JPH0832966B2 - Aluminum alloy coating plate for can lid and manufacturing method thereof - Google Patents
Aluminum alloy coating plate for can lid and manufacturing method thereofInfo
- Publication number
- JPH0832966B2 JPH0832966B2 JP2022557A JP2255790A JPH0832966B2 JP H0832966 B2 JPH0832966 B2 JP H0832966B2 JP 2022557 A JP2022557 A JP 2022557A JP 2255790 A JP2255790 A JP 2255790A JP H0832966 B2 JPH0832966 B2 JP H0832966B2
- Authority
- JP
- Japan
- Prior art keywords
- aluminum alloy
- lid
- treatment
- adhesion
- coating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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- Application Of Or Painting With Fluid Materials (AREA)
- Laminated Bodies (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は缶蓋用アルミニウム合金塗装用板にかかり、
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] The present invention relates to an aluminum alloy coating plate for a can lid,
The present invention relates to an aluminum alloy coating plate for a can lid that requires particularly excellent feathering resistance.
[従来の技術] 従来から、缶蓋用材料としてはAl−Mg系のJIS5052,50
82,5182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, as a material for a can lid, Al-Mg-based JIS5052,50
Aluminum alloy plates such as 82,5182 are used, and are coated to maintain the flavor of the contents of the can and prevent corrosion of the lid material.
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、エッ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。Then, in such coating, first a predetermined aluminum alloy plate is subjected to degreasing and etching treatment, and then phosphoric acid chromate treatment is performed, and then a vinyl chloride organosol-based, epoxyurea-based, or epoxyphenol-based resin coating is applied. 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に対応するため
に塩化ビニルオルガノゾル系塗料を10g/m2以上と圧膜に
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 that a film residue of the coating film on the inner surface of the lid called feathering occurs at the opening when the lid is opened. This phenomenon tends to occur when a vinyl chloride organosol-based paint is applied to a pressure film of 10 g / m 2 or more in order to deal with a more corrosive content, 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、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 serious problem when trying to increase the weight of the coating film in order to deal with more corrosive contents, for example, a container containing a large amount of salt, which was a big problem.
Therefore, the countermeasure against feathering is a major technical problem in the field of the present aluminum coating material, but as a solution to this feathering, by improving the adhesion between the coating film and the aluminum alloy plate, It was known to be preventable.
フェザリング防止の対策としては、例えば特開平1−
230787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℃
加熱処理を行って密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 for preventing feathering, for example, JP-A-1-
In the technology disclosed in No. 230787, the adjustment of the composition of the phosphoric acid chromate treatment liquid and the temperature of the aluminum alloy plate at 20 to 50 ° C.
Heat treatment is performed to improve adhesion. However, strict control of the liquid composition is difficult, and the occurrence of feathering occurs even in the case of manufacturing in the summer when the temperature is high, so it is unlikely that low-temperature heating is sufficiently effective.
特開昭64−79400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-64-79400, the phosphoric acid anodizing treatment is performed instead of the phosphoric acid chromate treatment to improve the adhesion. However, phosphoric acid is extremely corrosive to conductive metal materials and structural steel materials. In addition, a high voltage of 100 V or more is required to perform anodization at a high current density for processing in a short time, which makes industrialization difficult.
[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
広く採用されて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、エッチング処理槽及
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。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。[Problems to be Solved by the Invention] Although the phosphoric acid chromate treatment, which has been most widely used as a conventional base treatment method for aluminum plates, is found to be effective in improving adhesion, a degreasing bath, an etching treatment bath, and a chemical conversion treatment bath. Since a large number of processing tanks are required, the production line becomes long and the equipment cost increases. Further, since several kinds of treatment liquids have to be controlled separately, the quality tends to be unstable, and it is often impossible to stably improve the 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点にある。Particularly, the biggest problem is that the adhesion between the coating film and the aluminum alloy plate is insufficient as a material for a can lid.
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。Further, since the degreasing power is inferior only by electrolytic oxidation with an acidic aqueous solution of phosphoric acid, sulfuric acid, etc., it is necessary to provide a separate degreasing step, and in addition, a thick barrier layer of an oxide film is likely to be formed during electrolysis, and therefore it is necessary to process in a short time In addition, there is a problem that a very high DC electrolysis voltage is required for electrolysis at a high current density. Further, it has a basic problem that it has a strong corrosiveness with respect 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。The present invention effectively solves the above problems, can stably secure the adhesion between the coating film and the aluminum alloy plate, does not require a long time for the treatment, and is a low-cost can lid. It is an object of the present invention to provide an aluminum alloy plate for use and a manufacturing method thereof.
