化皮膜に色調の異
なつた模様着色を施す方法としては、陽極酸化処
理又は更に電解着色等により着色したアルミニウ
ムを熱硬化型の着色塗料を用いて浸漬塗装を行な
い、アルミニウム表面の凹凸部と平坦部の違いに
よつて色調の異なる模様着色皮膜を形成する方法
(特開昭55−54592号)、あるいはエツヂ部や曲率
半径の小さなコーナー部を有するるアルミニウム
に陽極酸化処理又は更に電解着色等により着色し
たアルミニウムを熱硬化型の着色塗料で塗装し
て、エツヂ部やコーナー部と他の平坦な部分で色
調を異にする方法(特開昭55−50491号)等が知
られているが、これらの方法によれば、一応、模
様着色を形成できるが、凹凸部やエツヂ部あるい
はコーナー部を除く平坦部の色調は塗料による着
色であるため、塗料によつて着色されている部分
については樹脂が摩耗して下地の色調が露出する
ので、実際上、特に屋外の使用には困難を伴う欠
点を有している。 Conventionally, the method of coloring the anodic oxide film of aluminum in patterns with different tones is to dip-paint aluminum that has been colored by anodizing treatment or electrolytic coloring using a thermosetting coloring paint. A method of forming a patterned colored film with different tones depending on the difference between uneven parts and flat parts (Japanese Patent Application Laid-Open No. 55-54592), or anodizing or further processing of aluminum having edges or corners with a small radius of curvature. There is a known method (Japanese Patent Application Laid-Open No. 55-50491), in which aluminum colored by electrolytic coloring or the like is painted with a thermosetting coloring paint so that the color tone differs between edges, corners, and other flat areas. However, according to these methods, it is possible to form a colored pattern, but the color tone of uneven parts, edges, or flat parts other than corner parts is colored by paint, so In some areas, the resin is worn away and the underlying color tone is exposed, so this has the drawback that it is difficult to use, especially outdoors.
本発明の方法は、前記のように塗装による着色
ではなく、陽極酸化皮膜を電解着色した後、透明
合成樹脂塗料を用いて浸漬塗装処理を行なう工程
と、着色成分を脱色させる陽極処理とをたくみに
組合せる事によつて、コーナー部のみを脱色し、
脱色されたコーナー部の陽極酸化皮膜を色調の異
なる色に再着色する方法で、着色部分の摩耗や退
色のない模様着色皮膜を形成する方法であり、こ
れによつて前記従来法の問題点を一挙に解決した
ものである。 The method of the present invention does not involve coloring by painting as described above, but includes a step of electrolytically coloring the anodic oxide film, followed by dip painting using a transparent synthetic resin paint, and an anodizing process to decolorize the coloring components. By combining it with, only the corners are bleached,
This is a method of recoloring the bleached anodized film on the corners to a different color tone, forming a patterned colored film that does not wear or fade on the colored parts, thereby solving the problems of the conventional method. It was resolved all at once.
即ち、通常の浸漬法によつて単一の塗料を塗装
する場合、被塗物の表面に付着する塗膜の厚さ
は、塗料の物性あるいは被塗物の塗料中からの引
上げ速度など純物理的な要因によつて管理できる
ため、例えばアルミニウム押出形材のような等断
面長尺材の縦吊り塗装方法として広く利用されて
いるが、塗装時に於ける被塗物表面の塗料の付着
状態、即ち、塗膜の厚さは、被塗物のコーナー部
分がそれ以外の平坦な場所よりも薄くなる事は良
く知られている。この傾向は、コーナー部分の曲
率半径が小さくなるほど顕著であつて、膜厚の差
を大きくしたいときには、塗料の種類、塗膜厚さ
等の条件によつて多少異なるが、通常の場合、コ
ーナー部分の曲率半径Rを5mm以下の寸法にすれ
ば、コーナー部分と他の部分とで大きな膜厚分布
の差が得られる。 In other words, when applying a single paint using the normal dipping method, the thickness of the paint film that adheres to the surface of the object to be coated depends on pure physical properties such as the physical properties of the paint or the rate at which the object is pulled up from the paint. For example, it is widely used as a vertically hanging coating method for long materials of equal cross section such as aluminum extrusion shapes because it can be controlled by various factors. That is, it is well known that the thickness of the coating film is thinner at the corners of the object than at other flat areas. This tendency becomes more pronounced as the radius of curvature of the corner portion becomes smaller, and when it is desired to increase the difference in film thickness, it is necessary to If the radius of curvature R is set to 5 mm or less, a large difference in film thickness distribution can be obtained between the corner portion and other portions.
