JPH03229895A - Aluminum alloy sheet to be coated for can lid and its production - Google Patents
Aluminum alloy sheet to be coated for can lid and its productionInfo
- Publication number
- JPH03229895A JPH03229895A JP2255790A JP2255790A JPH03229895A JP H03229895 A JPH03229895 A JP H03229895A JP 2255790 A JP2255790 A JP 2255790A JP 2255790 A JP2255790 A JP 2255790A JP H03229895 A JPH03229895 A JP H03229895A
- Authority
- JP
- Japan
- Prior art keywords
- aluminum alloy
- treatment
- adhesion
- oxide film
- 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.)
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- Application Of Or Painting With Fluid Materials (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は街着用アルミニウム合金塗装用根にかかり、特
に優れた耐フェザリング性を要求される缶蓋用アルミニ
ウム合金塗装用板に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an aluminum alloy coating board for can lids, which is applied to aluminum alloy coatings for street use and requires particularly excellent feathering resistance. .
[従来の技術]
従来から、缶蓋用材料としてはAl2−Mg系のJIS
5052.5(182,5182等のアルミニウム合金
板が使用され、缶の内容物の風味の保持や蓋材の腐食を
防止するために塗装が施されている。[Prior Art] Conventionally, Al2-Mg based JIS materials have been used as materials for can lids.
Aluminum alloy plates such as 5052.5 (182 and 5182) are used, and are painted to preserve the flavor of the contents of the can and to prevent corrosion of the lid.
そして、係る塗装においては、先ず所定のアルミニウム
合金板に脱脂、エツチング処理が施され、ついでリン酸
クロメート処理が実施された後に塩化ビニルオルガノゾ
ル系、エポキシ尿素系又はエポキシフェノール系等の樹
脂塗料により塗装し、そしてその焼付が行なわれている
。In such painting, a predetermined aluminum alloy plate is first degreased and etched, then subjected to phosphoric acid chromate treatment, and then coated with a resin paint such as vinyl chloride organosol, epoxy urea, or epoxy phenol. It is painted and then baked.
ところで、このようにして形成される塗膜の密着性が不
充分であると、開蓋時に開口部にフェザリングと呼ばれ
る蓋内面側塗膜の膜残りが発生するといった問題がある
。この現象はより腐食性の強い内容物番こ対応するため
に塩化ビニルオルガノゾル系塗料を]0g7m”以Fと
厚膜にする場合に発生し易く大きな問題となってきた。By the way, if the adhesion of the coating film formed in this way is insufficient, there is a problem in that when the lid is opened, the coating film on the inner surface of the lid remains at the opening, which is called feathering. This phenomenon tends to occur when a vinyl chloride organosol paint is made into a thick film of 0g7m'' or more in order to cope with more corrosive contents, and has become a serious problem.
このことは、より腐食性の強い内容物、例えば塩分が多
い収容物に対応するために、その塗膜重量を上げようと
すると顕在化し、大きな問題となっていたのであり、そ
れゆえに係るフェザリングに対する対策は1本アルミニ
ウム塗装材の分野において大きな技術的課題とされてい
るのであるが、このフェザリングに対する解決策として
、塗膜とアルミニウム合金板の密着性を向上することに
より防止できることが知られていた。This became a major problem when trying to increase the weight of the coating to deal with more corrosive contents, such as contents containing a lot of salt, and this was a major problem. Countermeasures against feathering are considered to be a major technical issue in the field of aluminum coating materials, but it is known that this feathering can be prevented by improving the adhesion between the coating film and the aluminum alloy plate. was.
フェザリング防止の対策としては、例えば特開平1−2
30787号に開示された技術においては、リン酸クロ
メート処理液組成の調整及びアルミニウム合金板の20
〜50℃加熱処理を行って烹着性向上を計っている。し
かし、液組成の厳しい管理は困難であり、フェザリング
の発生は温度の高い夏場に製造した場合にも起きるため
、低温加熱が充分に有効であるとは考えにくい。As a measure to prevent feathering, for example, Japanese Patent Application Laid-Open No. 1-2
In the technique disclosed in No. 30787, the composition of the phosphoric acid chromate treatment solution is adjusted and the
Heat treatment at ~50°C is performed to improve adhesion. However, it is difficult to strictly control the liquid composition, and feathering occurs even when manufactured in the hot summer months, so it is difficult to imagine that low-temperature heating is sufficiently effective.
