JP2003082484A - Surface treatment method for aluminum or aluminum alloy - Google Patents

Surface treatment method for aluminum or aluminum alloy

Info

Publication number
JP2003082484A
JP2003082484A JP2001275098A JP2001275098A JP2003082484A JP 2003082484 A JP2003082484 A JP 2003082484A JP 2001275098 A JP2001275098 A JP 2001275098A JP 2001275098 A JP2001275098 A JP 2001275098A JP 2003082484 A JP2003082484 A JP 2003082484A
Authority
JP
Japan
Prior art keywords
aluminum
bath
acid solution
treatment
degreasing
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.)
Pending
Application number
JP2001275098A
Other languages
Japanese (ja)
Inventor
Masayuki Kamimura
雅之 神村
Satoru Ikeda
哲 池田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Paint Co Ltd
Original Assignee
Nippon Paint Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Paint Co Ltd filed Critical Nippon Paint Co Ltd
Priority to JP2001275098A priority Critical patent/JP2003082484A/en
Publication of JP2003082484A publication Critical patent/JP2003082484A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a surface treatment method for aluminum or an aluminum alloy by which stable degreasing treatment can be performed in a rising period after initial make-up of an electrolytic bath. SOLUTION: An aluminum can is treated by the following stages including degreasing treatment: prerinsing-prewashing-washing (degreasing treatment)- primary rinsing-treatment (chemical conversion film treatment)-secondary rensing-deionized water rinsing-drying. In the degreasing treatment stage, on initial make-up of an electrolytic bath, aluminum salt is added to an acid bath so that the concentration of aluminum ions is controlled to the prescribed one, and, even in the rising period, the level of the aluminum ion concentration of the stable bath is held.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、アルミニウムまた
はアルミニウム合金の表面処理方法に関し、より詳細に
は硫酸イオンを主成分とする酸浴でアルミニウムまたは
アルミニウム合金を脱脂処理する方法に関する。
TECHNICAL FIELD The present invention relates to a surface treatment method for aluminum or an aluminum alloy, and more particularly to a method for degreasing aluminum or an aluminum alloy in an acid bath mainly containing sulfate ions.

【0002】[0002]

【従来の技術】アルミニウムまたはアルミニウム合金
は、家庭用品、家具、電気機器、建材等の広範な分野に
おいて利用されており、さらには、例えば飲料用缶の用
途においても、重量のある鋼鉄製の缶に比べて軽量であ
るアルミニウムまたはアルミニウム合金の缶が大量に利
用されている。
2. Description of the Related Art Aluminum or aluminum alloys are used in a wide range of fields such as household articles, furniture, electric appliances, and building materials. Further, for example, in beverage can applications, heavy steel cans are used. A large amount of aluminum or aluminum alloy cans are used, which are lighter than those in.

【0003】これらアルミニウムまたはアルミニウム合
金は、形成される自然酸化皮膜が不均一であるために耐
食性が不足し、また、表面に塗装を行うときには、この
酸化皮膜が塗料の密着性を阻害するため、表面処理を行
うことが必須である。
[0003] These aluminum or aluminum alloys have a poor natural corrosion resistance due to the non-uniform natural oxide film formed, and when the surface is coated, this oxide film hinders the adhesion of the paint. Surface treatment is essential.

【0004】アルミニウムまたはアルミニウム合金の表
面処理としては、鉄鋼の場合と同様に、サンドブラス
ト、バフ研磨などの機械的処理とともに化学的処理が施
される。
As for the surface treatment of aluminum or aluminum alloy, similar to the case of steel, chemical treatment is carried out in addition to mechanical treatment such as sandblasting and buffing.

【0005】このうち、後者の化学的処理についての標
準的な工程は、脱脂→水洗→皮膜化成→水洗→乾燥であ
る。さらに、脱脂に先立ち予備的に薬液洗浄や水洗が行
われ、あるいは、皮膜化成の前にエッチング、水洗等が
行われることもある。
Among these, the standard process for the latter chemical treatment is degreasing → washing → film formation → washing → drying. Furthermore, prior to degreasing, chemical cleaning or water washing may be performed in advance, or etching, water washing, or the like may be performed before film formation.