[課題を解決するための手段] 本発明は、缶蓋用アルミニウム合金であって、アルカ
リ性水溶液中の交流電解処理による膜厚500〜5000Åの
酸化皮膜が形成されている、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 an aluminum alloy for can lids, in which an oxide film having a film thickness of 500 to 5000Å is formed by an alternating current electrolytic treatment in an alkaline aqueous solution, which is excellent in coating film adhesion. Another object is to provide an aluminum alloy coating plate for a can lid.
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、膜厚500〜5000Å
の酸化皮膜が形成されるようにアルカリ性水溶液中、浴
温40〜90℃、電流密度4〜50A/dm2にて電気量が80c/dm2
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。Further, the aluminum alloy coating plate for a can lid excellent in the coating film adhesion is an aluminum alloy plate having a film thickness of 500 to 5000 Å
So that the oxide film is formed in an alkaline aqueous solution at a bath temperature of 40 to 90 ° C and a current density of 4 to 50 A / dm 2 with an electric quantity of 80 c / dm 2
For a period of time that exceeds the above, which can be obtained by a method for producing an aluminum alloy coating plate for a can lid excellent in coating film adhesion, which is characterized by performing an alternating current electrolytic treatment, and is a subject of the present invention for feathering resistance. Not only manufacturing aluminum alloy coating plates for can lids with excellent properties, but also processing in a short time,
The present invention also provides a manufacturing method that requires 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500Å〜5000Å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500Å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 the AC electrolytic treatment in the alkaline aqueous solution is formed to have a film thickness of 500Å to 5000Å, whereby the adhesion of the coating film of the vinyl-based coating applied thereon can be remarkably improved. If the thickness of the oxide film is less than 500Å, the thickness of the porous oxide film grown on the dense barrier layer will be insufficient, and the adhesion of the coating film formed on it will not be sufficient. Needless to say.
一方、酸化皮膜の厚さの上限である5000Å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 5000 Å, the effect of the present invention can be enjoyed by increasing the thickness, and there is no particular obstacle, but this degree is the upper limit of the thickness obtained under normal conditions, It is considered that there is no particular advantage even if the thickness is further increased.
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、通常はピロリン酸ナトリウム、炭酸
ナトリウム、炭酸カリウム、水酸化ナトリウム、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。The alkaline aqueous solution used in the present invention does not seem to be particularly limited, and is usually an aqueous solution of sodium pyrophosphate, sodium carbonate, potassium carbonate, sodium hydroxide, sodium phosphate, or the like, or a mixed solution of two or more thereof. Is preferable, and a surfactant may be contained in order to improve 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pH10〜12である。The desirable hydrogen ion exponent (pH) of the electrolytic solution is 9 to 13.5, preferably pH 10 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溶解残
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 the rolling oil and oxide film on the surface of the aluminum alloy plate cannot be dissolved and removed. Also, the bath voltage rises and uneven electrolysis tends to occur, which is not preferable.
On the other hand, if the pH exceeds 13.5, the solubility is too strong, and the resulting dissolved residue is not sufficiently removed by the bubbles, and a porous oxide film having excellent adhesiveness cannot be formed.
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 temperature of the alkaline solution bath during electrolysis is usually 40-
Within the range of 90 ℃. If the temperature is lower than 40 ° C, the degreasing / cleaning effect tends to be insufficient, while if it exceeds 90 ° C, the solubility is too strong, and it becomes difficult to obtain an anodized film having a required thickness. In addition, even in the range of 40 to 90 ° C., particularly preferably in the range of 60 to 80 ° C.
交流電解時の両極性での最大電流密度においては4〜
50A/dm2、好ましくは5〜30A/dm2である。3A/dm2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 maximum current density in both polarities during AC electrolysis is 4 ~
It is 50 A / dm 2 , preferably 5-30 A / dm 2 . If it is less than 3 A / dm 2 , the amount of bubbles generated during electrolysis is insufficient, the cleaning effect on the surface is poor, and the formation of a porous oxide film having excellent adhesion is insufficient, which is not preferable.
50A/dm2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、反応熱による「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 / dm 2 , not only is the electrolytic voltage too high and it is easy for leakage to occur, but also uneven appearance such as “burning” due to reaction heat is likely to occur, which is not preferable.
交流電解は総電気量が80c/dm2を越えることとなる時
間行なう必要がある。総電気量が80c/dm2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。AC electrolysis must be carried out for a time such that the total amount of electricity exceeds 80 c / dm 2 . If the total amount of electricity is 80 c / dm 2 or less, the porous oxide film will not be formed to a predetermined thickness, and therefore the adhesion with the coating film formed thereon will be insufficient. As the current density is higher, sufficient coating film adhesion can be obtained in a shorter time, but since the voltage is higher, a large power source is required.
The polarity must be an alternating waveform.