本発明者は、前記のように、浸漬塗装法では被
処理物のコーナー部分の膜厚が他の部分よりも薄
くなることに着目し、この現象を巧みに利用し
て、先に電解着色された陽極酸化皮膜処理材のコ
ーナー部分の脱色処理と脱色後の再着色処理とを
行なう方法により、アルミニウムの表面にコーナ
ー部分と他の部分とで色調の異なる模様着色皮膜
を得ることに成功したものであつて、次に本発明
によるアルミニウムの模様着色処理方法を具体的
且つ詳細に説明すると、この発明の方法では、
1 アルミニウムに陽極酸化皮膜を形成し、金属
塩溶液中での電解着色(一次着色)を行なう。 As mentioned above, the present inventor focused on the fact that in the dip coating method, the film thickness at the corners of the object to be treated is thinner than other parts, and skillfully utilized this phenomenon to apply electrolytic coloring first. By decolorizing the corners of the anodic oxide film treated material and recoloring it after decolorization, we succeeded in obtaining a patterned colored film on the surface of aluminum that differs in color between the corner and other parts. Next, the method of pattern coloring aluminum according to the present invention will be explained in detail. In the method of the present invention, 1. An anodic oxide film is formed on aluminum, and electrolytic coloring (primary coloring) is performed in a metal salt solution. coloring).
2 着色後の被処理材に対し、浸漬塗装法により
塗料を付着させ、被処理材表面の塗料溶剤を揮
発させる。2. Paint is applied to the colored material by dip coating, and the paint solvent on the surface of the material is evaporated.
3 電解質溶液中で陽極電解を行ない、コーナー
部分から皮膜孔中の着色成分を溶出させて脱色
する。3 Perform anodic electrolysis in an electrolyte solution to elute and decolorize the colored components in the film pores from the corner parts.
4 一次着色と異なる色調が得られる電解着色あ
るいは染色処理を行なつてコーナー部分のみを
着色(二次着色)し、コーナー部分と他の部分
とで色調の異なつた模様着色皮膜を得る。4. Perform electrolytic coloring or dyeing treatment to obtain a color tone different from the primary coloring to color only the corner portions (secondary coloring) to obtain a patterned colored film in which the color tone differs between the corner portions and other portions.
の順に処理を施すので、以下、これらの各工程に
ついて、実施の態様とその際に留意すべき事項を
工程順に詳しく説明する。Since the processing is performed in the order of , below, the mode of implementation and matters to be kept in mind for each of these steps will be explained in detail in the order of the steps.
(1) 陽極酸化皮膜及び電解着色処理
この工程での陽極酸化皮膜処理及び電解着色
処理(一次着色)は、通常行なわれている一般
的な方法でよく、電解着色には、住化法(陰極
電解着色)、浅田法(交流電解着色)のいずれ
を適用してもよい。(1) Anodic oxide film treatment and electrolytic coloring treatment The anodic oxide film treatment and electrolytic coloring treatment (primary coloring) in this process may be carried out by the commonly used methods. Either the electrolytic coloring method (electrolytic coloring) or the Asada method (AC electrolytic coloring) may be applied.
(2) 塗装処理
前記一次着色後の塗装処理には、浸漬による
塗装を行なうが、この工程での塗装は、後の工
程で施される被処理材コーナー部分の脱色と二
次着色に大きな影響を及ぼすので、次のような
点に留意して適確に行なう必要がある。(2) Painting treatment The painting process after the primary coloring is done by dipping, but the painting in this process has a great effect on the decolorization and secondary coloring of the corners of the treated material that will be applied in the later process. Therefore, it is necessary to carry out the process properly by paying attention to the following points.
(イ) 被処理材の塗装に使用する塗料は、通常の
塗装に用いる塗料であればよく、TFS塗装
法として知られるトリクレンを溶媒とする溶
剤タイプでも、一般に電着塗装法に用いられ
るような水を溶媒とする水溶性タイプでも差
支えない。 (b) The paint used for painting the material to be treated may be any paint used for normal painting, including a solvent type using trichlene as a solvent known as the TFS painting method, as well as paints such as those commonly used for electrodeposition painting. A water-soluble type that uses water as a solvent may also be used.
