JP2983404B2 - Continuous annealing and acid cleaning same line processing method for Mg-containing aluminum alloy plate - Google Patents

Continuous annealing and acid cleaning same line processing method for Mg-containing aluminum alloy plate

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Publication number
JP2983404B2
JP2983404B2 JP5062471A JP6247193A JP2983404B2 JP 2983404 B2 JP2983404 B2 JP 2983404B2 JP 5062471 A JP5062471 A JP 5062471A JP 6247193 A JP6247193 A JP 6247193A JP 2983404 B2 JP2983404 B2 JP 2983404B2
Authority
JP
Japan
Prior art keywords
acid cleaning
continuous annealing
aluminum alloy
acid
solution
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 - Fee Related
Application number
JP5062471A
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Japanese (ja)
Other versions
JPH06256980A (en
Inventor
義孝 広前
正裕 倉田
公隆 林
吉彦 武岡
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.)
SUKAI ARUMINIUMU KK
Nippon Steel Corp
Original Assignee
SUKAI ARUMINIUMU KK
Nippon Steel Corp
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Application filed by SUKAI ARUMINIUMU KK, Nippon Steel Corp filed Critical SUKAI ARUMINIUMU KK
Priority to JP5062471A priority Critical patent/JP2983404B2/en
Publication of JPH06256980A publication Critical patent/JPH06256980A/en
Application granted granted Critical
Publication of JP2983404B2 publication Critical patent/JP2983404B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、缶の素材あるいは自
動車車体の素材等として用いられるMg含有アルミニウ
ム合金板について、MgOを主体とする酸化膜の除去の
ために酸洗浄を行なう方法に関するものであり、特に酸
洗浄を連続焼鈍と同一のラインで行なう方法に関するも
のである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of performing acid cleaning on a Mg-containing aluminum alloy plate used as a material for a can or a body of an automobile for removing an oxide film mainly composed of MgO. Particularly, the present invention relates to a method of performing acid cleaning on the same line as continuous annealing.

【0002】[0002]

【従来の技術】周知のようにMgを比較的多量に含有す
る合金としては、JIS 5000番系のAl−Mg系
合金、JIS 6000番系のAl−Mg−Si系合
金、JIS 7000番系のAl−Zn−Mg系合金な
どがある。ところでMgは極めて酸化され易い元素であ
るため、酸素や水分を含有する雰囲気中で前述のような
Mg含有アルミニウム合金に熱処理を施せば、表面にM
gOを主体とする酸化膜が形成されてしまう。一方、缶
あるいは自動車車体等の用途においては、アルミニウム
合金板表面に塗装を施すことが多く、またその場合塗装
前にクロメート処理やリン酸亜鉛処理等の化成処理を施
しておくことも多い。ところが前述のようにMgOを主
体とする酸化膜が表面に形成されたアルミニウム合金板
では、塗膜の密着性が悪くなったり、化成処理性が悪く
なったりし、そのため塗膜や化成皮膜が均一に形成され
なくなって、塗装後の耐食性が劣ってしまう問題が生じ
る。そこで従来から、Mg含有アルミニウム合金板につ
いては、塗装前あるいは化成処理前に硫酸溶液等を用い
て酸洗浄を行ない、表面の酸化膜を除去することが行な
われている。
2. Description of the Related Art As is well known, alloys containing relatively large amounts of Mg include JIS No. 5000 series Al-Mg based alloys, JIS No. 6000 series Al-Mg-Si based alloys, and JIS No. 7000 series alloys. Al-Zn-Mg alloys and the like are available. By the way, since Mg is an element which is extremely easily oxidized, if the above-described Mg-containing aluminum alloy is subjected to a heat treatment in an atmosphere containing oxygen or moisture, the surface of the Mg-containing aluminum alloy becomes M
An oxide film mainly composed of gO is formed. On the other hand, in applications such as cans and automobile bodies, the surface of an aluminum alloy plate is often coated, and in that case, a chemical conversion treatment such as chromate treatment or zinc phosphate treatment is often performed before painting. However, in the case of an aluminum alloy plate having an oxide film mainly composed of MgO formed on the surface as described above, the adhesion of the coating film becomes poor, or the chemical conversion treatment becomes poor, so that the coating film or the chemical conversion film becomes uniform. And the corrosion resistance after coating is deteriorated. Therefore, conventionally, an Mg-containing aluminum alloy plate has been subjected to acid cleaning using a sulfuric acid solution or the like before coating or chemical conversion treatment to remove an oxide film on the surface.

【0003】従来このような酸洗浄を行なうにあたって
は、専用の酸洗浄ラインを設けておき、酸洗浄を独立し
た工程で行なうか、あるいは化成処理−塗装ラインに酸
洗浄装置を組入れておいて、化成処理の前処理として酸
洗浄を行なうのが通常であった。
Conventionally, in performing such acid cleaning, a dedicated acid cleaning line is provided, and the acid cleaning is performed in an independent process, or an acid cleaning apparatus is incorporated in the chemical conversion-coating line. Usually, acid cleaning is performed as a pretreatment of the chemical conversion treatment.