「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。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。[Operation] In the present invention, electrolytic treatment is carried out using an alternating current in an alkaline solution at a high temperature of 40 to 90 ° C. By such electrolytic treatment, as described in detail below, the surface of the aluminum plate is strongly degreased and washed, and at the same time, an anodized film having excellent coating adhesion is produced.
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500〜5000Å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, regarding the degreasing / cleaning action, in addition to the alkaline solution having degreasing properties by itself,
Due to the high temperature, the degreasing property is stronger. Moreover, in the electrolysis by alternating current, oxygen gas is generated during the anode reaction, while hydrogen gas is generated during the cathode reaction, so the degreasing / cleaning action by the oxidation of organic substances adhering to the plate surface works during the anode reaction, and during the cathode reaction. A mechanical cleaning action works by the expansion of hydrogen bubbles on the plate surface. Therefore, according to the AC electrolysis treatment in a high temperature alkaline solution, the above-mentioned respective functions synergistically exert a strong degreasing / cleaning effect, and adversely affect the coating adhesion in a very short time. It completely removes the rolling oil on the surface of the aluminum alloy sheet and the thermal oxide film formed in a lump, and at the same time forms a porous oxide film with a clean surface and a film thickness of 500 to 5000Å with excellent coating adhesion. is there.
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ができる。Furthermore, since electrolytic treatment is performed by alternating current, rough skin is unlikely to occur, and a large amount of electric current can be applied in a short time without causing rough skin, thus significantly reducing the processing time and improving workability. You can
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を効率よく生成させるこ
とができるのである。That is, in the conventional general electrolytic treatment with direct current, if a large amount of electricity is applied in a short time (therefore,
When electrolyzing at a high current density), the bath voltage is likely to rise rapidly, and thus non-uniform electrolysis is likely to occur, but electrolysis with an AC waveform does not cause this and a large amount of electricity can be generated in a short time without causing skin roughness. A large amount of electrolysis, that is, electrolysis at high current density can be performed, and a film having excellent adhesion can be efficiently produced.
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。Further, in the present invention, as described above, degreasing / cleaning and formation of an anodized film having excellent adhesion are carried out by the same treatment in the same tank, so that when anodizing in another tank after degreasing, Differently, the stains do not adhere between the steps, and the anodic oxide film is generated while the plate surface remains activated, so that a film of uniform quality can be obtained and stable and excellent adhesion can be exhibited. .
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。Therefore, it is considered that the anodized film formed in this way has significantly improved adhesion to the coating film as compared with 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
の電解時間も短かいため、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。Also, degreasing / cleaning and anodized film formation are performed by the same electrolytic treatment in the same tank, and the electrolysis time is also short, so the overall work time is significantly shortened compared to conventional production. And the facility cost will be significantly reduced.
[実施例] 缶蓋用アルミニウム等金板(JIS5052、厚さ0.3mmt)
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、KAN−COATI8−D374)を塗布し、熱風乾燥炉中
で280℃×30秒の焼き付けを行なった。塗膜の厚さは塗
膜として15g/m2とした。[Embodiment] Aluminum metal plate for can lid (JIS5052, thickness 0.3 mm t )
Using Examples, the electrolytic treatment shown in Examples and Comparative Examples is performed, followed by washing with water and drying, and then applying a vinyl chloride organosol paint (KAN-COATI8-D374 manufactured by Kansai Paint Co., Ltd.) in a hot air drying oven at 280 ° C. It was baked for 30 seconds. The thickness of the coating film was 15 g / m 2 as the coating film.
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50mm×50mmに切断してレトルト処理(121℃水中6
0分間処理)をしたのち、塗膜密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 plate thus obtained was cut into 50 mm × 50 mm pieces and retort treated (6
After treatment for 0 minutes, feathering was generated by the Alcoa method (Note) to evaluate the coating adhesion, and the maximum width was measured.
結果を第1図表に示す。 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1/2インチ幅で約5mmほ
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 FIG. 1, make a cut of about 5 mm with a 1/2 inch width in the middle of one side of a painted aluminum plate of 1 to 2 inch square, and bend it in the direction opposite to the painted surface.
これを100〜121℃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測定する。This in hot water at 100-121 ℃ for a predetermined time (30-60 minutes)
Immediately after immersing and taking out, pinch it with a vise and pull off the bent part with pliers. The maximum width of the remaining coating film at the fractured part of the remaining aluminum piece is measured.
(実施例1) 浴温70℃の2%Na4P2O7のpHが10.5の水溶液中にて、
交流電流密度10A/dm2(正弦波形、50Hz)にて23.6秒電
解処理(総電気量150c/dm2)の電解処理を行なった。Example 1 In an aqueous solution of 2% Na 4 P 2 O 7 having a bath temperature of 70 ° C. and a pH of 10.5,
Electrolytic treatment was performed for 23.6 seconds (total electricity amount: 150 c / dm 2 ) at an alternating current density of 10 A / dm 2 (sine waveform, 50 Hz).