特開昭6−4−79400号に開示された技術ではリン
酸クロメート処理の代わりにリン酸陽極酸化処理を行っ
て密着性の向上を計っている。しかし、リン酸は導電用
金属材料、構造用鋼材に対して非常に強い腐食性がある
。また、短時間で処理するために高電流密度で陽極酸化
を行なうためには100V以上の高電圧が必要となるた
め、工業化が困難なものとなっている。In the technique disclosed in JP-A-6-4-79400, phosphoric acid anodic oxidation treatment is performed instead of phosphoric acid chromate treatment to improve adhesion. However, phosphoric acid is highly corrosive to conductive metal materials and structural steel materials. Further, in order to carry out anodic oxidation at a high current density in order to perform the process in a short time, a high voltage of 100 V or more is required, making it difficult to commercialize the process.
[発明が解決しようとする課題]
従来のアルミニウム板に対する下地処理法として最も広
く採用されでいるリン酸クロメート処理は密着性の向上
に効果が認められるが、脱脂槽、エツチング処理槽及び
化成処理槽などの多数の処理槽を必要とするため、製造
ラインが長大となって設備コストも大きくなるという問
題があった。[Problems to be Solved by the Invention] Phosphoric acid chromate treatment, which is the most widely used base treatment method for conventional aluminum plates, is effective in improving adhesion, but it is difficult to use in degreasing baths, etching treatment baths, and chemical conversion treatment baths. Since a large number of processing tanks are required, the production line becomes long and the equipment cost increases.
また数種類の処理液を別個に制御しなければならないた
め、品質が不安定となり易く、安定して密着性を向上さ
せ得ないことが多かった。Furthermore, since several types of treatment liquids must be controlled separately, the quality tends to be unstable, and it is often not possible to stably improve adhesion.
特に一番大きな問題は缶蓋用材として塗膜とアルミニウ
ム合金板の密着性が不充分である声、にある。The biggest problem in particular is that there are complaints that the adhesion between the paint film and the aluminum alloy plate used as a material for can lids is insufficient.
また、リン酸、硫酸等の酸性水溶液による電解酸化のみ
では脱脂力が劣るため、別に脱脂工程を設ける必要があ
り、そのうえ電解時に酸化皮膜のバリヤー層が厚く生成
し易いので短時間で処理するために高電流密度にて電解
するには非常に高い直流電解電圧を必要とする問題点が
ある。更に導電用金属材料、構造鋼材に対する強い腐食
性を持つ等の基本的な問題を有している。In addition, electrolytic oxidation using an acidic aqueous solution such as phosphoric acid or sulfuric acid alone has poor degreasing power, so a separate degreasing process is required.Furthermore, a thick barrier layer of oxide film tends to form during electrolysis, so it is necessary to process in a short time. However, there is a problem in that a very high DC electrolysis voltage is required for electrolysis at high current density. Furthermore, it has fundamental problems such as being highly corrosive to conductive metal materials and structural steel materials.
この発明は以上の問題を有効に解決して、塗膜とアルミ
ニウム合金板の密着性を安定して確保でき、しかも処理
に長時間を要さず、また設備的にも低コストで済む缶蓋
用アルミニウム合金板及びその製造方法を提供すること
を目的とするものである。This invention effectively solves the above-mentioned problems, and can stably ensure adhesion between the coating film and the aluminum alloy plate, and can lids that do not require long processing times and are inexpensive in terms of equipment. The object of the present invention is to provide an aluminum alloy plate for use in aluminum alloys and a method for manufacturing the same.
[課題を解決するための手段]
本発明はアルミニウム合金板を、アルカリ性水溶液中に
て交流電解処理を施して膜厚500〜5000人の酸化
皮膜を形成させたことを特徴とする塗膜密着性に優れた
缶蓋用アルミニウム合金塗装用板を提供することにある
。[Means for Solving the Problems] The present invention is characterized in that an aluminum alloy plate is subjected to AC electrolysis treatment in an alkaline aqueous solution to form an oxide film with a thickness of 500 to 5,000. To provide an aluminum alloy coating plate for can lids which is excellent in quality.