【0004】[0004]

【発明が解決しようとする課題】前述のようにMg含有
アルミニウム合金板の酸化膜除去のために、専用の酸洗
浄ラインを設けて酸洗浄を独立の工程として行なう場
合、製造工程が増えるため、コスト上昇を招く問題があ
る。また化成処理−塗装ラインに酸洗浄装置を組込んで
化成処理の前処理として酸洗浄を行なう場合、化成処理
の温度との関係から酸洗浄の温度を余り高温にすること
ができず、そのため酸洗浄時間が長くなって生産性が劣
る問題がある。
As described above, in the case where a dedicated acid cleaning line is provided and acid cleaning is performed as an independent step for removing an oxide film from the Mg-containing aluminum alloy plate, the number of manufacturing steps increases. There is a problem that increases costs. In addition, when acid cleaning is performed as a pretreatment of a chemical conversion treatment by incorporating an acid cleaning device in the chemical conversion-coating line, the temperature of the acid cleaning cannot be made too high due to the relationship with the temperature of the chemical conversion treatment. There is a problem that the washing time becomes longer and the productivity is deteriorated.

【0005】ところで最近のアルミニウム合金薄板の製
造過程においては、再結晶や溶体化、あるいは軟質化等
の目的で行なう焼鈍として、コイルから連続的に薄板を
繰出しながら炉内を連続的に通過させ、再びコイル状に
巻取るようにした連続焼鈍を適用することが多くなって
おり、既に述べたようなMg含有アルミニウム合金板に
ついても連続焼鈍を行なうことが多くなっている。
[0005] In the recent production process of aluminum alloy sheets, annealing is performed for the purpose of recrystallization, solution treatment, softening, etc., and the sheet is continuously passed through the furnace while continuously feeding the sheet from the coil. In many cases, continuous annealing in which a coil is wound again is applied, and continuous annealing is often performed also on an Mg-containing aluminum alloy plate as described above.

【0006】そこでこのような連続焼鈍ラインに酸洗浄
装置を組込み、連続焼鈍と酸洗浄とを同一ラインで処理
することによって、製造工程数の増加によるコスト上昇
を抑えることが考えられる。しかしながらその場合にお
いて、連続焼鈍ラインに適した条件でMgOを主体とす
る酸化膜を確実に除去ししかも既存の連続焼鈍設備の大
幅な改変を伴なうことなく実施するための方法は、未だ
確立されていなかったのが実情である。
Therefore, it is conceivable to incorporate an acid cleaning apparatus into such a continuous annealing line and perform continuous annealing and acid cleaning on the same line, thereby suppressing an increase in cost due to an increase in the number of manufacturing steps. However, in this case, a method for reliably removing an oxide film mainly composed of MgO under conditions suitable for a continuous annealing line and performing the method without significant modification of existing continuous annealing equipment is still established. The fact is that it was not done.

【0007】この発明は以上の事情を背景としてなされ
たもので、Mg含有アルミニウム合金板について、その
表面のMgOを主体とする酸化膜を除去するための酸洗
浄を、大幅なコスト上昇や生産性の低下を招くことな
く、高能率で行ない得るようにすることを基本的な目的
とし、特に連続焼鈍と酸洗浄とを同一ラインで処理する
場合において、短時間で確実に酸化膜を除去でき、しか
も既存の連続焼鈍ラインの大幅な設備改変を伴なうこと
なく、低コストで実施し得るようにした方法を提供する
ことを目的とするものである。
The present invention has been made in view of the above circumstances. For an Mg-containing aluminum alloy plate, acid cleaning for removing an oxide film mainly composed of MgO on the surface of the aluminum alloy plate is performed at a large cost and productivity. The basic purpose is to be able to perform at a high efficiency without inducing the decrease of, especially when the continuous annealing and the acid cleaning are processed in the same line, the oxide film can be reliably removed in a short time, Moreover, it is an object of the present invention to provide a method which can be carried out at low cost without significantly modifying the existing continuous annealing line.

【0008】[0008]

【課題を解決するための手段】前述のような課題を解決
するため、本発明者等は鋭意実験・検討を重ねた結果、
酸洗浄液の温度を、処理対象のMg含有アルミニウム合
金板が酸洗浄液に接触している時間(酸洗浄時間)に応
じて適切な範囲内に定めることによって、短時間で確実
にMgOを主体とする酸化膜を除去できることを見出し
た。そしてその条件を適用することによって、連続焼鈍
ライン中での酸洗浄が実際に可能となること、しかも既
存の連続焼鈍設備の大幅な改変を要さずに実施可能とな
ること、さらには連続焼鈍直後の板の保有熱を有効利用
して、熱効率をも向上させ得ることを見出し、この発明
をなすに至った。
Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors have conducted extensive experiments and studies, and as a result,
By setting the temperature of the pickling solution within an appropriate range according to the time during which the Mg-containing aluminum alloy plate to be treated is in contact with the pickling solution (the pickling time), MgO is surely mainly contained in a short time. It has been found that the oxide film can be removed. By applying the conditions, acid cleaning in the continuous annealing line can actually be performed, and it can be performed without significant modification of the existing continuous annealing equipment. The present inventors have found that the heat efficiency of the plate immediately after can be effectively utilized to improve the thermal efficiency, and have led to the present invention.