(ロ) けれども、次の陽極電解による脱色工程に
おいて、コーナー部分のみを選択的に電解
し、コーナー部分以外を電解しないようにす
るための塗膜厚分布は、塗装時に使用する塗
料によつて異なるので、浸漬浴の塗料濃度及
び被処理材の引上げ速度等の諸条件を使用塗
料の種類に応じて適宜設定しなければならな
い。 (b) However, in the next decolorization process using anodic electrolysis, the coating thickness distribution that selectively electrolyzes only the corner areas and does not electrolyze areas other than the corners varies depending on the paint used during painting. Therefore, various conditions such as the paint concentration in the dipping bath and the rate of pulling up the material to be treated must be set appropriately depending on the type of paint used.
例えば、塩素系溶剤型の塗料である東亜ペ
イント株式会社製のTFS塗料、トアトリペ
イントS8001(AL−2)を用いた場合には、
被処理材のコーナー部分以外の箇所に於いて
約2〜3μm以下の塗膜厚さに設定する必要が
あり、浴温80℃で塗料浴の固形分濃度は15%
以下、被処理材の引上げ速度も1m/分以下
の低膜厚になる条件が必要である。 For example, when using Toa Toa Paint Co., Ltd.'s TFS paint, Toatri Paint S8001 (AL-2), which is a chlorinated solvent type paint,
It is necessary to set the coating thickness to approximately 2 to 3 μm or less in areas other than the corners of the treated material, and the solid content concentration of the paint bath is 15% at a bath temperature of 80℃.
Below, conditions are required to achieve a low film thickness of 1 m/min or less for the pulling speed of the material to be treated.
他方、水溶性型塗料である神東塗料株式会
社製の電着塗装AL−200−50を用いた場合、
塗膜厚さの影響は少なく、約10μm以下の塗
膜厚さで充分使用可能であり、作業性をも加
味した適当な塗料浴の固形分濃度は、約20%
以下であつて、引上げ速度の影響も少なく、
使用する塗料の性質によりコーナー部分以外
の面の塗膜厚さが異なるが、本発明の方法で
は、後の陽極電解によりコーナー部分の脱色
が可能な程度の条件を設定すれば良い。 On the other hand, when using electrodeposition coating AL-200-50 manufactured by Shinto Paint Co., Ltd., which is a water-soluble type paint,
The effect of the coating film thickness is small, and it can be used sufficiently with a coating thickness of about 10 μm or less, and the solid content concentration of a suitable paint bath that takes workability into consideration is about 20%.
The effect of the pulling speed is also small.
Although the thickness of the coating film on surfaces other than the corner portions varies depending on the properties of the paint used, in the method of the present invention, conditions may be set to such an extent that the corner portions can be decolored by subsequent anodic electrolysis.
(ハ) このようにして塗料浴から引上げた被処理
材は、その表面から溶剤を揮発させ、塗料樹
脂を被処理材の表面に充分固定してから脱色
した方が良く、溶剤の揮発が遅いタイプの塗
料を用いる場合には加熱乾燥を施す方が良
い。しかしながら、使用する塗料浴が高温浴
の場合や常温でも揮発しやすい塗料浴を用い
る場合には、被処理材を浸漬浴から引上げる
と、溶剤は比較的速やかに揮発するので、別
段加熱乾燥処理を行なう必要がない。この場
合、溶剤がある程度揮発しないと、陽極処理
による脱色がコーナー部分以外に及ぶことが
ある。 (c) It is better to evaporate the solvent from the surface of the treated material that has been pulled out of the paint bath in this way and fully fix the paint resin on the surface of the treated material before decolorizing it, as this will slow down the volatilization of the solvent. When using this type of paint, it is better to heat dry it. However, if the paint bath used is a high-temperature bath or a paint bath that easily evaporates even at room temperature, the solvent will evaporate relatively quickly when the material to be treated is pulled out of the immersion bath, so separate heat drying treatment is required. There is no need to do this. In this case, unless the solvent evaporates to some extent, decolorization due to anodization may extend to areas other than the corner areas.
(ニ) また前記の塗膜固定に際し、加熱乾燥処理
が高温で行なわれることは好ましくなく、高
温乾燥を行なつて塗料を必要以上に硬化させ
てしまうと、次の陽極電解にいてコーナー部
分の脱色が困難になるため、塗料が本来の性
能を発揮する高温での乾燥は避けた方がよ
い。 (d) Also, when fixing the paint film, it is not preferable to perform heat drying treatment at high temperatures. It is best to avoid drying at high temperatures, where the paint performs best, as decolorization becomes difficult.