さらに該塗膜密着性に優れた缶蓋用アルミニウム合金塗
装用板は、アルミニウム合金板を、アルカリ性水溶液中
、電流密度4〜50A/dm2にて電気量が80 c
/ d m ”を越えることとなる時間、交流電解処理
を行なうことを特徴とする塗膜密着性の優れた缶蓋用ア
ルミニウム合金塗装用板の製造方法により得ることがで
き、本発明の課題である耐フェザリング性の優れた缶蓋
用アルミニウム合金塗装用板の製造のみならず、短時間
の処理で済み、且つ低コストですむ製造方法を提供する
ものである。Furthermore, the aluminum alloy coating plate for can lids with excellent coating film adhesion can be coated with an aluminum alloy plate having an electrical charge of 80 c at a current density of 4 to 50 A/dm2 in an alkaline aqueous solution.
/ d m'', which can be obtained by a method for manufacturing an aluminum alloy coating plate for can lids with excellent coating film adhesion, which is characterized by performing AC electrolytic treatment for a time exceeding The object of the present invention is not only to manufacture an aluminum alloy coating plate for can lids with excellent feathering resistance, but also to provide a manufacturing method that requires only a short processing time and at low cost.
本発明においてアルカリ性水溶液中で交流電解処理によ
り得られる酸化皮膜は500人〜5000人の膜厚にお
いて形成せしめられ、これによってそのうえに塗布され
るビニル系塗料の塗膜の密着性が著しく改善され得るの
である。なお、かかる酸化皮膜の膜厚が500人よりも
薄くなると、緻密なバリヤー層上に成長する多孔性酸化
皮膜の厚さが不充分であるため、そのうえに形成される
塗膜の密着性が充分でなくなることは言うまでもないと
ころである。In the present invention, the oxide film obtained by alternating current electrolytic treatment in an alkaline aqueous solution is formed to a thickness of 500 to 5,000 coats, which can significantly improve the adhesion of the vinyl paint film applied thereon. be. If the thickness of the oxide film becomes thinner than 500, the thickness of the porous oxide film grown on the dense barrier layer will be insufficient, and the adhesion of the coating film formed thereon will not be sufficient. Needless to say, it will disappear.
一方、酸化皮膜の厚さの上限である5000人は、厚く
なることにより本発明の効果は享受でき、障害は特にな
いが、通常の条件で得られる厚さの上限としてこの程度
が限界であり、これ以上厚くしても特にメリットはない
と考えられるものである。On the other hand, the upper limit of the thickness of the oxide film is 5,000 people, and although the effects of the present invention can be enjoyed by increasing the thickness and there are no particular problems, this is the upper limit of the thickness that can be obtained under normal conditions. , it is thought that there is no particular advantage in making it thicker than this.
本発明に使用するアルカリ水溶液としては、特に制限が
ないようであり、通常はビロリン酸ナトJウム、炭酸ナ
トリウム、炭酸カリウム、水酸化ナトリウム、水酸化カ
リウム、リン酸ナトリウム等の水溶液、もしくはそれら
の2種以上の混合溶液を用いることが望ましく、また脱
脂性を向上させるために表面活性剤を含んでいてもよい
。There seems to be no particular restriction on the alkaline aqueous solution used in the present invention, and it is usually an aqueous solution of sodium birophosphate, sodium carbonate, potassium carbonate, sodium hydroxide, potassium hydroxide, sodium phosphate, etc., or aqueous solutions thereof. It is desirable to use a mixed solution of two or more types, and a surfactant may be included in order to improve the degreasing property.
また、その電解液の望ましい水素イオン指数(pH)は
9〜13.5、好ましくはpHto〜12である。Further, the desirable hydrogen ion index (pH) of the electrolytic solution is 9 to 13.5, preferably pHto to 12.
pH9未満では脱脂性が劣り、アルミニウム合金板表面
の圧延油、酸化皮膜の溶解除去ができない。また浴電圧
が上昇して不均一な電解が生じ易いから好ましくなく、
一方pH13,5を越えれば溶解性が強すぎて生成する
忍解残渣の気泡による除去が不充分なだけでなく、密着
性に優れた多孔性酸化皮膜が形成されなくなるので避け
るべきである。If the pH is less than 9, the degreasing property is poor and rolling oil and oxide film on the surface of the aluminum alloy plate cannot be dissolved and removed. It is also undesirable because the bath voltage increases and non-uniform electrolysis tends to occur.
