JPH0320487A - Surface treatment of long-size material - Google Patents

Surface treatment of long-size material

Info

Publication number
JPH0320487A
JPH0320487A JP15494689A JP15494689A JPH0320487A JP H0320487 A JPH0320487 A JP H0320487A JP 15494689 A JP15494689 A JP 15494689A JP 15494689 A JP15494689 A JP 15494689A JP H0320487 A JPH0320487 A JP H0320487A
Authority
JP
Japan
Prior art keywords
pickling
tank
descaling
steel strip
pickling 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.)
Granted
Application number
JP15494689A
Other languages
Japanese (ja)
Other versions
JPH0577752B2 (en
Inventor
Yoshinobu Nakane
中根 義信
Hideo Tatemichi
立道 英夫
Shohei Tanaka
田中 昌平
Kazusato Tanaka
田中 和里
Fumio Tomimatsu
冨松 文男
Takeshi Takahashi
武士 高橋
Hideaki Yoshimura
吉村 秀昭
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP15494689A priority Critical patent/JPH0320487A/en
Publication of JPH0320487A publication Critical patent/JPH0320487A/en
Publication of JPH0577752B2 publication Critical patent/JPH0577752B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • C23G3/02Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
    • C23G3/021Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously by dipping

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

PURPOSE:To effectively carry out descaling treatment by allowing a steel strip to travel at high speed while pressing a pickling solution into a pickling tank confined in space at the time of passing a steel strip through a pickling solution and exerting descaling. CONSTITUTION:A pickling solution, such as aqueous solution of HCl, is pressed via press-in nozzles 8a, 8b into a pickling tank 2 confined in space, and a steel strip 1 after annealing is allowed to travel at high speed in a state where fluid pressure is formed in the whole region of the pickling tank 2, by which oxide scales on the steel-strip surface are dissolved by means of the pickling solution and removed. Plural staggeredly arranged skids 10 are provided in the pickling tank 2 and also discharge holes 9 for the pickling solution are provided in the bottom of the pickling tank 2, by which the pickling solution is formed into the state of turbulent flow in the tank 2 without forming voids free from the pickling solution in the pickling tank 2. Since, consequently, the steel-strip 1 surface is free from the associated flow of the pickling solution and a fresh pickling solution is always supplied, descaling reaction is accelerated and the descaling treatment for the steel strip can be effectively performed by a small device and with small amounts of pickling solution.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は長尺材料の表面処理方法に関し、たとえば鋼板
を酸洗処理して脱スケールを行なう様な場合に、脱スケ
ールを効率良く遂行し得る様に改善された方法に関する
ものであるi尚木発明は連続的に走行させながら処理す
ることのできる種々の長尺材料の・表面処理法として広
く活用することができるが、以下の説明では鋼帯を連続
的に酸洗処理して脱スケールを行なう場合を代表的にと
り上げて説明,する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for surface treatment of long materials. For example, when a steel plate is descaled by pickling, it is possible to efficiently perform descaling. The Naoki invention, which relates to an improved method for obtaining a surface treatment, can be widely used as a surface treatment method for various long materials that can be treated while continuously running. The following is a representative example of a case in which a steel strip is descaled by continuous pickling treatment.

[従来の技術] W4帯の連続生産に当たっては、熱間圧延や玲間圧延工
程あるいは歪取り焼鈍工程等で生成する表面のスケール
を除去して清浄化するため、最終工程で酸洗による脱ス
ケール処理が行なわれる。この脱スケール処理法として
現在汎用されているのは、濃度が15〜20%程度の加
熱塩酸(85〜95℃程度)を酸洗液とする方法であり
、連tA処理の具体的な方法としては、■加熱塩酸の装
入された複数の酸洗槽に銅帯を浸漬させながら連続的に
走行させるディピング法(酸洗槽を浅めにしたSHAL
LOW法もこの方法に含まれる)と、■走行する#fの
両面に加熱塩酸を噴射するスプレー法があるが、この中
でも現在のところは前者の浸漬法が主流となっている。
[Prior art] In continuous production of W4 strips, descaling by pickling is carried out in the final process to remove and clean the surface scale generated during hot rolling, rolling process, strain relief annealing process, etc. Processing is performed. The currently widely used method for this descaling treatment is to use heated hydrochloric acid (approximately 85 to 95°C) with a concentration of about 15 to 20% as the pickling solution. ■The dipping method in which the copper strip is continuously run while immersed in multiple pickling tanks charged with heated hydrochloric acid (SHAL with shallow pickling tanks)
(The LOW method is also included in this method) and (2) a spray method in which heated hydrochloric acid is injected onto both surfaces of the running #f, but among these methods, the former dipping method is currently the mainstream.