【0009】具体的には、請求項1の発明の連続焼鈍・
酸洗浄同一ライン処理方法は、Mgを0.3wt%以上含
有するアルミニウム合金板について連続焼鈍を施すにあ
たり、連続焼鈍後のアルミニウム合金板を巻取る前に、
その連続焼鈍後のアルミニウム合金板を、酸洗浄液中も
しくは酸洗浄液スプレー帯中を通過させ、かつその通過
中の酸洗浄液接触時間を20秒以下に規制するととも
に、接触時間t(秒)と酸洗浄液の温度T(℃)との関
係が、次の(1)式 logt≧3.6−3.5×10-2×T …(1) を満たすように規制することを特徴とするものである。
Specifically, the continuous annealing of the invention of claim 1
The acid cleaning same line processing method is to perform continuous annealing on an aluminum alloy plate containing 0.3 wt% or more of Mg, before winding the aluminum alloy plate after the continuous annealing,
The aluminum alloy plate after the continuous annealing is passed through an acid cleaning liquid or an acid cleaning liquid spray zone, and the contact time of the acid cleaning liquid during the passage is restricted to 20 seconds or less. Is regulated so as to satisfy the following equation (1): logt ≧ 3.6−3.5 × 10 −2 × T (1) .

【0010】さらに請求項2の発明の連続焼鈍・酸洗浄
同一ライン処理方法は、請求項1に記載の方法におい
て、前記酸洗浄液として、硫酸、硝酸もしくは燐酸の1
種以上を合計で1〜20wt%の濃度で含み、かつpHが
2.0以下のものを用いるものである。
Further, in the method for continuous annealing and pickling in the same line according to the second aspect of the present invention, in the method according to the first aspect, the acid cleaning solution may include sulfuric acid, nitric acid or phosphoric acid.
Those containing more than one species at a concentration of 1 to 20 wt% in total and having a pH of 2.0 or less are used.

【0011】そしてまた請求項3の発明の連続焼鈍・酸
洗浄同一ライン処理方法は、請求項1に記載の方法にお
いて、連続焼鈍後、アルミニウム合金板を酸洗浄液中も
しくは酸洗浄液スプレー帯に導入する前に、アルカリ脱
脂を連続的に行なうものである。
According to a third aspect of the present invention, in the method of the first aspect, after the continuous annealing, the aluminum alloy plate is introduced into the acid cleaning solution or into the acid cleaning solution spray zone. Prior to this, alkali degreasing is continuously performed.

【0012】[0012]

【作用】この発明において対象とするアルミニウム合金
板は、Mgを0.3wt%以上含有するものとする。Mg
が0.3wt%未満のアルミニウム合金では、MgO主体
の酸化膜が形成されにくいため、特に酸洗浄を要するこ
とは少ない。このようにMgを0.3wt%以上含有する
アルミニウム合金としては、代表的には、前述のように
JIS 5000番系、6000番系、7000番系が
あるが、これらに限定されないことはもちろんである。
なおMg量の上限は特に規定しないが、工業的に使用さ
れるアルミニウム合金板としては、Mg量が10wt%以
下の場合が多い。
According to the present invention, an aluminum alloy plate to be treated contains 0.3 wt% or more of Mg. Mg
In an aluminum alloy having a content of less than 0.3 wt%, an oxide film mainly composed of MgO is difficult to be formed, so that acid cleaning is rarely required. As described above, typical aluminum alloys containing 0.3 wt% or more of Mg include JIS No. 5000 series, 6000 series, and 7000 series as described above, but are not limited to these. is there.
Although the upper limit of the Mg content is not particularly specified, the aluminum alloy plate used industrially often has a Mg content of 10% by weight or less.

【0013】この発明の方法では、前述のようなMg含
有アルミニウム合金板の酸洗浄を、板製造過程における
連続焼鈍ライン中で行なう。すなわち、例えば図1に示
すように連続焼鈍ライン1中に酸洗浄装置2を配設して
おき、連続焼鈍に続いて酸洗浄を連続的に行なう。
In the method of the present invention, the acid cleaning of the Mg-containing aluminum alloy plate as described above is performed in a continuous annealing line in the plate manufacturing process. That is, for example, as shown in FIG. 1, an acid cleaning device 2 is provided in a continuous annealing line 1 and acid cleaning is continuously performed after continuous annealing.

【0014】具体的な連続焼鈍−酸洗浄について図1の
場合を例にとって説明すれば、一般に連続焼鈍ライン1
においては、アンコイラ(コイル繰出装置)3から繰出
されたアルミニウム合金板4は、入側アキュムレータ5
を経て連続焼鈍炉6に導かれる。この連続焼鈍炉6は、
通常は予加熱帯6A、保持帯6B、冷却帯6Cに区分さ
れている。この連続焼鈍炉6の冷却帯6Cから出たアル
ミニウム合金板4は、従来の一般的な連続焼鈍ラインの
場合は、そのまま出側アキュムレータ7を経てリコイラ
(巻取機)8によって再びコイル状に巻取られる。一方
この発明の方法を実施する場合、連続焼鈍炉6の出側と
出側アキュムレータ7との間に酸洗浄装置2を設置して
おき、アルミニウム合金板4に対する酸洗浄を、連続焼
鈍後、巻取前に連続的に行なうことになる。ここで、酸
洗浄装置2は、酸洗浄液中にアルミニウム合金板を直接
浸漬させる型式のもの、すなわち酸洗浴タイプのものと
しても、あるいはスプレーにて酸洗浄液をアルミニウム
合金板に吹付けるようにしたスプレー帯を有する構成の
ものとしても良い。
A specific example of the continuous annealing-acid cleaning will be described by taking the case of FIG. 1 as an example.
In the above, the aluminum alloy plate 4 fed from the uncoiler (coil feeding device) 3 is connected to an entry-side accumulator 5.
Through the continuous annealing furnace 6. This continuous annealing furnace 6
Usually, it is divided into a preheating zone 6A, a holding zone 6B, and a cooling zone 6C. In the case of a conventional general continuous annealing line, the aluminum alloy plate 4 that has exited from the cooling zone 6C of the continuous annealing furnace 6 is again wound into a coil shape by a recoiler (winding machine) 8 through an outlet accumulator 7 as it is. Taken. On the other hand, when carrying out the method of the present invention, the acid cleaning device 2 is installed between the discharge side of the continuous annealing furnace 6 and the discharge side accumulator 7, and the acid cleaning for the aluminum alloy plate 4 is performed after the continuous annealing and the winding. It will be done continuously before taking. Here, the pickling apparatus 2 is of a type in which the aluminum alloy plate is directly immersed in the pickling solution, that is, a pickling bath type, or a spray in which the pickling solution is sprayed on the aluminum alloy plate by a spray. A configuration having a band may be used.