On the other hand, if the pH exceeds 13.5, the solubility is too strong, and the removal of the generated oxidation residue by bubbles is insufficient, and a porous oxide film with excellent adhesion is not formed, so it should be avoided.
電解処理の際のアルカリ性溶液の浴温は、通常は40〜
90℃の範囲内である。40℃未満の低温では脱脂・洗
浄効果が不充分になり易く、一方90℃を越えれば溶解
性が強すぎて必要な厚みの陽極酸化皮膜が得られ難くな
る。なお、40〜90℃の範囲内でも、特に60〜80
℃の範囲内が好ましい。The bath temperature of the alkaline solution during electrolytic treatment is usually 40~
It is within the range of 90°C. At low temperatures below 40°C, the degreasing and cleaning effects tend to be insufficient, while at temperatures above 90°C, the solubility is too strong and it becomes difficult to obtain an anodic oxide film of the required thickness. In addition, even within the range of 40 to 90°C, especially 60 to 80°C
It is preferably within the range of °C.
交流電解時の電流密度両極性においては4〜50 A
/ d m ”、好ましくは5〜30 A / d m
”である。3 A / d m ”未満では電解時発
生する気泡の量が不充分で表面の清浄化効果が劣り、密
着性に優れた多孔性酸化皮膜の生成が不充分であるので
好ましくない。The current density during AC electrolysis is 4 to 50 A in both polarities.
/dm”, preferably 5-30 A/dm
If it is less than 3 A/d m, the amount of bubbles generated during electrolysis is insufficient, the surface cleaning effect is poor, and the formation of a porous oxide film with excellent adhesion is insufficient, so it is not preferable. .
50 A / d m 2を越えると電解電圧が高くな
りすぎ、漏電を起こし易くなるだけでなく1反応熱によ
るし焼け」等の外観ムラが発生し易いので好ましくない
。If it exceeds 50 A/dm2, the electrolytic voltage becomes too high, which is not preferable because it not only tends to cause electrical leakage but also tends to cause uneven appearance such as "burning" due to the heat of one reaction.
交流電解は総電気量が80 c / d m 2を越え
ることとなる時間性なう必要がある。総電気量が80
c / d m 2以下であると多孔性酸化皮膜が所定
の厚さまで生成しないので、そのうえに形成される塗膜
との密着性が充分でない。電流密度が高いほど短時間に
て充分な塗膜密着性を得ることができるが、電圧が高く
なるため大型電源が必要となる。極性は交流波形でなけ
ればならない。The alternating current electrolysis must be of a temporal nature such that the total amount of electricity exceeds 80 c/dm 2 . Total electricity amount is 80
If it is less than c/d m 2 , a porous oxide film will not be formed to a predetermined thickness, and the adhesion to the coating film formed thereon will not be sufficient. The higher the current density, the more sufficient coating film adhesion can be obtained in a shorter time, but the higher the voltage, the greater the need for a large power source. The polarity must be an AC waveform.
1作 用」
この発明では、40〜90℃という高温のアルカリ性溶
液中で交流を用いて電解処理を行なう。1. In this invention, electrolytic treatment is performed using alternating current in an alkaline solution at a high temperature of 40 to 90°C.
このような電解処理によって、以下に詳細に述べるよう
にアルミニウム板の表面が強力に脱脂・洗浄されると同
時に、塗膜密着性が優れた陽極酸化皮膜が生成される。By such electrolytic treatment, as described in detail below, the surface of the aluminum plate is strongly degreased and cleaned, and at the same time, an anodic oxide film with excellent coating film adhesion is generated.