【0006】例えば、アルミニウムまたはアルミニウム
合金を用いた飲料用缶の表面処理を行うとき、上記した
各処理を行うための一連の浴が並べられた処理工程にお
いて、開口を下向きに配置した缶が無端のメッシュコン
ベア上に配置されて連続的に搬送され、順次処理が施さ
れる。
[0006] For example, when the surface treatment of a beverage can using aluminum or an aluminum alloy is performed, in the treatment process in which a series of baths for performing each treatment described above is arranged, the can with the opening facing downward is endless. Is placed on the mesh conveyor, continuously conveyed, and sequentially processed.

【0007】脱脂処理工程では、例えば酸浴上を搬送さ
れる缶の上下から酸液が缶に対してスプレーされ、脱脂
が行われる。スプレー後の酸液は酸浴に回収され循環使
用される。
In the degreasing process, for example, an acid solution is sprayed onto the can from above and below the can conveyed on an acid bath to degrease the can. The acid solution after spraying is collected in an acid bath and is recycled.

【0008】上記脱脂処理を含む一連の表面処理は、予
め各浴に所定の組成の液を準備した状態、すなわち、建
浴した後、作業が開始される。無数の缶に対して表面処
理が繰り返し施されるにつれて、脱脂処理工程では酸液
成分の濃度が低下するため、逐次新たな酸液の補給が行
われる。
A series of surface treatments including the above degreasing treatment are started in a state where a liquid having a predetermined composition is prepared in each bath in advance, that is, after the bath is constructed. As the surface treatment is repeatedly applied to innumerable cans, the concentration of the acid liquid component decreases in the degreasing process, so that new acid liquid is sequentially replenished.

【0009】この場合、作業開始後の所定期間、例えば
2〜3日の間は、液組成が不安定になりやすく、所謂不
安定浴の状態にあるが、その後は、液組成が安定化し、
所謂安定浴の状態に至る。
In this case, the liquid composition is likely to be unstable for a predetermined period after the work is started, for example, for 2 to 3 days, and the liquid composition is in a so-called unstable bath state.
A so-called stabilizing bath is reached.

【0010】安定浴になると、その後は原理的には無限
に安定した処理を行うことが可能である。処理対象の缶
の需給条件や作業態勢等の諸事情により例えば日中のみ
処理して夜間は処理を休止するパターンの場合におい
て、休止後処理を再開するときには、休止前の浴を用い
て直ちに安定した処理を行うことができる。
In the stable bath, it is possible in principle to carry out stable treatment infinitely thereafter. Depending on various conditions such as supply and demand conditions of the cans to be treated and work conditions, for example, in the case of a pattern in which processing is done only during the day and processing is suspended at night, when restarting processing after suspension, use the bath before suspension to stabilize immediately. The processing that has been performed can be performed.

【0011】したがって、脱脂処理においては、建浴
後、酸液の組成が安定する安定浴に至るまでの数日間の
運転管理に、より注力することになる。
Therefore, in the degreasing treatment, it is necessary to focus more on operation management for several days after the bath is built up until the stabilizing bath in which the composition of the acid solution is stabilized.

【0012】[0012]