【0015】このように連続焼鈍ライン中で酸洗浄を行
なうにあたっては、酸洗浄時間と酸洗温度との関係が極
めて重要である。
As described above, in performing the pickling in the continuous annealing line, the relationship between the pickling time and the pickling temperature is extremely important.

【0016】すなわち、本発明者等が、後述する実施例
で改めて説明するように、Mg4.5wt%、Cu0.3
wt%を含有し、残部が実質的にAlよりなり、通常の連
続焼鈍により表面にMgOを主体とする酸化膜が形成さ
れたアルミニウム合金板について、10%H2 SO4
溶液からなる酸洗浄液を用いた場合における表面のMg
Oを主体とする酸化膜の除去に要する時間と酸洗浄液の
温度との関係を調べたところ、図2に示すような結果が
得られた。なおここで、MgOを主体とする酸化膜の除
去時間は、グロー放電発光分析(GDS)によって表面
層のMgピークが実質的に消失するまでの酸洗浄時間と
して求めた。酸洗浄前後のGDS分析結果の代表例を図
3の(A),(B)に示す。図3の(A)は酸洗浄前の
状態であって、表面附近にMgのピークがあらわれてお
り、一方図3の(B)は10%H2 SO4 からなる酸洗
浄液によって80℃で10秒酸洗浄した後の状態であっ
て、Mgのピークが消失していることが判る。
That is, as will be described later by the present inventors in the embodiments described later, Mg 4.5 wt%, Cu 0.3
An acid cleaning solution consisting of a 10% H 2 SO 4 aqueous solution was used for an aluminum alloy plate containing wt%, the balance being substantially Al and having an oxide film mainly composed of MgO formed on the surface by ordinary continuous annealing. Mg on the surface when used
When the relationship between the time required for removing the oxide film mainly composed of O and the temperature of the acid cleaning solution was examined, the results shown in FIG. 2 were obtained. Here, the removal time of the oxide film mainly composed of MgO was determined by glow discharge emission spectroscopy (GDS) as the acid cleaning time until the Mg peak on the surface layer substantially disappeared. Representative examples of the GDS analysis results before and after the acid washing are shown in FIGS. FIG. 3A shows a state before the acid cleaning, in which a Mg peak appears near the surface, while FIG. 3B shows a state at 80 ° C. of 10% with an acid cleaning solution containing 10% H 2 SO 4. It can be seen that the Mg peak has disappeared in the state after the acid washing for 2 seconds.

【0017】図2に示されるように、通常の連続焼鈍に
より形成された表面のMgOを主体とする酸化膜の除去
に要する時間は、酸洗浄液の温度に大きく影響され、図
2の直線Lの右上の領域の酸洗浄時間−酸洗浄液温度と
した場合にMgOを主体とする酸化膜の除去がほぼ完全
になされることが判明した。ここで、酸洗浄時間をt
(秒)、酸洗浄液の温度をT(℃)とすれば、直線L
は、次の(2)式であらわされる。 logt=3.6−3.5×10-2×T …(2)
As shown in FIG. 2, the time required to remove the oxide film mainly composed of MgO on the surface formed by ordinary continuous annealing is greatly affected by the temperature of the acid cleaning solution, and is represented by a straight line L in FIG. It was found that the removal of the oxide film mainly composed of MgO was almost completely performed when the acid cleaning time and the acid cleaning solution temperature in the upper right region were set. Here, the acid cleaning time is t
(Seconds), if the temperature of the acid cleaning solution is T (° C.), the straight line L
Is expressed by the following equation (2). logt = 3.6-3.5 × 10 −2 × T (2)

【0018】したがって、酸洗浄時間(すなわち酸洗浄
液に接触している時間)tを、酸洗浄液の温度Tに応じ
て次の(1)式 logt≧3.6−3.5×10-2×T …(1) を満たす時間とすることによって、MgOを主体とする
酸化膜のほぼ完全な除去を図ることができる。
Therefore, the pickling time (that is, the time during which the pickling solution is in contact with the pickling solution) is changed by the following equation (1) according to the temperature T of the pickling solution: logt ≧ 3.6−3.5 × 10 −2 × By setting the time to satisfy T 1 (1), it is possible to substantially completely remove the oxide film mainly composed of MgO.