第2図はこの浸漬法を例示する概念図であり、鋼帯1の
走行方向に沿って酸洗4i2a,2b,・・・2y,2
zが直列に配置されており、最下流側の酸洗相2Zに酸
洗液供給ボンブ3から酸洗液を供給し、該酸洗槽2Zか
らオーバーフローした酸洗液は中間槽4を経た後送給ボ
ンプ5によってその上流側の酸洗41 2 yへ送り、
同様にして酸洗液は順次上流側の酸洗槽へ送られた後、
最上流側の酸洗49 2 aから排出される。そして鋼
帯1はガイドロール6によって酸洗41 2 a , 
 2 b ・・・2 y , 2 zの順に浸漬走行し
、この間に銅帯表面の酸化物は熱塩酸により除去される
.最下流側の酸洗槽2zを出た鋼f1はリンス装置(図
示せず)により酸洗液を除去した後乾燥して巻取られる
FIG. 2 is a conceptual diagram illustrating this dipping method, in which pickling 4i2a, 2b, . . . 2y, 2
z are arranged in series, the pickling liquid is supplied from the pickling liquid supply bomb 3 to the pickling phase 2Z on the most downstream side, and the pickling liquid overflowing from the pickling tank 2Z passes through the intermediate tank 4. The feed pump 5 sends it to the pickling 41 2 y on the upstream side,
In the same way, the pickling liquid is sequentially sent to the upstream pickling tank, and then
It is discharged from the pickling 49 2 a on the most upstream side. Then, the steel strip 1 is pickled by the guide roll 6 41 2 a ,
2 b . . . 2 y , 2 z are immersed in this order, and during this time oxides on the surface of the copper strip are removed with hot hydrochloric acid. The steel f1 that has exited the pickling tank 2z on the most downstream side has the pickling liquid removed by a rinsing device (not shown), then is dried and wound up.

[発明が解決しようとする課題] ところが図示した様なディッピング法は、脱スケール速
度の点で必ずしも満足し得るものではなく、十分な脱ス
ケールを達成するには銅帯の走行速度を落とすか、ある
いは酸洗槽の数を増やしたり個々の酸洗槽を長尺にしな
ければならず、それに伴って生産性が低下し、あるいは
酸洗設備が長くなるという問題が生じてくる。そこでこ
うした問題を回避し脱スケール速度を高める為の手段と
して、■酸洗前の鋼帯を予備加熱しておく方法、あるい
は■鋼帯にメカニカルデスケラー処理、テンション付与
、スキンバス処理等を施してスケールに亀裂を生ぜしめ
、その後の脱スケールを容易にする方法が実施されてい
る。しかしこれらの方法では、銅帯の予熱あるいは脱ス
ケール促進の為の予備処理(デスケラτ処理等)に特別
の設備が必要になるので、設備費が高くなるばかりでな
く、工程管理も煩雑になる。
[Problem to be solved by the invention] However, the dipping method as illustrated is not necessarily satisfactory in terms of descaling speed, and in order to achieve sufficient descaling, it is necessary to reduce the running speed of the copper strip or to reduce the running speed of the copper strip. Alternatively, the number of pickling tanks must be increased or the length of each pickling tank must be increased, resulting in problems such as decreased productivity or lengthened pickling equipment. Therefore, as a means to avoid these problems and increase the descaling rate, there are two methods: 1) Preheating the steel strip before pickling, 2) Applying mechanical descaler treatment, tensioning, skin bath treatment, etc. to the steel strip. A method has been implemented in which cracks are created in the scale to facilitate subsequent descaling. However, these methods require special equipment for preheating the copper strip or for preliminary treatment to promote descaling (descaler τ treatment, etc.), which not only increases equipment costs but also complicates process control. .