【発明が解決しようとする課題】しかしながら、従来の
脱脂処理の場合、建浴後、酸液の組成が安定する安定浴
に至るまでの数日間の運転管理方法として、使用酸液の
電気伝導度のオンライン測定に基づいて新酸液の自動補
給管理を行い、また、これと合わせてオフラインで使用
酸液の遊離酸濃度測定を所定の頻度で行って酸液の正確
な濃度を把握して新酸液の補給条件を修正する等によっ
て安定した脱脂処理を行うべく努力しているが、このよ
うな管理は煩雑であり、かつこのような煩雑な管理を行
っているにも関わらず、酸液の組成が管理範囲を外れ、
これにより脱脂不良を生じることを完全に回避すること
ができていないのが実情である。そして、このような脱
脂不良より短時間のうちに缶の不良品を大量に発生する
ことになる。
However, in the case of the conventional degreasing treatment, as a method of operation control for several days after the building bath until the stabilizing bath in which the composition of the acid solution is stable, the electric conductivity of the acid solution used is changed. Automatic replenishment management of the new acid solution is performed based on the online measurement, and in addition to this, the free acid concentration of the acid solution used is measured off line at a predetermined frequency to grasp the accurate concentration of the acid solution and measure the new acid. Efforts are being made to carry out stable degreasing treatment by modifying the replenishment conditions of the solution, etc., but such management is complicated, and despite such complicated management, The composition is out of the control range,
The fact is that it has not been possible to completely prevent defective degreasing. Then, a large amount of defective cans will be produced within a short time after such degreasing failure.

【0013】本発明は、上記の課題に鑑みてなされたも
のであり、建浴後の立ちあがり期間において安定した脱
脂処理を行うことができるアルミニウムまたはアルミニ
ウム合金の表面処理方法を提供することを目的とする。
The present invention has been made in view of the above problems, and an object of the present invention is to provide a surface treatment method for aluminum or aluminum alloy, which enables stable degreasing treatment during the rising period after the bath is built. .

【0014】[0014]

【課題を解決するための手段】本発明に係るアルミニウ
ムまたはアルミニウム合金の表面処理方法は、酸浴でア
ルミニウムまたはアルミニウム合金を脱脂処理するアル
ミニウムまたはアルミニウム合金の表面処理方法におい
て、建浴時に、該酸浴中に所定のアルミニウムイオン濃
度になるようにアルミニウム塩を添加しておくことを特
徴とする。
The method for surface treatment of aluminum or aluminum alloy according to the present invention is a method for surface treatment of aluminum or aluminum alloy, which comprises degreasing aluminum or aluminum alloy in an acid bath, wherein the acid is applied during construction. It is characterized in that an aluminum salt is added to the bath so as to have a predetermined aluminum ion concentration.

【0015】ここで、所定のアルミニウムイオン濃度
は、一律ではなく、アルミニウムまたはアルミニウム合
金の所要脱脂量等の処理条件や、酸浴の条件等、具体的
な脱脂処理プロセスごとに異なるものであり、当該プロ
セスごとに実験的に最適なアルミニウムイオンの濃度を
把握し、設定する。このアルミニウムイオンの濃度は、
脱脂処理プロセスが異なっても概ね数百〜数千ppmの
範囲内にある。
Here, the predetermined aluminum ion concentration is not uniform and varies depending on the specific degreasing treatment process such as the treatment conditions such as the required degreasing amount of aluminum or aluminum alloy, the conditions of the acid bath, etc. The optimum aluminum ion concentration is experimentally determined and set for each process. The concentration of this aluminum ion is
Even if the degreasing process is different, it is generally within the range of several hundreds to several thousands ppm.

【0016】従来の脱脂処理においては、建浴後の2〜
3日間の立ちあがり期間において、前記したように、循
環使用中の酸液の電気伝導度のオンライン測定に基づい
て新酸液の自動補給管理を行っている。但し、処理が進
むに連れて酸浴中に缶から溶出したアルミニウムイオン
が蓄積し、循環使用中の酸液のアルミニウムイオンが次
第に上昇し、この結果、酸液の電気伝導度の測定値が変
化し、真の酸液の組成と対応しなくなる。すなわち、仮
に真の酸液の組成が一定であっても、酸液に溶けこむア
ルミニウムイオン濃度の上昇に伴い酸液中の水素イオン
が還元されて水素ガスになり、い酸液中の水素イオン濃
度が低下する。そのため酸液の電気伝導度の測定値(指
示値)が低下する。この結果、新酸液が必要量よりも過
剰に注入され、浴中の酸液の実際の濃度が規定値よりも
高くなる。
In the conventional degreasing treatment, 2 to
During the rising period of 3 days, as described above, the automatic replenishment management of the new acid solution is performed based on the online measurement of the electric conductivity of the acid solution during the cyclic use. However, as the treatment progresses, aluminum ions eluted from the can accumulate in the acid bath, and the aluminum ions in the acid solution during cyclic use gradually increase, resulting in a change in the measured electrical conductivity of the acid solution. However, it does not correspond to the composition of the true acid solution. That is, even if the composition of the true acid solution is constant, as the concentration of aluminum ions dissolved in the acid solution increases, the hydrogen ions in the acid solution are reduced to hydrogen gas, and the hydrogen ions in the acid solution are reduced. The concentration decreases. Therefore, the measured value (indicated value) of the electric conductivity of the acid solution is lowered. As a result, the fresh acid solution is injected in excess of the required amount, and the actual concentration of the acid solution in the bath becomes higher than the specified value.