【0019】また連続焼鈍ラインにおいては、既存の連
続焼鈍設備において設置可能な酸洗浄装置の設備長さは
限られており、一方ラインを新設する場合でもなるべく
コンパクトな設計が要求されるから、一般に適用されて
いるアルミの連続焼鈍のライン速度(30〜200m/
min )とを考慮すれば、長時間の酸洗浄は不適当であ
る。すなわち、一般的な連続焼鈍のライン速度で長時間
酸洗浄を行なう場合には、酸洗浄装置が長大化して、既
存の連続焼鈍ラインにおける連続焼鈍炉と出側アキュム
レータとの間に酸洗浄装置を設置することが困難とな
り、また新設のラインでもライン長が著しく長くなって
しまう。したがってこの発明では、後述する通板長さ
(酸洗浄液に接している長さ)を10m以下とし、上述
の連続焼鈍のライン速度の下限(30/min )とから、
酸洗浄時間(酸洗浄液に接触している時間)tの上限を
20秒以下とした。
In a continuous annealing line, the length of an acid cleaning device that can be installed in existing continuous annealing equipment is limited. On the other hand, even when a new line is installed, a compact design is required as much as possible. Line speed of continuous annealing of applied aluminum (30-200m /
min), acid cleaning for a long time is not suitable. In other words, when performing acid cleaning for a long time at a general continuous annealing line speed, the acid cleaning device becomes longer, and an acid cleaning device is provided between the continuous annealing furnace and the outlet accumulator in the existing continuous annealing line. Installation becomes difficult, and the line length becomes extremely long even for a newly installed line. Therefore, in the present invention, the passing length (length in contact with the acid cleaning liquid) described later is set to 10 m or less, and the lower limit (30 / min) of the line speed of the continuous annealing is set as follows.
The upper limit of the acid cleaning time (time in contact with the acid cleaning liquid) t was set to 20 seconds or less.

【0020】このように酸洗浄液接触時間tについて、
(1)式を満たしかつ20秒以下の条件とすることは、
図2中における斜線領域内に酸洗浄液接触時間t、酸洗
浄液温度Tを定めることを意味する。この図2から判る
ように、酸洗浄液温度Tは最低でも約65℃以上の高温
となるが、この発明の方法の場合、連続焼鈍時にアルミ
ニウム合金板に与えられた熱を有効利用することによっ
て、上述のような65℃以上の高温での酸洗浄でも、酸
洗浄液の加熱に要するエネルギが少なくて済む。すなわ
ち連続焼鈍炉においては、焼鈍の目的によっても異なる
が、アルミニウム合金板は通常は到達温度400〜60
0℃程度に加熱され、連続焼鈍炉内の冷却帯において冷
却されても焼鈍炉出口で通常は100〜250℃程度の
温度は保有している。したがって連続焼鈍後のアルミニ
ウム合金板を直ちに酸洗浄液中に浸漬もしくはスプレー
することによって酸洗浄液の接触温度も高くなるから、
酸洗浄液自体の加熱が不要となるか、または少なくとも
若干の加熱だけで足りるようになる。
As described above, regarding the contact time t of the acid cleaning solution,
When the condition (1) is satisfied and the condition is 20 seconds or less,
It means that the contact time t and the temperature T of the acid cleaning liquid are determined in the shaded area in FIG. As can be seen from FIG. 2, the temperature T of the pickling solution is at least as high as about 65 ° C. or more. In the case of the method of the present invention, the heat given to the aluminum alloy plate during the continuous annealing is effectively used. Even in the acid cleaning at a high temperature of 65 ° C. or more as described above, less energy is required for heating the acid cleaning liquid. That is, in a continuous annealing furnace, although it varies depending on the purpose of annealing, the aluminum alloy plate usually has an ultimate temperature of 400 to 60.
Even when it is heated to about 0 ° C. and cooled in a cooling zone in a continuous annealing furnace, it usually has a temperature of about 100 to 250 ° C. at the outlet of the annealing furnace. Therefore, by immediately dipping or spraying the aluminum alloy plate after continuous annealing in an acid cleaning solution, the contact temperature of the acid cleaning solution also increases,
The heating of the acid cleaning solution itself is not required, or at least a slight heating is sufficient.

【0021】酸洗浄液にアルミニウム合金板が接触して
いる時間、すなわち酸洗浄液中の通過時間もしくは酸洗
浄液スプレー帯の通過時間は、酸洗浴もしくはスプレー
帯における通板長さ(酸洗浄液に接している長さ)と連
続焼鈍のライン速度とによって定まるが、既存の連続焼
鈍設備に酸洗浄装置を付加する場合、前述のように通板
長さは最大でも10m程度と見積ることができる。そこ
で通板長さを10mとし、前述の(1)式の関係を酸洗
浄温度T(℃)とライン速度R(m・sec-1)の関係
に書き換えれば、(3)式が得られることになる。 log(10/R)≧3.6−3.5×10-2×T …(3) (3)式から、(4)式が得られる。 log(R-1)≧2.6−3.5×10-2×T …(4) この(4)式が満たされる場合には、酸洗浄通板長さが
10mの場合に必ず(1)式も満たされることになる。
また通板長さL(m)が10m以下の場合には、t=L
/Rとして(1)式を満たすように酸洗浄液の温度Tと
ライン速度Rとを定めることによって、MgOを主体と
する酸化膜の除去を確実に行なうことができる。
The time during which the aluminum alloy plate is in contact with the pickling solution, that is, the passage time in the pickling solution or the passing time in the pickling solution spray zone, is the length of the plate passing in the pickling bath or spray zone (contact with the pickling solution). Length) and the line speed of the continuous annealing, but when an acid washing device is added to the existing continuous annealing equipment, it is possible to estimate the threading length at a maximum of about 10 m as described above. Therefore, if the threading length is set to 10 m and the relation of the above equation (1) is rewritten to the relation between the acid cleaning temperature T (° C.) and the line speed R (m · sec −1 ), the equation (3) is obtained. become. log (10 / R) ≧ 3.6−3.5 × 10 −2 × T (3) From the expression (3), the expression (4) is obtained. log (R −1 ) ≧ 2.6−3.5 × 10 −2 × T (4) When the expression (4) is satisfied, the value ( 1 ) is always required when the pickling plate length is 10 m. ) Expression is also satisfied.
When the threading length L (m) is 10 m or less, t = L
By determining the temperature T of the acid cleaning liquid and the line speed R so as to satisfy the expression (1) as / R, it is possible to reliably remove the oxide film mainly composed of MgO.