(実施例2) 交流電解密度20A/dm2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 at an alternating current electrolytic density of 20 A / dm 2 for 11.8 seconds.
(実施例3) 浴温40℃の2%Na2CO3のpHが12の水溶液中にて10A/dm
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) 10 A / dm in an aqueous solution of 2% Na 2 CO 3 having a pH of 12 at a bath temperature of 40 ° C.
The same treatment as in Example 1 was performed except that the electrolytic treatment was performed at 2 for 23.6 seconds.
(実施例4) 交流電解密度40A/dm2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 at an alternating current electrolytic density of 40 A / dm 2 for 4.7 seconds.
(実施例5) 交流電解密度20A/dm2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 at an alternating current electrolytic density of 20 A / dm 2 for 7.9 seconds.
(実施例6) 交流電解密度40A/dm2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 process as in Example 1 was performed except that the electrolytic treatment was performed at an alternating current electrolytic density of 40 A / dm 2 for 7.9 seconds.
(実施例7) 交流電解密度7A/dm2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 at an AC electrolytic density of 7 A / dm 2 for 22.4 seconds.
(比較例1) 電流密度を3A/dm2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 The same process as in Example 1 was performed except that the current density was 3 A / dm 2 .
(比較例2) 総電気量を80c/dm2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 treatment as in Example 1 was performed except that the total amount of electricity was 80 c / dm 2 .
(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
Cr量が30mg/m2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 degreasing agent and washing with water,
Phosphoric acid chromate treatment was performed so that the Cr amount was 30 mg / m 2 .
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.
[発明の効果] 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較して格段に優れた利点を有す
る。 [Effects of the Invention] The aluminum alloy coating plate for a can lid of the present invention has significantly improved feathering resistance as compared with the currently practiced phosphorous chromate-treated aluminum alloy coating material for a can lid. In addition, since an alkaline aqueous solution is used, corrosiveness to equipment materials such as steel materials can be greatly reduced, and it is easy to reduce the voltage because it is an AC electrolysis method. It has advantages that it can form an oxide film and that it can achieve degreasing and cleaning and formation of an oxide film (anodic oxidation treatment) by the same treatment in the same apparatus, which is far superior to the conventional method.
第1図はアルコア法によるフェザリング測定法を示す。 FIG. 1 shows a feathering measurement method by the Alcoa method.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭64−79400(JP,A) 特開 昭52−150751(JP,A) 特開 昭48−47448(JP,A) 特公 昭55−36718(JP,B2) 特公 昭54−25502(JP,B2) 特公 昭57−4716(JP,B2) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP-A 64-79400 (JP, A) JP-A 52-150751 (JP, A) JP-A 48-47448 (JP, A) JP-B 55- 36718 (JP, B2) JP 54-25502 (JP, B2) JP 57-4716 (JP, B2)
Claims (2)
カリ性水溶液中の交流電解処理による膜厚500〜5000Å
の酸化皮膜が形成されている溶膜密着性に優れた缶蓋用
アルミニウム合金塗装用板。1. An aluminum alloy plate for a can lid, having a film thickness of 500 to 5000Å by an alternating current electrolytic treatment in an alkaline aqueous solution.
Aluminum alloy coating plate for can lids, which has excellent oxide film adhesion and has an oxide film formed on it.
000Åの酸化皮膜が形成されるようにアルカリ性水溶液
中、浴温40〜90℃、電流密度4〜50A/dm2にて電気量が8
0c/dm2を越えることとなる時間、交流電解処理を行うこ
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 for a can lid having a film thickness of 500 to 5
The amount of electricity is 8 at a bath temperature of 40 to 90 ° C and a current density of 4 to 50 A / dm 2 in an alkaline aqueous solution so that an oxide film of 000 Å is formed.
A method for producing an aluminum alloy coating plate for a can lid, which is excellent in coating film adhesion, characterized by performing an alternating current electrolytic treatment for a time that exceeds 0 c / dm 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 JPH03229895A (en) | 1991-10-11 |
JPH0832966B2 true 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) |
Families Citing this family (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 |
AU2888599A (en) * | 1998-03-06 | 1999-09-20 | Dow Chemical Company, The | 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 |
JP6148821B2 (en) * | 2012-03-23 | 2017-06-14 | 株式会社Uacj | Surface-treated aluminum material and method for producing the same |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5214214B2 (en) * | 1971-10-22 | 1977-04-20 | ||
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
Also Published As
Publication number | Publication date |
---|---|
JPH03229895A (en) | 1991-10-11 |
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