【0017】この状態を看過すると、アルミニウムある
いはアルミニウム合金はエッチング過多となり、表面が
荒れて外観が白くなりすぎる不具合を生じる。一方、浴
中の酸液の濃度が規定値よりも低くなったときには、ア
ルミニウムあるいはアルミニウム合金はエッチング不十
分となり、後工程である皮膜化成処理において、耐食性
に優れた化成皮膜を形成することができず、密着性も不
十分となる。このため、例えば2時間間隔で酸浴の酸液
をマニュアルサンプリングし、遊離酸濃度を手分析し
て、酸液の正しい組成を把握し、この結果に基づいて、
電気伝導度の設定値を漸次下方修正することにより新酸
液の補給条件の修正を行っている。
If this state is overlooked, aluminum or aluminum alloy will be over-etched, causing a problem that the surface becomes rough and the appearance becomes too white. On the other hand, when the concentration of the acid solution in the bath becomes lower than the specified value, the aluminum or aluminum alloy will be insufficiently etched, and a chemical conversion film having excellent corrosion resistance can be formed in the film chemical conversion treatment in the subsequent step. In addition, the adhesion is insufficient. Therefore, for example, the acid solution in the acid bath is manually sampled at intervals of 2 hours, the free acid concentration is manually analyzed, and the correct composition of the acid solution is grasped. Based on this result,
The replenishment condition of the new acid solution is corrected by gradually lowering the set value of electric conductivity.

【0018】しかしながら、このような、遊離酸濃度の
測定結果に基づくアクションは、ときとして、作業状況
により遊離酸濃度の測定のタイミングが遅れ、あるい
は、測定のタイミングを逸する事態を生じることもあ
り、この場合、酸液の組成が規定値を外れることにな
る。また、2時間間隔での遊離酸濃度の測定結果に基づ
くアクションを確実に行ったたとしても、その2時間の
間に生じる酸液の組成変化を避けることができない。
However, such an action based on the measurement result of the free acid concentration may sometimes cause a delay in the measurement timing of the free acid concentration or a situation in which the measurement timing is missed depending on the work situation. However, in this case, the composition of the acid solution deviates from the specified value. Further, even if the action based on the measurement result of the free acid concentration at 2 hour intervals is surely performed, the composition change of the acid solution which occurs during the 2 hours cannot be avoided.

【0019】なお、短期間で安定浴のアルミニウムイオ
ン濃度条件を得るために、建浴後の初期時間において、
新酸液とは別に補給する補給水の量を極端に絞りあるい
は一定時間が経過するまでは補給水の補給を行わないこ
とも考えられるが、この場合、酸液中に通常含まれる界
面活性剤の浴中での滞留時間が増加することによって界
面活性剤が変質し、脱脂不良の原因となる。
In order to obtain the aluminum ion concentration condition of the stabilizing bath in a short period of time, in the initial time after the bath construction,
It is conceivable that the amount of make-up water to be supplied separately from the new acid solution will be extremely narrowed or the make-up water will not be supplied until a certain period of time elapses. When the residence time in the bath is increased, the surfactant deteriorates and causes degreasing failure.