【0022】またこの発明の方法において酸洗浄に用い
る溶液は、経済性や環境問題等から硫酸溶液が望ましい
が、MgOを主体とする酸化膜を短時間で除去可能な無
機酸であれば硫酸溶液に限られるものではなく、例えば
硫酸以外に硝酸や燐酸、あるいはこれらの混酸等を用い
ることができる。またこのような無機酸の溶液は、無機
酸の濃度が合計で1〜20wt%、pHが2以下が適当で
ある。なお充分な環境対策を講じれば、これら無機酸溶
液に弗素化合物を添加することによって反応を促進で
き、その場合には酸洗浄装置をさらにコンパクトにする
ことができる。
The solution used for acid cleaning in the method of the present invention is preferably a sulfuric acid solution from the viewpoint of economy and environmental problems. However, a sulfuric acid solution is preferable if it is an inorganic acid capable of removing an oxide film mainly composed of MgO in a short time. However, the present invention is not limited thereto, and for example, nitric acid, phosphoric acid, a mixed acid thereof, or the like can be used in addition to sulfuric acid. It is appropriate that the concentration of the inorganic acid is 1 to 20 wt% in total and the pH of the inorganic acid solution is 2 or less. If sufficient environmental measures are taken, the reaction can be promoted by adding a fluorine compound to these inorganic acid solutions, in which case the acid cleaning apparatus can be made more compact.

【0023】さらに、連続焼鈍後のアルミニウム合金板
に対しては直ちに酸洗浄を施しても良いが、合金板表面
に圧延油等の油脂分が残留していれば均一な酸洗浄が阻
害されるおそれがあるから、連続焼鈍後、酸洗浄前にリ
ン酸ソーダ、苛性ソーダ、オルソ珪酸ソーダ等を用いて
アルカリ脱脂を施すことが望ましい。そのためには、例
えば図1における連続焼鈍炉6と酸洗浄装置2との間
に、図示しないアルカリ脱脂槽を設けておけば良い。
Further, the aluminum alloy sheet after the continuous annealing may be immediately subjected to acid cleaning. However, if an oil or fat such as rolling oil remains on the surface of the alloy sheet, uniform acid cleaning is hindered. For this reason, it is preferable to perform alkali degreasing using sodium phosphate, sodium hydroxide, sodium orthosilicate, or the like after continuous annealing and before acid cleaning. For this purpose, for example, an alkaline degreasing tank (not shown) may be provided between the continuous annealing furnace 6 and the acid cleaning device 2 in FIG.

【0024】なおこの発明の方法においては、酸洗浄後
の処理については特に限定されるものではないが、通常
は酸洗浄後に表面に残留した酸溶液を水洗によって除去
してから乾燥させ、さらに表面の傷入り防止および防錆
のために潤滑油や防錆油を塗布するのが通常である。
In the method of the present invention, the treatment after the acid washing is not particularly limited. Usually, the acid solution remaining on the surface after the acid washing is removed by washing with water, followed by drying and further drying. It is usual to apply a lubricating oil or a rust-preventive oil to prevent scratching and rust prevention.

【0025】また連続焼鈍前の板製造プロセス、および
連続焼鈍の具体的条件等は、材質や製品板の用途等に応
じて任意に設定できるが、一般にはDC鋳造−均熱−熱
間圧延−冷間圧延によって所要の板厚とした圧延板、ま
たは連続鋳造−冷間圧延によって所定の板厚とした圧延
板に、アルカリ溶液や有機溶剤、温水等を用いて脱脂を
施してから連続焼鈍炉に導入するのが通常であり、また
連続焼鈍炉においては、400〜550℃程度に到達さ
せ、保持なしあるいは20秒程度以下の短時間保持とす
るのが通常である。そして連続焼鈍炉では、加熱雰囲気
として燃焼ガスもしくは加熱空気を用いるのが通常であ
る。
The sheet manufacturing process before the continuous annealing and the specific conditions of the continuous annealing can be arbitrarily set according to the material, the use of the product sheet, and the like. In general, DC casting—soaking—hot rolling— A continuous annealing furnace after degreasing a rolled sheet having a predetermined thickness by cold rolling or a rolled sheet having a predetermined thickness by continuous casting and cold rolling using an alkaline solution, an organic solvent, hot water, or the like. In a continuous annealing furnace, the temperature is usually raised to about 400 to 550 ° C., and is usually not held or held for a short time of about 20 seconds or less. In a continuous annealing furnace, it is usual to use a combustion gas or heated air as a heating atmosphere.