すなわち、先ず脱脂・洗浄作用について述べれば、アル
カリ性溶液はそれ自体で脱脂性を有しているに加え、高
温であるため、脱脂性はより強力となっている。しかも
交流による電解では、アノード反応時には酸素ガスが発
生する一方、カソード反応時には水素ガスが発生するか
ら、アノード反応時には板表面に付着している有機物の
酸化による脱脂・洗浄作用が働き、カソード反応時には
板表面での水素気泡の膨張による機械的洗浄作用が働く
。したがって、高温のアルカリ性溶液中での交流電解処
理によれば、上述の各作用が相乗的に機能して、強力な
脱脂・洗浄効果が発揮され、極めて短時間で、塗膜密着
性に悪影響を与えるアルミニウム合金板表面の圧延油、
塊状に生成した熱酸化皮膜を完全に除去すると同時に、
清浄な表面を持つ膜厚500〜5000人の塗膜密着性
の優れた多孔性酸化皮膜を形成するものである。That is, first of all, speaking of the degreasing and cleaning effects, the alkaline solution has degreasing properties by itself, and because of the high temperature, the degreasing properties are stronger. Moreover, in electrolysis using alternating current, oxygen gas is generated during the anode reaction, while hydrogen gas is generated during the cathode reaction. Therefore, during the anode reaction, degreasing and cleaning effects occur due to the oxidation of organic matter attached to the plate surface, and during the cathode reaction, the degreasing and cleaning effects are activated. A mechanical cleaning action occurs due to the expansion of hydrogen bubbles on the plate surface. Therefore, when AC electrolytic treatment is performed in a high-temperature alkaline solution, the above-mentioned effects function synergistically to produce a strong degreasing and cleaning effect, and in an extremely short period of time, there is no adverse effect on paint film adhesion. Rolling oil on the aluminum alloy plate surface, giving
At the same time as completely removing the thermal oxide film that has formed in lumps,
It forms a porous oxide film with a clean surface, a film thickness of 500 to 5,000 people, and excellent film adhesion.
更に、交流による電解処理を行なっているため、肌荒れ
が生じにくく、肌荒れを招かずに短時間で大電気量の電
流を与えることができ、そのため処理時間を著しく短縮
して作業性を向上させることかできる。Furthermore, because electrolytic treatment is performed using alternating current, it is difficult to cause skin roughness, and a large amount of current can be applied in a short period of time without causing skin roughness, which significantly shortens treatment time and improves workability. I can do it.
すなわち、従来の一般的な直流電流による電−解処理で
は、短時間で大電気量の電流を与えれば(したがって、
高電流密度で電解すれば)、浴電圧が急激に上昇し易く
、そのため不均一の電解が生じ易いが、交流波形による
電解ではこのようなことがなく、肌荒れを招かずに短時
間で大電気量の電解、したがって高電流密度での電解を
行ない、密着性の優れた皮膜な効率よく生成させること
ができるのである。In other words, in conventional general electrolytic treatment using direct current, if a large amount of current is applied in a short period of time (therefore,
If electrolysis is carried out at a high current density), the bath voltage tends to rise rapidly, which tends to cause non-uniform electrolysis, but this does not occur with electrolysis using an AC waveform, and large amounts of electricity can be generated in a short time without causing skin irritation. By electrolyzing at a high current density, it is possible to efficiently produce a film with excellent adhesion.
さらに、この発明では前述のように脱脂・洗浄と密着性
に優れた陽極酸化皮膜の生成とを同一槽内での同一処理
によって行なっているため、脱脂後の別の槽で陽極酸化
させる場合と異なり、工程間で汚れが付着せず、板表面
が活性化されたままで陽極酸化皮膜が生成されるから、
均一な品質の皮膜が得られ、安定して優れた密着性を発
揮させることができる。Furthermore, in this invention, as described above, degreasing/cleaning and formation of an anodic oxide film with excellent adhesion are performed in the same process in the same tank, so it is possible to perform anodization in a separate tank after degreasing. Unlike this, dirt does not adhere during the process, and an anodic oxide film is generated while the board surface remains activated.
A film of uniform quality can be obtained, and it can exhibit stable and excellent adhesion.
このため、このようにしてできた陽極酸化皮膜は塗膜と
の密着性が従来法による酸化皮膜と比べて格段に向上し
たものと考えている。For this reason, it is believed that the anodic oxide film formed in this manner has significantly improved adhesion to the paint film compared to the oxide film formed by the conventional method.
そしてまた、脱脂・洗浄と陽極酸化皮膜の生成とが同一
槽内での同一の電解処理によって行なわれ、しかもその
電解時間も短いため、従来よりも全体としての作業時間
が著しく短縮され、生産性が向上すると共に、設備コス
トも著しく安価となる。Furthermore, since degreasing/cleaning and the formation of an anodized film are performed in the same electrolytic treatment in the same tank, and the electrolytic time is short, the overall working time is significantly shortened compared to conventional methods, and productivity is increased. In addition to improving the performance, equipment costs are also significantly reduced.