【0020】これに対して、本発明によれば、事前の実
験等により、対象となる脱脂処理系における安定浴の酸
液中のアルミニウムイオン濃度を把握し、建浴時に、予
め浴中にアルミニウムイオンを添加し、建浴当初から安
定浴の酸液中のアルミニウムイオン濃度を保持するた
め、建浴後の立ちあがり期間中においても、従来と同様
の態勢で電気伝導度および遊離酸濃度の測定管理を行う
ことにより、安定した脱脂処理を行うことができる。
On the other hand, according to the present invention, the aluminum ion concentration in the acid solution of the stabilizing bath in the degreasing system of interest is ascertained by a preliminary experiment, etc. Since ions are added and the aluminum ion concentration in the acid solution of the stabilizing bath is maintained from the beginning of the bath, the electrical conductivity and free acid concentration can be measured and controlled in the same manner as before even during the rising period after the bath. By doing so, a stable degreasing treatment can be performed.

【0021】この場合、前記酸浴が、主成分として硫酸
イオンを含むとともに、副成分として第2鉄イオン、硝
酸イオンおよび界面活性剤を含み、前記アルミニウムま
たはアルミニウム合金が、飲料用缶材料であると、好適
である。
In this case, the acid bath contains sulfate ions as a main component and ferric ions, nitrate ions and a surfactant as auxiliary components, and the aluminum or aluminum alloy is a beverage can material. Is preferable.

【0022】[0022]

【発明の実施の形態】本発明に係るアルミニウムまたは
アルミニウム合金の表面処理方法の好適な実施の形態
(以下、本実施の形態例という。)について、飲料用の
アルミ缶を例にとり、以下に説明する。
BEST MODE FOR CARRYING OUT THE INVENTION A preferred embodiment of the surface treatment method for aluminum or aluminum alloy according to the present invention (hereinafter referred to as the present embodiment) will be described below by taking an aluminum can for beverage as an example. To do.

【0023】アルミニウムDI(ドローイング・アンド
・アイアニング)缶(以下、単にアルミニウム缶とい
う。)は、例えば350mlのビール缶であり、毎分数
千缶単位で表面処理が施される。
An aluminum DI (drawing and ironing) can (hereinafter, simply referred to as an aluminum can) is, for example, a 350 ml beer can and is subjected to surface treatment at a unit of several thousand cans per minute.

【0024】アルミニウム缶は、脱脂処理を含め以下の
工程で処理される。
The aluminum can is treated in the following steps including degreasing treatment.

【0025】プレリンス→プレウオッシュ→ウオッシ
ュ:脱脂処理→第1リンス→トリートメント(化成皮膜
処理)→第2リンス→脱イオン水リンス→乾燥なお、ア
ルミニウム缶は乾燥後、さらに塗装工程に送られ、缶の
表面に意匠が施される。
Pre-rinse → pre-wash → wash: degreasing treatment → first rinse → treatment (chemical conversion coating treatment) → second rinse → deionized water rinse → dry Incidentally, after drying the aluminum can, it is further sent to the painting process, and then the can. Design is applied to the surface of.

【0026】各工程間の缶の搬送は、従来例で説明した
ように、開口を下向きに配置した缶を無端のメッシュコ
ンベア上に配置することによって行われる。
As described in the conventional example, the cans are conveyed between the respective steps by arranging the cans with the openings facing downward on the endless mesh conveyor.

【0027】脱脂処理は、脱脂液としての酸液を貯留し
た浴上をメッシュコンベアによって搬送される缶に対し
てメッシュコンベアの上下双方に設けたスプレーノズル
から、例えば70℃の温度の酸液を缶の内外表面双方
に、例えば30〜50s程度スプレーすることによって
行われる。スプレーノズルから吐出される酸液は、ポン
プによって浴から抜き出された酸液であり、スプレー後
の余剰の酸液は浴中に落下して、回収され、循環使用さ
れる。
The degreasing treatment is carried out by spraying an acid solution at a temperature of, for example, 70 ° C. from spray nozzles provided both above and below the mesh conveyor with respect to a can conveyed by the mesh conveyor on a bath storing an acid solution as a degreasing solution. It is performed by spraying both the inner and outer surfaces of the can for about 30 to 50 seconds. The acid solution discharged from the spray nozzle is the acid solution extracted from the bath by the pump, and the excess acid solution after spraying falls into the bath, is collected, and is circulated and used.