例えば、前述の電着塗料AL−200−50を
190℃の温度で乾燥した場合、塗膜厚さに関
係なく被処理材のコーナー部分は脱色不能と
なつた。この事から陽極電解処理による脱色
は、コーナー部分の塗膜厚さが薄いことの他
に、塗膜の硬化が不完全な条件下で電気的に
コーナー部分の塗膜を破壊することにより行
なわれるものと考えられる。 For example, use the electrocoating paint AL-200-50 mentioned above.
When dried at a temperature of 190°C, the corners of the treated material could not be bleached regardless of the coating thickness. For this reason, decolorization by anodic electrolytic treatment is performed by electrically destroying the coating film at the corner parts under conditions where the coating film is not completely cured, in addition to the thinness of the coating film at the corner parts. considered to be a thing.
(ホ) 実験の結果、次の陽極電解において被処理
材のコーナー部分だけを選択的に脱色するた
めには、コーナー部分の曲率半径は約5mmR
以下が好ましく、塗料の種類、塗膜の厚さ及
び乾燥等の処理条件によつては、限界の曲率
半径が更に小さくなる。被処理材のコーナー
部分の曲率半径が大きくなると、コーナー部
分と他の部分との膜厚分布の差が少ないの
で、被処理材の表面全体に脱色ムラが生じた
り、コーナー部分の脱色が困難になつたりす
る。 (e) As a result of the experiment, in order to selectively decolorize only the corner portion of the material to be treated in the next anodic electrolysis, the radius of curvature of the corner portion should be approximately 5 mmR.
The following is preferable, and depending on the type of paint, the thickness of the paint film, and processing conditions such as drying, the critical radius of curvature may become even smaller. When the radius of curvature of the corner part of the material to be treated becomes large, there is little difference in the film thickness distribution between the corner part and other parts, so uneven decoloring occurs over the entire surface of the material to be treated, and it becomes difficult to decolorize the corner part. I feel relaxed.
(3) 陽極電解による脱色処理
電解着色された陽極酸化皮膜を酸またはそれ
らの塩の水溶液で被処理材を陽極として電解を
行なうと、皮膜孔中に沈着していた金属又は金
属塩が電解液中に溶出して脱色される。けれど
も、本発明方法に於いては、電解着色(一次着
色)後の被処理材を陽極電解する際に、その前
工程で電気的抵抗の大きい塗装処理を行ない、
被処理材の表面にコーナー部分と他の部分とで
膜厚分布の違つた塗膜を形成してあるので、コ
ーナー部分以外の塗膜の厚い箇所は電解され
ず、塗料の付着が少ないコーナー部分の塗膜は
電気的に破壊されやすくなつているため、この
部分だけが集中的に電解され、その結果、被処
理材のコーナー部分のみが選択的に脱色される
ことになる。(3) Decolorization treatment by anodic electrolysis When the electrolytically colored anodic oxide film is electrolyzed with an aqueous solution of an acid or its salt using the material to be treated as the anode, the metal or metal salt deposited in the pores of the film is removed by the electrolytic solution. It is eluted and decolorized. However, in the method of the present invention, when the material to be treated after electrolytic coloring (primary coloring) is subjected to anodic electrolysis, a coating treatment with high electrical resistance is performed in the previous step,
Since a coating film with a different thickness distribution is formed on the surface of the material to be treated between corner areas and other areas, areas where the coating film is thick other than the corner areas are not electrolyzed, and the corner areas have less paint adhesion. Since the coating film is easily destroyed electrically, only this part is electrolyzed intensively, and as a result, only the corner parts of the material to be treated are selectively decolored.
尚、本工程での陽極電解処理に用いる電解浴
は特定されるものではなく、経済性が作業性等
の観点から適宜決定すればよいので、当初の陽
極酸化皮膜形成に供した電解浴または一次着色
に供した電解着色浴を利用することも可能であ
るが、アルカリ浴はアルマイトを溶解させやす
いため、酸もしくは塩を添加した酸性浴が良
い。 The electrolytic bath used for the anodic electrolytic treatment in this step is not specified and can be determined as appropriate from the viewpoint of economic efficiency and workability, so the electrolytic bath used for the initial anodic oxide film formation or the primary Although it is possible to use an electrolytic coloring bath that has been used for coloring, an alkaline bath easily dissolves alumite, so an acidic bath to which an acid or salt is added is preferable.