[実施例]
五着用アルミニウム等金板(JIS5052、厚さ0.
3mm ’)を用い、実施例、比較例に示す電解処理を
行ない、水洗・乾燥後、塩化ビニルオルガノゾル系塗料
(関西ペイント社製、KANCOAT l 8−D37
4)を塗布し、熱風乾燥炉中で280℃×30秒の焼き
付けを行なった。[Example] Metal plate such as five-piece aluminum (JIS5052, thickness 0.
After washing and drying, a vinyl chloride organosol paint (manufactured by Kansai Paint Co., Ltd., KANCOAT l 8-D37) was applied.
4) was applied and baked at 280° C. for 30 seconds in a hot air drying oven.
塗膜の厚さは塗膜として15g/m2とした。The thickness of the coating film was 15 g/m2.
このようにして得られたアルミニウム合金塗装板をそれ
ぞれ50mmX50mmに切断してレトルト処理(12
1°C水中60分間処理)をしたのち、塗膜塞着性を評
価するためアルコア法(註)によりフェザリングを発生
させ、その幅の最大値を測定した。The aluminum alloy coated plates thus obtained were each cut into 50mm x 50mm pieces and subjected to retort treatment (12
After treatment in water at 1° C. for 60 minutes, feathering was generated using the Alcoa method (Note) to evaluate coating film adhesion, and the maximum value of its width was measured.
結果を第1表に示す。The results are shown in Table 1.
(註)第1図に示すごとく、1〜2インチ角の塗装され
たアルミニウム板の一辺の中間に騒インチ幅で約5 m
mはど切り込みを入れ、塗装面と反対方向に折り曲げ
ておく。(Note) As shown in Figure 1, approximately 5 m in inch width is placed in the middle of one side of a 1 to 2 inch square painted aluminum plate.
Make a notch in M and fold it in the opposite direction to the painted surface.
これを100〜121’cの熱水中に所定時間(30〜
60分間)浸漬し、取り出すと直ちに万力にはさみ、折
り曲げた部分をペンチで引っ張り引きちぎる。残ったア
ルミ片の破断部における残った塗膜の最大の幅を111
定する。This is placed in hot water of 100-121'C for a specified time (30-121'C).
Soak for 60 minutes), then take it out, immediately put it in a vise, and pull the bent part with pliers to tear it off. The maximum width of the remaining paint film at the broken part of the remaining aluminum piece is 111
Set.
(実施例1)
浴温70℃の2%Na4Pz OtのpHが1O65の
水溶液中にて、交流電流密度10A/dm”(正弦波形
、50Hz)にて23.6秒電解処理(総電気量150
c / d m 2)の電解処理を行なった。(Example 1) In an aqueous solution of 2% Na4Pz Ot with a bath temperature of 70°C and a pH of 1O65, electrolytic treatment was performed for 23.6 seconds at an alternating current density of 10 A/dm" (sine waveform, 50 Hz) (total electricity amount 150
c/d m2) electrolytic treatment was performed.
(実施例2)
交流電解密度2 OA / d m ”で11,8秒電
解処理を行なった以外は実施例1と同一の処理を行なっ
た。(Example 2) The same treatment as in Example 1 was performed except that the electrolytic treatment was performed for 11.8 seconds at an AC electrolytic density of 2 OA/d m''.
(実施例3)
浴温40℃の2%Na 2 Co 3のpHが12の水
溶液中にて10 A / d m 2で23.6秒電解
処理を行なった以外は、実施例1と同一の処理を行なっ
た。(Example 3) Same as Example 1 except that electrolytic treatment was performed at 10 A/d m2 for 23.6 seconds in an aqueous solution of 2% Na2Co3 with a pH of 12 and a bath temperature of 40°C. Processed.
(実施例4)
交流電解密度40 A / d m 2で4.7秒電解
処理を行なった以外は実施例1と同一の処理を行なった
。(Example 4) The same treatment as in Example 1 was performed except that the electrolytic treatment was performed for 4.7 seconds at an AC electrolytic density of 40 A/dm2.