【0028】脱脂処理を連続して行うとき、浴は、酸液
が消費されるとともに、蒸発等により水分が減少する。
このため、酸液の消費、減少程度を電気伝導度のオンラ
イン測定によって把握し、電気伝導度が所定値を維持す
るように酸液を自動補給するとともに、浴中の液レベル
を所定値に維持するように新水を補給する。なお、前記
したように、電気伝導度の測定と平行して、酸液の真の
組成を把握するために酸液の遊離酸を手分析し、遊離酸
の測定値に応じて電気伝導度の設定値を変更することに
より酸液の補給量を修正する。これらの一連の作業自体
は、前記した従来例と同様の内容である。
When the degreasing treatment is continuously carried out, the acid solution is consumed in the bath and the water content is reduced by evaporation or the like.
Therefore, the consumption and decrease of the acid solution are grasped by online measurement of the electric conductivity, and the acid solution is automatically replenished so that the electric conductivity maintains a predetermined value, and the liquid level in the bath is maintained at the predetermined value. Add fresh water as you would. In addition, as described above, in parallel with the measurement of the electric conductivity, the free acid of the acid solution is manually analyzed to grasp the true composition of the acid solution, and the electric conductivity of the free acid is measured according to the measured value of the free acid. Correct the supply amount of acid solution by changing the set value. The series of operations themselves have the same contents as the above-mentioned conventional example.

【0029】本実施の形態例では、作業開始時、すなわ
ち建浴時に浴中に張り込まれる新しい酸液は、以下の組
成に調製される。
In the present embodiment, a new acid solution filled in the bath at the start of work, that is, at the time of building a bath is prepared to have the following composition.

【0030】すなわち、ベース組成として、図1に示す
薬剤を、予め検討し、設定された、当該脱脂処理プロセ
スにおいて望ましい図1の酸液の組成になるように所定
量の水の中に添加する。薬剤は、例えば、硫酸イオン源
として硫酸、硫酸第2鉄、硫酸アルミニウムを用い、第
2鉄イオン源として硫酸第2鉄を用い、硝酸イオン源と
して試薬硝酸を用い、界面活性剤としてポリオキシエチ
レンアルキルエーテルを用いる。なお、酸液は、運転
中、このベース組成を維持するように濃度管理される。
That is, as the base composition, the chemical shown in FIG. 1 is added in a predetermined amount of water so that the composition of the acid solution shown in FIG. . As the drug, for example, sulfuric acid, ferric sulfate, and aluminum sulfate are used as a sulfate ion source, ferric sulfate is used as a ferric ion source, reagent nitric acid is used as a nitrate ion source, and polyoxyethylene is used as a surfactant. Alkyl ether is used. The concentration of the acid solution is controlled during operation so as to maintain this base composition.

【0031】そして、建浴時の硫酸イオン源の一部とし
て、例えば硫酸アルミニウムの14〜18水塩を添加す
る場合、このアルミニウムイオンの所定の濃度は、脱脂
処理プロセス条件によって異なり、例えば、図2に示す
ように、500〜1500ppmの範囲内の特定の値と
する。
When, for example, a 14-18 hydrate of aluminum sulfate is added as a part of the sulfate ion source at the time of building the bath, the predetermined concentration of this aluminum ion varies depending on the degreasing treatment process conditions. As shown in 2, the specific value is within the range of 500 to 1500 ppm.