【0026】[0026]

【実施例】[実施例1] Mg4.5wt%、Cu0.3wt%を含有し、残部が
実質的にAlよりなるアルミニウム合金を、通常のDC
鋳造−均熱−熱間圧延−冷間圧延によって板厚1.0m
mの圧延板とした。この圧延板を有機溶剤(MEK)に
よって脱脂した後、連続焼鈍炉によって500℃×10
秒加熱して200℃まで空冷し、酸洗浄液としての50
〜90℃の硫酸水溶液(硫酸濃度10wt%、pH<
1)に2〜60秒浸漬した。酸洗浄後、純水により洗浄
して乾燥させた。乾燥後の板の表面層についてGDS分
析を行なって、深さ方向のMg,Al,Oの濃度分布を
求めて、表面附近のMg濃度のピークの有無から、Mg
Oを主体とする酸化膜の存在状況を調べた。
[Example 1] An aluminum alloy containing 4.5 wt% of Mg and 0.3 wt% of Cu, and the balance substantially consisting of Al was converted to a normal DC.
Casting, soaking, hot rolling, cold rolling
m rolled plate. After degreased with an organic solvent (MEK), the rolled plate was heated at 500 ° C. × 10 by a continuous annealing furnace.
Heat for 2 seconds and air-cool to 200 ° C.
Aqueous solution of sulfuric acid at ~ 90 ° C (sulfuric acid concentration 10wt%, pH <
It was immersed in 1) for 2 to 60 seconds. After acid cleaning, the substrate was washed with pure water and dried. GDS analysis was performed on the surface layer of the dried plate to determine the concentration distribution of Mg, Al, and O in the depth direction.
The existence state of the oxide film mainly composed of O was examined.

【0027】図2に、MgOを主体とする酸化膜の除去
状況(Mg濃度ピークの存在状況)と、酸洗浄時間(酸
洗浄液接触時間)および酸洗浄液の温度の関係を示す。
FIG. 2 shows the relationship between the removal state of the oxide film mainly composed of MgO (the presence state of the Mg concentration peak), the acid cleaning time (contact time with the acid cleaning liquid), and the temperature of the acid cleaning liquid.

【0028】図2に示されるように、酸洗浄液の温度T
と酸洗浄液接触時間tが直線Lの右上の領域、すなわち
前記(1)式を満たす場合に、MgOを主体とする酸化
膜をほぼ完全に除去することができた。なお図2におけ
る直線Lの右上の領域であれば、酸洗浄液接触時間が2
0秒を越える場合でももちろんMgO主体の酸化膜の完
全除去は行なわれたが、既に述べたように20秒を越え
る酸洗時間は実際の連続焼鈍ラインでは不都合を生じ
る。
As shown in FIG. 2, the temperature T of the pickling solution is
When the contact time t with the acid cleaning liquid was in the upper right region of the straight line L, that is, when the formula (1) was satisfied, the oxide film mainly composed of MgO could be almost completely removed. In the upper right area of the straight line L in FIG.
Even when the time exceeds 0 second, the oxide film mainly composed of MgO is completely removed. However, as described above, the pickling time exceeding 20 seconds causes inconvenience in an actual continuous annealing line.

【0029】[実施例2]前記実施例と同様にして連続
焼鈍後に酸洗浄を行なうにあたり、酸洗浄液に対する圧
延板の接触長さを10mで一定とし、連続焼鈍ライン速
度を0.3m/sec〜1.0m/secの範囲内で変
化させるとともに、酸洗浄液の温度を50〜90℃の範
囲内で変化させた。この場合、酸洗浄液の温度Tとライ
ン速度Rとの関係が(4)式を満たしている場合には、
MgOを主体とする酸化膜の除去を完全に行なうことが
できた。
Example 2 In performing acid cleaning after continuous annealing in the same manner as in the above example, the contact length of the rolled plate with the acid cleaning liquid was kept constant at 10 m, and the continuous annealing line speed was 0.3 m / sec or more. The temperature was changed within a range of 1.0 m / sec, and the temperature of the pickling solution was changed within a range of 50 to 90 ° C. In this case, when the relationship between the temperature T of the pickling solution and the line speed R satisfies the expression (4),
The oxide film mainly composed of MgO was completely removed.

【0030】[0030]

【発明の効果】以上の説明で明らかなように、この発明
の方法によれば、Mgを含有するアルミニウム合金板の
表面のMgOを主体とする酸化膜の除去のための酸洗浄
を、連続焼鈍ラインと同一ライン中で効率良く連続的に
行なうことができ、特に酸洗浄を適用することによる生
産性の低下もなく、しかも連続焼鈍ラインの通常のライ
ン速度を適用しつつ確実に酸化膜を除去できるととも
に、既存の連続焼鈍設備の大幅な改変を伴なうことなく
実施することができ、さらに連続焼鈍における加熱エネ
ルギを有効利用して高温での酸洗浄を行なうため、単に
酸化膜除去効率に優れるばかりでなく、酸洗浄液の加熱
のためのエネルギも削減することができ、したがってト
ータルとして熱利用効率が高くなり、トータル的なラン
ニングコストの低減を図ることができる。
As is apparent from the above description, according to the method of the present invention, the acid cleaning for removing the oxide film mainly composed of MgO on the surface of the aluminum alloy plate containing Mg is performed by continuous annealing. It can be carried out efficiently and continuously in the same line as the line, without any decrease in productivity especially by applying acid cleaning, and reliably removing oxide films while applying the normal line speed of the continuous annealing line It can be carried out without significant modification of existing continuous annealing equipment, and it is possible to carry out acid cleaning at high temperature by effectively utilizing the heating energy in continuous annealing. Not only is it excellent, it can also reduce the energy for heating the acid cleaning solution, thus increasing the total heat utilization efficiency and reducing the total running cost. It is possible to achieve.