(実施例5)
交流電解密度20 A / d m 2で7,9秒電解
処理を行なった以外は実施例1と同一の処理を行なった
。(Example 5) The same treatment as in Example 1 was performed except that the electrolytic treatment was performed for 7.9 seconds at an AC electrolytic density of 20 A/d m 2 .
(実施例6)
交流電解密度40 A / d m 2で7.9秒電解
処理を行なった以外は実施例1と同一の処理を行なった
。(Example 6) The same treatment as in Example 1 was performed except that the electrolytic treatment was performed for 7.9 seconds at an AC electrolytic density of 40 A/dm2.
(実施例7)
交流電解密度7 A / d m 2で22.4秒電解
処理を行なった以外は実施例1と同一の処理を行なった
。(Example 7) The same treatment as in Example 1 was performed except that the electrolytic treatment was performed for 22.4 seconds at an AC electrolytic density of 7 A/dm2.
(比較例1)
電流密度を3 A / d m 2で行なった以外は、
実施例1と同一の処理を行なった。(Comparative Example 1) Except that the current density was 3 A/d m2,
The same treatment as in Example 1 was performed.
(比較例2)
総電気量を8.0076m2とした以外は実施例1と同
一の処理を行なった。(Comparative Example 2) The same process as in Example 1 was performed except that the total amount of electricity was 8.0076 m2.
(比較例3)
アルカリ系脱脂剤にて脱脂し、水洗した後、皮膜中のC
rMが30 m g / m ”となるようにリン酸ク
ロメート処理を行なった。(Comparative Example 3) After degreasing with an alkaline degreaser and washing with water, C in the film was removed.
Phosphate chromate treatment was performed so that rM was 30 mg/m''.
実施例1〜7、比較例1〜3の結果を第1表に示す。The results of Examples 1 to 7 and Comparative Examples 1 to 3 are shown in Table 1.
(以下余白)
第1表
塗膜密着性評価
[発明の効果J
本発明の缶蓋用アルミニウム合金塗装用板は、現在実施
されているリン酸クロメート処理をした缶蓋用アルミニ
ウム合金塗装材に比して耐フェザリング性が著しく改良
されており、またアルカリ性水溶液を使用するため鋼材
などの装置材料に対する腐食性を大幅に減らすことがで
きること、交流電解法であるため電圧を低めることが容
易であり、大電流密度で短時間の処理で必要な酸化皮膜
を形成できること、脱脂、洗浄と酸化皮膜の形成(陽極
酸化処理)を同一装置内で同一の処理により達成できる
ことなど従来法に比して格段に優れた利点を有する。(Leaving space below) Table 1: Evaluation of paint film adhesion [Effects of the invention J] The aluminum alloy coating plate for can lids of the present invention is comparable to the aluminum alloy coating material for can lids that is currently being treated with phosphoric acid chromate. This method significantly improves the feathering resistance, and since it uses an alkaline aqueous solution, it can significantly reduce the corrosivity to equipment materials such as steel, and because it uses an AC electrolytic method, it is easy to lower the voltage. , the ability to form the necessary oxide film in a short time with high current density, and the ability to perform degreasing, cleaning, and oxide film formation (anodization treatment) in the same equipment, making it significantly superior to conventional methods. has excellent advantages.
第1図はアルコア法によるフェザリング測定法を小す。 FIG. 1 shows the feathering measurement method using the Alcoa method.
Claims (2)
交流電解処理を施して膜厚500〜5000Åの酸化皮
膜を形成させたことを特徴とする塗膜密着性に優れた缶
蓋用アルミニウム合金塗装用板。(1) For aluminum alloy coating for can lids with excellent coating adhesion, characterized by subjecting an aluminum alloy plate to AC electrolysis treatment in an alkaline aqueous solution to form an oxide film with a thickness of 500 to 5000 Å. Board.
流密度4〜50A/dm^2にて電気量が80c/dm
^2を越えることとなる時間、交流電解処理を行なうこ
とを特徴とする塗膜密着性の優れた缶蓋用アルミニウム
合金塗装用板の製造方法。(2) An aluminum alloy plate is heated to an electric capacity of 80 c/dm at a current density of 4 to 50 A/dm^2 in an alkaline aqueous solution.