【0032】このとき、上記図2に示すように、図1の
一定のベース組成であっても酸液中のアルミニウムイオ
ンの濃度レベルによって、酸液の電気伝導度は異なり、
アルミニウムイオンの濃度が大きくなるにつれて電気伝
導度は例えば53(mS/cm)から49(mS/c
m)へと低下する。ちなみに、図2に合わせて示すよう
に、従来の建浴時のアルミニウムイオンの存在しない酸
浴の電気伝導度は53(mS/cm)である。なお、電
気伝導度の測定温度は70℃である。
At this time, as shown in FIG. 2, the electric conductivity of the acid solution varies depending on the concentration level of aluminum ions in the acid solution even if the base composition shown in FIG. 1 is constant.
As the concentration of aluminum ions increases, the electrical conductivity increases, for example, from 53 (mS / cm) to 49 (mS / c).
m). By the way, as shown in FIG. 2, the electric conductivity of the conventional acid bath in which aluminum ions do not exist at the time of building bath is 53 (mS / cm). The measurement temperature of electric conductivity is 70 ° C.

【0033】上記本実施の形態例の表面処理方法では、
建浴当初から安定浴の酸液中のアルミニウムイオン濃度
を保持するため、建浴後の立ちあがり期間中において
も、従来と同様の態勢で電気伝導度および遊離酸濃度の
測定管理を行うことにより、基本的には電気伝導度に基
づく酸液の自動補給制御によって組成変動の少ない酸液
の状態を常に維持することができ、さらに遊離酸濃度の
測定管理によってより正確な酸液の組成に修正、維持さ
れる。これにより、建浴後の立ちあがり期間中において
も、安定した脱脂処理を行うことができ、脱脂不良の缶
の発生を防止することができる。
In the surface treatment method of the above-mentioned embodiment,
Since the aluminum ion concentration in the acid solution of the stable bath is maintained from the beginning of the bath, the electrical conductivity and free acid concentration can be measured and managed in the same manner as before even during the rising period after the bath is built up. As a result, the automatic replenishment control of the acid solution based on electrical conductivity can always maintain the state of the acid solution with less composition fluctuation, and the measurement and control of the free acid concentration corrects and maintains the composition of the acid solution more accurately To be done. This makes it possible to perform a stable degreasing treatment even during the standing-up period after the bath is built up, and to prevent the occurrence of defective degreasing cans.

【0034】[0034]

【発明の効果】本発明に係るアルミニウムまたはアルミ
ニウム合金の表面処理方法によれば、酸浴でアルミニウ
ムまたはアルミニウム合金を脱脂処理するアルミニウム
またはアルミニウム合金の表面処理方法において、建浴
時に、該酸浴中に所定のアルミニウムイオン濃度になる
ようにアルミニウム塩を添加しておくため、建浴後の立
ちあがり期間中においても、従来と同様の態勢で電気伝
導度および遊離酸濃度の測定管理を行うことにより、安
定した脱脂処理を行うことができ、アルミニウムあるい
はアルミニウム合金がエッチング過多となって表面が荒
れて外観が白くなりすぎる不具合や、エッチング不十分
となって後工程である皮膜化成処理において耐食性が不
十分となる不具合を防止することができる。
According to the surface treatment method for aluminum or aluminum alloy according to the present invention, in the surface treatment method for aluminum or aluminum alloy in which degreasing treatment of aluminum or aluminum alloy is carried out in an acid bath, during the construction bath, in the acid bath Since an aluminum salt is added to the container so that it has a predetermined aluminum ion concentration, it is possible to stabilize by measuring and controlling the electric conductivity and the free acid concentration in the same manner as before even during the standing up period after the construction bath. Degreasing treatment can be performed, aluminum or aluminum alloy is overetched and the surface becomes rough and the appearance becomes too white, or the etching becomes insufficient and corrosion resistance is insufficient in the film chemical conversion treatment which is a post process. Can be prevented.