(4) 二次着色処理
前記の陽極電解によつてコーナー部分を脱色
した被処理材は、つぎに一次着色とは異なつた
色調が得られる着色手段により二次着色を施せ
ば、コーナー部分以外の箇所は一次着色の色調
を保ちつつコーナー部分だけ二次着色による別
種の色調に着色される。この場合、二次着色に
は一次着色と同じく電解着色法を用いてもよい
し、染色法等のように別種の着色法を使用する
ことも可能である。(4) Secondary coloring treatment The material to be treated whose corner portions have been decolored by the above-mentioned anodic electrolysis is then subjected to secondary coloring using a coloring method that provides a color tone different from the primary coloring. While maintaining the color tone of the primary coloring, only the corners are colored in a different tone by secondary coloring. In this case, the electrolytic coloring method may be used for the secondary coloring as in the primary coloring, or it is also possible to use a different coloring method such as a dyeing method.
(5) 上記のようにして、コーナー部分と他の部分
とで色調の異なる模様着色皮膜を形成した後、
その表面に再び浸漬法あるいはスプレー法等に
よる保護塗装処理を施し、更に焼付乾燥処理を
行なえば、耐食性に優れ且つ美麗な多色の模様
着色皮膜が得られる。(5) After forming a patterned colored film with different tones between the corner part and other parts as described above,
If the surface is again subjected to a protective coating treatment using a dipping method or a spraying method, and then a baking drying treatment, a multicolored patterned coating with excellent corrosion resistance and beautiful appearance can be obtained.
以下、本発明による模様着色処理方法の具体的
な実施例を次に掲げるが、本発明は必ずしもこれ
らの各実施例のみに拘束されるものではない。 Specific examples of the pattern coloring method according to the present invention are listed below, but the present invention is not necessarily limited to these examples.
実施例 1
一辺が40mmの方形でコーナー部分の曲率半径
0.4mmRの断面形を有する6063S―T5のアルミニ
ウム押出形材を長さ200mmに切断し、通常の前処
理を行なつた後、硫酸150g/l、アルミニウム
イオン10g/l、浴温20℃の浴中にて電流密度
1.2A/dm2で30分間の陽極酸化処理を行ない、
アルミニウム形材の表面に約10μmの陽極酸化皮
膜を形成し、硫酸ニツケル50g/l、ホウ酸
40g/l、浴温30℃で陽極をニツケル板として
0.5A/dm2、30秒間の直流陰極電解を行なつて
均一なブロンズ色の着色を得た。Example 1 The radius of curvature of the corner of a rectangle with one side of 40 mm
A 6063S-T5 aluminum extrusion shape with a cross section of 0.4 mmR was cut to a length of 200 mm, and after normal pretreatment, it was placed in a bath containing 150 g/l of sulfuric acid, 10 g/l of aluminum ions, and a bath temperature of 20°C. Current density inside
Perform anodizing treatment at 1.2A/ dm2 for 30 minutes,
An anodic oxide film of approximately 10μm is formed on the surface of the aluminum profile, and 50g/l of nickel sulfate and boric acid are applied.
40g/l, bath temperature 30℃, using nickel plate as anode
Direct current cathodic electrolysis was carried out at 0.5 A/dm 2 for 30 seconds to obtain a uniform bronze coloration.
次に前記着色形材を神東塗料(株)のAL―200―50
の樹脂分15%水溶液に浸漬し、0.6m/分の引上
げ速度で形材を引上げて、80℃の温度で5分間の
乾燥を行なつた。そして、この形材を硫酸
150g/l、浴温20℃の浴中で電圧15V、3分間の
陽極電解処理を行なつたところ、各々のコーナー
部分においてブロンズ色は脱色されたが、コーナ
ー部分以外の箇所はブロンズ色のまゝであつた。
なお前記脱色処理後に於いて、コーナー部分以外
の塗膜厚さは約7μmであつた。 Next, the colored shape was coated with AL-200-50 from Shinto Paint Co., Ltd.
The shape was immersed in a 15% aqueous solution of resin, pulled up at a pulling speed of 0.6 m/min, and dried at a temperature of 80°C for 5 minutes. This shape was then heated using sulfuric acid.
When anodic electrolytic treatment was performed for 3 minutes at a voltage of 15 V in a bath containing 150 g/l and a bath temperature of 20°C, the bronze color was bleached at each corner, but the bronze color remained in areas other than the corner areas. It was hot.
After the decolorization treatment, the thickness of the coating film other than the corner portions was approximately 7 μm.