A method for producing an aluminum alloy coating plate for can lids with excellent coating film adhesion, characterized by performing AC electrolytic treatment for a time exceeding ^2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022557A JPH0832966B2 (en) | 1990-02-01 | 1990-02-01 | Aluminum alloy coating plate for can lid and manufacturing method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022557A JPH0832966B2 (en) | 1990-02-01 | 1990-02-01 | Aluminum alloy coating plate for can lid and manufacturing method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03229895A true JPH03229895A (en) | 1991-10-11 |
| JPH0832966B2 JPH0832966B2 (en) | 1996-03-29 |
Family
ID=12086158
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2022557A Expired - Lifetime JPH0832966B2 (en) | 1990-02-01 | 1990-02-01 | Aluminum alloy coating plate for can lid and manufacturing method thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0832966B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03274296A (en) * | 1990-03-22 | 1991-12-05 | Sky Alum Co Ltd | Aluminum alloy material to be painted for deep drawing and its production |
| WO1999045177A3 (en) * | 1998-03-06 | 1999-11-25 | Dow Chemical Co | Anodic spark coating |
| WO2013118870A1 (en) * | 2012-02-12 | 2013-08-15 | 古河スカイ株式会社 | Surface treated aluminum material, method for producing same, and resin-coated surface treated aluminum material |
| JP2013199664A (en) * | 2012-03-23 | 2013-10-03 | Furukawa-Sky Aluminum Corp | Surface-treated aluminum material and method for producing the same |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4847448A (en) * | 1971-10-22 | 1973-07-05 | ||
| JPS52150751A (en) * | 1976-06-11 | 1977-12-14 | Shokosha Kk | Secondary electrolytic pigmentation process for aluminum and aluminum alloy |
| JPS5425502A (en) * | 1977-07-29 | 1979-02-26 | Kayaba Ind Co Ltd | Multiplex pump apparatus |
| JPS5536718A (en) * | 1978-09-06 | 1980-03-14 | Hitachi Ltd | Level display unit |
| JPS574716A (en) * | 1980-06-12 | 1982-01-11 | Matsushita Electric Works Ltd | Mold for pressure forming |
| JPS6479400A (en) * | 1987-09-18 | 1989-03-24 | Sumitomo Light Metal Ind | Coated aluminum material having superior feathering resistance |
-
1990
- 1990-02-01 JP JP2022557A patent/JPH0832966B2/en not_active Expired - Lifetime
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4847448A (en) * | 1971-10-22 | 1973-07-05 | ||
| JPS52150751A (en) * | 1976-06-11 | 1977-12-14 | Shokosha Kk | Secondary electrolytic pigmentation process for aluminum and aluminum alloy |
| JPS5425502A (en) * | 1977-07-29 | 1979-02-26 | Kayaba Ind Co Ltd | Multiplex pump apparatus |
| JPS5536718A (en) * | 1978-09-06 | 1980-03-14 | Hitachi Ltd | Level display unit |
| JPS574716A (en) * | 1980-06-12 | 1982-01-11 | Matsushita Electric Works Ltd | Mold for pressure forming |
| JPS6479400A (en) * | 1987-09-18 | 1989-03-24 | Sumitomo Light Metal Ind | Coated aluminum material having superior feathering resistance |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03274296A (en) * | 1990-03-22 | 1991-12-05 | Sky Alum Co Ltd | Aluminum alloy material to be painted for deep drawing and its production |
| WO1999045177A3 (en) * | 1998-03-06 | 1999-11-25 | Dow Chemical Co | Anodic spark coating |
| WO2013118870A1 (en) * | 2012-02-12 | 2013-08-15 | 古河スカイ株式会社 | Surface treated aluminum material, method for producing same, and resin-coated surface treated aluminum material |
| CN104114752A (en) * | 2012-02-12 | 2014-10-22 | 株式会社Uacj | Surface treated aluminum material, method for producing same, and resin-coated surface treated aluminum material |
| KR20140123589A (en) | 2012-02-12 | 2014-10-22 | 가부시키가이샤 유에이씨제이 | Surface treated aluminum material, method for producing same, and resin-coated surface treated aluminum material |
| JP2013199664A (en) * | 2012-03-23 | 2013-10-03 | Furukawa-Sky Aluminum Corp | Surface-treated aluminum material and method for producing the same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0832966B2 (en) | 1996-03-29 |
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