【0035】また、本発明に係るアルミニウムまたはア
ルミニウム合金の表面処理方法によれば、酸浴が、主成
分として硫酸イオンを含むとともに、副成分として第2
鉄イオン、硝酸イオンおよび界面活性剤を含み、アルミ
ニウムまたはアルミニウム合金が、飲料用缶材料である
と、好適である。
According to the surface treatment method for aluminum or aluminum alloy according to the present invention, the acid bath contains sulfate ions as the main component and the second component as the sub-component.
Aluminum or aluminum alloy containing iron ions, nitrate ions and a surfactant is preferably used as a beverage can material.

【図面の簡単な説明】[Brief description of drawings]

【図1】脱脂処理液のベース組成を示す表図である。FIG. 1 is a table showing a base composition of a degreasing treatment liquid.

【図2】建浴時に浴中に添加して保持されるアルミニウ
ムイオンの濃度およびそのときの電気伝導度を示す表図
である。
FIG. 2 is a table showing the concentration of aluminum ions added and retained in the bath during the construction bath and the electrical conductivity at that time.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 酸浴でアルミニウムまたはアルミニウム
合金を脱脂処理するアルミニウムまたはアルミニウム合
金の表面処理方法において、 建浴時に、該酸浴中に所定のアルミニウムイオン濃度に
なるようにアルミニウム塩を添加しておくことを特徴と
するアルミニウムまたはアルミニウム合金の表面処理方
法。
1. A method for surface-treating aluminum or an aluminum alloy for degreasing aluminum or an aluminum alloy in an acid bath, wherein an aluminum salt is added to the acid bath at a predetermined aluminum ion concentration during the construction bath. A method for treating the surface of aluminum or an aluminum alloy, which comprises:
【請求項2】 前記酸浴が、主成分として硫酸イオンを
含むとともに、副成分として第2鉄イオン、硝酸イオン
および界面活性剤を含み、 前記アルミニウムまたはアルミニウム合金が、飲料用缶
材料であることを特徴とする請求項1記載のアルミニウ
ムまたはアルミニウム合金の表面処理方法。
2. The acid bath contains sulfate ions as a main component and ferric ions, nitrate ions and a surfactant as auxiliary components, and the aluminum or aluminum alloy is a beverage can material. The surface treatment method for aluminum or aluminum alloy according to claim 1, wherein
JP2001275098A 2001-09-11 2001-09-11 Surface treatment method for aluminum or aluminum alloy Pending JP2003082484A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001275098A JP2003082484A (en) 2001-09-11 2001-09-11 Surface treatment method for aluminum or aluminum alloy

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001275098A JP2003082484A (en) 2001-09-11 2001-09-11 Surface treatment method for aluminum or aluminum alloy

Publications (1)

Publication Number Publication Date
JP2003082484A true JP2003082484A (en) 2003-03-19

Family

ID=19100021

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001275098A Pending JP2003082484A (en) 2001-09-11 2001-09-11 Surface treatment method for aluminum or aluminum alloy

Country Status (1)

Country Link
JP (1) JP2003082484A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101893900B1 (en) 2018-06-01 2018-08-31 주식회사 에이엘텍 Aluminum foil washing equipment and control method of said aluminum foil washing equipment

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61231188A (en) * 1985-04-04 1986-10-15 Nippon Paint Co Ltd Method for controlling aluminum surface cleaning agent
JPH03140483A (en) * 1989-10-26 1991-06-14 Matsushita Electric Works Ltd Surface treatment for copper laminated sheet
JP2001226790A (en) * 2000-02-15 2001-08-21 Nippon Paint Co Ltd Acidic cleaning solution for aluminum material and cleaning method therefor

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61231188A (en) * 1985-04-04 1986-10-15 Nippon Paint Co Ltd Method for controlling aluminum surface cleaning agent
JPH03140483A (en) * 1989-10-26 1991-06-14 Matsushita Electric Works Ltd Surface treatment for copper laminated sheet
JP2001226790A (en) * 2000-02-15 2001-08-21 Nippon Paint Co Ltd Acidic cleaning solution for aluminum material and cleaning method therefor

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101893900B1 (en) 2018-06-01 2018-08-31 주식회사 에이엘텍 Aluminum foil washing equipment and control method of said aluminum foil washing equipment

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