このコーナー部分が脱色された形材を二酸化セ
レン15g/l、硫酸銅0.6g/l、硫酸亜鉛0.3g/
l、浴温20℃の浴中でカーボンを陽極として、電
圧13V、3分間の直流陰極電解を行なつたとこ
ろ、コーナー部分はゴールド色に着色され、コー
ナー部分以外がブロンズ色の模様着色皮膜を得
た。 The shape with its corner parts bleached is made of selenium dioxide 15g/l, copper sulfate 0.6g/l, zinc sulfate 0.3g/l,
l. When DC cathode electrolysis was performed at a voltage of 13 V for 3 minutes using carbon as an anode in a bath at a bath temperature of 20°C, the corners were colored gold, and the areas other than the corners had a bronze-colored patterned colored film. Obtained.
実施例 2
実施例1と同一の形状寸法を有するアルミニウ
ム押出形材(6063S―T5)に、実施例1と同様の
陽極酸化皮膜処理及び電解着色処理(一次着色)
を施し、次に東亜ペイント(株)製のTFS塗料トア
トリペイントS8001(AL−2)、浴温80℃固形分
濃度12%の塗料浴を用いて、0.5m/分の引上げ
速度により塗装を施した後、陽極酸化皮膜の形成
に用いた電解浴で電圧15V、5分間の陽極電解処
理を行なつたところ、コーナー部分だけが脱色さ
れ、その他の部分はブロンズ色のまゝであつた。
(コーナー部分以外の塗膜厚は約1μm)
前記脱色処理後の形材を実施例1と同様の二酸
化セレン浴で電圧12V、3分間の陰極電解着色処
理理(二次着色)を行なつたところ、コーナー部
分はゴールド色に着色された。Example 2 An extruded aluminum material (6063S-T5) having the same shape and dimensions as Example 1 was subjected to the same anodic oxidation coating treatment and electrolytic coloring treatment (primary coloring) as in Example 1.
Then, painting was applied at a pulling speed of 0.5 m/min using the TFS paint Toatri Paint S8001 (AL-2) manufactured by Toa Paint Co., Ltd. and a paint bath with a bath temperature of 80°C and a solid content concentration of 12%. After that, anodic electrolysis treatment was performed for 5 minutes at a voltage of 15 V in the electrolytic bath used to form the anodic oxide film, and only the corner portions were decolored, while the other portions remained bronze-colored.
(The thickness of the coating film other than the corner portions was approximately 1 μm.) The shape after the decolorization treatment was subjected to a cathodic electrolytic coloring treatment (secondary coloring) at a voltage of 12 V for 3 minutes in the same selenium dioxide bath as in Example 1. However, the corners were colored gold.
実施例 3
一辺が50mmの方形でコーナー部分の曲率半径が
0.5mmRの断面形を有する6063S―T5のアルミニ
ウム押出形材を長さ200mmに切断し、通常の前処
理を行なつた後、硫酸150g/l、アルミニウム
イオン10g/l、浴温20℃の電解浴にて電流密度
1.2A/dm2、30分間の陽極酸化処理を行ない、
更に硫酸ニツケル50g/l、ホウ酸40g/lの浴
で電流密度0.5A/dm2、15秒間の陰極電解処理
を行なつて被処理材の表面に淡ブロンズ色の均一
な着色皮膜を得た。Example 3 A rectangle with one side of 50 mm and a corner radius of curvature
A 6063S-T5 aluminum extrusion with a cross-sectional shape of 0.5 mmR was cut into lengths of 200 mm, and after normal pretreatment, electrolysis was carried out at 150 g/l of sulfuric acid, 10 g/l of aluminum ions, and a bath temperature of 20°C. Current density in bath
1.2A/dm 2 , anodizing for 30 minutes,
Further, cathodic electrolysis treatment was performed in a bath containing 50 g/l of nickel sulfate and 40 g/l of boric acid at a current density of 0.5 A/dm 2 for 15 seconds to obtain a uniform colored film of light bronze color on the surface of the treated material. .
次にこの着色形材を神東塗料(株)製の溶剤型塗料
ポリンALクリヤUNを樹脂分5%に希釈した定
温の塗料浴にて0.6m/分の引上げ速度で塗装を
施し、温度60℃で5分間の乾燥処理を行なつた
後、当初の陽極酸化皮膜形成に用いた硫酸浴で電
圧15V、5分間の陽極電解処理を行なつたとこ
ろ、各コーナー部分は脱色されたが、他の各面は
淡ブロンズ色のまゝであつた。 Next, this colored shape was painted at a drawing speed of 0.6 m/min in a constant temperature paint bath containing the solvent-based paint Porin AL Clear UN manufactured by Shinto Toyo Co., Ltd. diluted to a resin content of 5%. After drying at ℃ for 5 minutes, anodic electrolysis was performed at a voltage of 15 V for 5 minutes in the same sulfuric acid bath used to form the anodic oxide film, and each corner was bleached, but the others were Each side remained pale bronze in color.