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

【図1】この発明の方法に従って連続焼鈍と酸洗浄とを
同一ラインで行なうための設備の一例を示す略解図であ
る。
FIG. 1 is a schematic diagram showing an example of equipment for performing continuous annealing and acid cleaning on the same line according to the method of the present invention.

【図2】連続焼鈍後のMg含有アルミニウム合金板につ
いて酸洗浄を行なった場合の酸洗浄液温度および酸洗浄
時間(酸洗浄液接触時間)と、酸化膜除去状況との関係
を示す相関図である。
FIG. 2 is a correlation diagram showing a relationship between an acid cleaning liquid temperature and an acid cleaning time (an acid cleaning liquid contact time) and an oxide film removal state when an acid cleaning is performed on an Mg-containing aluminum alloy plate after continuous annealing.

【図3】図2に示されるデータを得るためのGDS分析
によるMg含有アルミニウム合金板表面層における深さ
方向のMg,Al,Oの濃度分布の代表例を示すグラフ
で、(A)は連続焼鈍後、酸洗浄前の板について示すグ
ラフ、(B)は連続焼鈍−酸洗浄後の板について示すグ
ラフである。
3 is a graph showing a typical example of a concentration distribution of Mg, Al, and O in a depth direction in a surface layer of an Mg-containing aluminum alloy plate by GDS analysis for obtaining data shown in FIG. FIG. 3 is a graph showing a sheet after annealing and before acid cleaning, and FIG. 3B is a graph showing a sheet after continuous annealing and acid cleaning.

【符号の説明】[Explanation of symbols]

1 連続焼鈍ライン 2 酸洗浄装置 6 連続焼鈍炉 Reference Signs List 1 continuous annealing line 2 acid cleaning device 6 continuous annealing furnace

フロントページの続き (72)発明者 林 公隆 千葉県富津市新富20−1 新日本製鐵株 式会社 技術開発本部内 (72)発明者 武岡 吉彦 東京都千代田区大手町2丁目6番3号 新日本製鐵株式会社内 (58)調査した分野(Int.Cl.6,DB名) C23G 3/02 Continued on the front page (72) Inventor Kimitaka Hayashi 20-1 Shintomi, Futtsu-shi, Chiba Nippon Steel Corporation Technology Development Headquarters (72) Inventor Yoshihiko Takeoka 2-6-3 Otemachi, Chiyoda-ku, Tokyo New Nippon Steel Corporation (58) Field surveyed (Int.Cl. 6 , DB name) C23G 3/02

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 Mgを0.3wt%以上含有するアルミニ
ウム合金板について連続焼鈍を施すにあたり、 連続焼鈍後のアルミニウム合金板を巻取る前に、その連
続焼鈍後のアルミニウム合金板を、酸洗浄液中もしくは
酸洗浄液スプレー帯中を通過させ、かつその通過中の酸
洗浄液接触時間を20秒以下に規制するとともに、接触
時間t(秒)と酸洗浄液の温度T(℃)との関係が、次
の(1)式 logt≧3.6−3.5×10-2×T …(1) を満たすように規制することを特徴とする、Mg含有ア
ルミニウム合金板の連続焼鈍・酸洗浄同一ライン処理方
法。
1. In performing continuous annealing on an aluminum alloy sheet containing 0.3 wt% or more of Mg, before winding the aluminum alloy sheet after continuous annealing, the aluminum alloy sheet after continuous annealing is placed in an acid cleaning solution. Alternatively, the solution is passed through an acid cleaning solution spray zone, and the acid cleaning solution contact time during the passage is regulated to 20 seconds or less, and the relationship between the contact time t (second) and the temperature T (° C.) of the acid cleaning solution is as follows. (1) Formula logt ≧ 3.6−3.5 × 10 −2 × T (1) A method for continuous annealing and acid cleaning of Mg-containing aluminum alloy sheets on the same line, characterized by regulation. .
【請求項2】 請求項1に記載の方法において、前記酸
洗浄液として、硫酸、硝酸もしくは燐酸の1種以上を合
計で1〜20wt%の濃度で含み、かつpHが2.0以下
のものを用いる、Mg含有アルミニウム合金板の連続焼
鈍・酸洗浄同一ライン処理方法。
2. The method according to claim 1, wherein the acid washing solution contains one or more of sulfuric acid, nitric acid and phosphoric acid at a total concentration of 1 to 20% by weight and has a pH of 2.0 or less. The same line processing method for continuous annealing and acid cleaning of the Mg-containing aluminum alloy plate used.
【請求項3】 請求項1に記載の方法において、連続焼
鈍後、アルミニウム合金板を酸洗浄液中もしくは酸洗浄
液スプレー帯に導入する前に、アルカリ脱脂を連続的に
行なう、Mg含有アルミニウム合金板の連続焼鈍・酸洗
浄同一ライン処理方法。
3. The method according to claim 1, wherein the alkali-degreasing is continuously performed after the continuous annealing before introducing the aluminum alloy plate into the pickling solution or into the pickling solution spray zone. Continuous annealing and acid cleaning same line processing method.
JP5062471A 1993-03-01 1993-03-01 Continuous annealing and acid cleaning same line processing method for Mg-containing aluminum alloy plate Expired - Fee Related JP2983404B2 (en)

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