この部分を脱色した形材を硫酸スズ5g/l、
硫酸7g/l、浴温20℃の電解着色浴で対極をカ
ーボンとして電圧12V、3分間の交流電解を行な
つたところ、脱色されていたコーナー部分は褐色
に着色した。 The shape with this part bleached was treated with tin sulfate 5g/l.
When alternating current electrolysis was carried out for 3 minutes at a voltage of 12 V with carbon as the counter electrode in an electrolytic coloring bath containing 7 g/l of sulfuric acid and a bath temperature of 20°C, the decolored corners were colored brown.
実施例 4
一辺が75mmの方形でコーナー部分の曲率半径が
1mmRの断面形を有する6063S―T5のアルミウム
押出形材を長さ200mmに切断し、通常の前処理を
行なつた後、硫酸150g/l、アルミニウムイオ
ン10g/l、浴温20℃の電解浴にて電流密度
1.2A/dm2、30分間の陽極酸化処理を行ない、
更に硫酸スズ5g/l、硫酸7g/l、浴温20℃の
電解浴で対極をカーボンとして電圧12V、2分間
の交流電解を行なつて褐色の着色皮膜を得た。Example 4 A 6063S-T5 aluminum extrusion having a cross-sectional shape of a rectangle with a side of 75 mm and a corner radius of curvature of 1 mmR was cut to a length of 200 mm, and after normal pretreatment, 150 g of sulfuric acid/ l, aluminum ion 10g/l, current density in an electrolytic bath with a bath temperature of 20°C
1.2A/dm 2 , anodizing for 30 minutes,
Further, alternating current electrolysis was carried out for 2 minutes at a voltage of 12 V using carbon as a counter electrode in an electrolytic bath containing 5 g/l of tin sulfate and 7 g/l of sulfuric acid at a bath temperature of 20° C. to obtain a brown colored film.
次にこの着色形材を実施例1で用いた塗料の7
%水溶液、常温浴にて引上げ速度1.5m/分の条
件で塗料を付着させ、温度80℃、5分間の乾燥処
理を行なつた後、硫酸100g/l、浴温20℃の浴
で電圧18V、3分間の陽極電解処理を行なつたと
ころ、各コーナー部分は脱色されたが、コーナー
部分以外は褐色のまゝであつた。(塗膜厚約2μm)
このコーナー部分を脱色された形材を硫酸銅
10g/l、硫酸20g/l、浴温20℃の電解浴で対
極を銅板として電圧12V、2分間の交流電解処理
を行なつたところ、コーナー部分は赤褐色に着色
された。 Next, apply this colored shape to the coating material used in Example 1.
% aqueous solution in a normal temperature bath at a pulling speed of 1.5 m/min, and after drying for 5 minutes at a temperature of 80°C, apply a voltage of 18 V in a bath containing 100 g/l of sulfuric acid and a bath temperature of 20°C. When anodic electrolysis treatment was carried out for 3 minutes, each corner part was bleached, but the parts other than the corner parts remained brown. (Coating film thickness approx. 2μm) The shape with this corner part bleached is coated with copper sulfate.
When AC electrolytic treatment was carried out for 2 minutes at a voltage of 12 V using a copper plate as a counter electrode in an electrolytic bath containing 10 g/l of sulfuric acid and 20 g/l of sulfuric acid at a bath temperature of 20°C, the corner portions were colored reddish brown.
実施例 5
実施例3と同一の形状寸法を有するアルミニウ
ム押出形材(6063S―T5)に、実施例1と同じ条
件で前処理、陽極酸化後、電解着色を施して浸漬
法による塗料付着を行なつた後、温度60℃で5分
間の乾燥処理を施し、次に蓚酸50g/lの常温浴
中で電圧15V、3分間の陽極電解処理を行なつて
コーナー部分を脱色した後、蓚酸第二鉄アンモニ
ウム5g/l、浴温50℃の染色浴で10分間の浸漬
処理を行なつたところ、被処理材の表面にコーナ
ー部分が黄色、コーナー部分以外の箇所がブロン
ズ色をした模様着色皮膜を得た。Example 5 An extruded aluminum material (6063S-T5) having the same shape and dimensions as Example 3 was pretreated under the same conditions as Example 1, anodized, electrolytically colored, and then coated with paint by dipping. After drying at a temperature of 60°C for 5 minutes, the corners were decolorized by anodic electrolysis treatment at a voltage of 15V for 3 minutes in a room-temperature bath containing 50g/l of oxalic acid. When immersed for 10 minutes in a dyeing bath containing iron ammonium 5g/l and a bath temperature of 50°C, a patterned colored film was formed on the surface of the treated material with yellow corners and bronze colored areas other than the corners. Obtained.
以上のように、本発明の方法によれば、陽極酸
化皮膜形成後のアルミニウムに模様着色を施す場
合、前後二回の着色工程の間に、簡単な浸漬によ
る塗装処理と酸性溶液中での陽極電解による脱色
処理の両工程を介在させる独自の表面処理方法に
よつて、従来法のように着色塗料を用いずに、被
処理材の表面にコーナー部分と他の部分とで色調
の異なる模様着色皮膜を得ることが出来、従つ
て、これを室内建具用のアルミニウム押出形材を
はじめ、各種アルミニウム材料の表面処理加工に
適用すれば、現有の設備を利用して簡単に多色の
模様着色を実現することが可能になり、その生産
性が高く、然かも耐食性に優れ且つ美麗な模様着
色皮膜が得られる事とも相俟つて、斯業の発展に
大きな貢献を果すものである。 As described above, according to the method of the present invention, when applying pattern coloring to aluminum after an anodic oxide film is formed, between the two coloring steps, a simple immersion painting process and an anodizing process in an acidic solution are performed. By using a unique surface treatment method that involves both electrolytic decolorization processes, the surface of the treated material is colored in a pattern with different tones between corners and other areas, without using colored paint as in conventional methods. It is possible to obtain a film, and if this film is applied to the surface treatment of various aluminum materials, including aluminum extrusion shapes for interior fittings, it is possible to easily color multi-colored patterns using existing equipment. It has become possible to realize this method, has high productivity, has excellent corrosion resistance, and can provide a beautiful colored film with a beautiful pattern, making a great contribution to the development of this industry.
Claims (1)
被処理材に陽極酸化皮膜を形成し、電解着色によ
る一次着色を施した後、浸漬による透明合成樹脂
塗装を行なつて被処理材の表面にコーナー部分と
他の部分とで膜厚分布の違つた塗膜を形成せし
め、次にこの被処理材を酸性溶液中で陽極電解し
て当該被処理材のコーナー部分のみを選択的に脱
色し、その後、一次着色で得られた色調と異なつ
た色調が得られる電解着色あるいは染色による二
次着色を施して被処理材のコーナー部分だけを着
色し、被処理材の表面にコーナー部分と他の部分
とで色調の異なる模様着色皮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模様
着色処理方法。1 After forming an anodized film on the material to be treated made of aluminum or aluminum alloy and applying primary coloring by electrolytic coloring, a transparent synthetic resin coating is applied by dipping to the surface of the material to be treated, and the corners and other parts are colored. A coating film with a different film thickness distribution is formed using the above methods, and then this treated material is subjected to anodic electrolysis in an acidic solution to selectively decolorize only the corners of the treated material, and then the color obtained by primary coloring is applied. Electrolytic coloring or secondary coloring by dyeing that produces a color tone different from the original color is applied to color only the corner parts of the treated material, and the surface of the treated material has a pattern in which the color tone differs between the corner part and other parts. A method for pattern-coloring aluminum or aluminum alloy, the method comprising obtaining a colored film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9283081A JPS57207198A (en) | 1981-06-16 | 1981-06-16 | Treatment for patterned coloring of aluminum or aluminum alloy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9283081A JPS57207198A (en) | 1981-06-16 | 1981-06-16 | Treatment for patterned coloring of aluminum or aluminum alloy |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57207198A JPS57207198A (en) | 1982-12-18 |
| JPS6360119B2 true JPS6360119B2 (en) | 1988-11-22 |
Family
ID=14065345
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9283081A Granted JPS57207198A (en) | 1981-06-16 | 1981-06-16 | Treatment for patterned coloring of aluminum or aluminum alloy |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57207198A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5816099A (en) * | 1981-07-22 | 1983-01-29 | Tateyama Alum Kogyo Kk | Patternwise coloring method for aluminum or aluminum alloy |
-
1981
- 1981-06-16 JP JP9283081A patent/JPS57207198A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57207198A (en) | 1982-12-18 |
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