そこでディッピング法の改善法として後述する様なター
ブランス(Turbulance)方式の酸洗法が開発
されたが、この方式でも期待される程の洗浄力向上効果
は得られていない。
Therefore, as a method for improving the dipping method, a turbulence pickling method, which will be described later, was developed, but even this method has not been able to achieve the expected effect of improving cleaning power.

本発明はこの様な事情に着目してなされたものであって
、その目的は、簡単な設備および工程で脱スケールを効
率良く行なうことのできる方法を提供し、また脱スケー
ルに限らず他の様々の表面処理にも適用できる様な方法
を提供しようとするものである。
The present invention was made in view of these circumstances, and its purpose is to provide a method that can efficiently descale with simple equipment and processes, and to provide a method that can be used not only for descaling but also for other purposes. The purpose is to provide a method that can be applied to various surface treatments.

[課題を解決するための手段] 上記課題を解決することのできた本発明に係る表面処理
法の構成は、狭小空間内に処理液を加圧導入し、該狭小
空間内の全域において液圧を形成した状態で任意部位よ
り該処理液を系外へ放出させる様に制御しつつ、該狭小
空間内に長尺材料を高速走行させるところに要旨を有す
るものである。
[Means for Solving the Problems] The structure of the surface treatment method according to the present invention that can solve the above problems involves introducing a treatment liquid under pressure into a narrow space and applying liquid pressure throughout the narrow space. The gist of this method is to run a long material at high speed within the narrow space while controlling the processing liquid to be discharged from any part of the system in the formed state.

[作用] 本発明者らは前述の様な従来技術の問題点に鑑み、ディ
ッピング法による脱スケール処理効率が期待されるほど
上がらない理由を明確にしようとして色々検討を行なっ
た。その結果、酸洗槽における鋼帯の走行状態と酸洗液
の流動状態により酸洗効果(即ち脱スケール効果)に顕
著な違いが生じてくることが確認された.即ち第3図は
、従来のディッピング法を採用したときの1つの酸洗槽
2内における鋼帯1と酸洗液Lの流れ状況を示す模式図
であり、鋼帯lは酸洗槽2内の酸洗液L中を白抜き矢印
方向へ高速走行しながら酸洗されるものとする。
[Function] In view of the problems of the prior art as described above, the present inventors conducted various studies in an attempt to clarify the reason why the descaling efficiency by the dipping method is not as high as expected. As a result, it was confirmed that the pickling effect (i.e. descaling effect) significantly differs depending on the running condition of the steel strip in the pickling tank and the flow condition of the pickling solution. That is, FIG. 3 is a schematic diagram showing the flow situation of the steel strip 1 and the pickling liquid L in one pickling tank 2 when the conventional dipping method is adopted. It is assumed that the pickling process is carried out while traveling at high speed in the pickling liquid L in the direction of the white arrow.

今、鋼帯1が酸洗液L中を高速で走行すると、開放され
た酸洗楢2内の粘性を持った酸洗液Lは、鋼帯1の走行
に伴なって随伴流を形成し、鋼帯1の走行方向に沿って
流動する。その結果、酸洗液Lは層流に近い流動状態を
示すことになる。
Now, when the steel strip 1 runs through the pickling solution L at high speed, the viscous pickling solution L in the open pickling cage 2 forms an accompanying flow as the steel strip 1 runs. , flows along the running direction of the steel strip 1. As a result, the pickling liquid L exhibits a fluid state close to laminar flow.

モして鋼帯1に近接して流動する酸洗液Lは、脱スケー
ル反応(F6203 ” 6}ICI= 2FeC13
 ” 3}+20またはFeO + 2HCl4 Fe
C12 + }1,0)により洗浄活性が低下し、ある
いは洗浄活性を失った後もそのまま鋼帯1付近を流動す
ることになり、wI%F1から離れた位置に存在する新
鮮な(洗浄活性を持った)洗浄液が鋼帯l付近へ流入し
てくるのを妨げることになり、脱スケール効果が徐々に
低下してくるものと思われる。またこの様に新鮮な洗浄
液が鋼帯1付近へ移行しにくくなるということは、加熱
された洗浄液により鋼帯1の表面を加熱して洗浄力を高
めようとする場合の熱伝達も阻害されることになり、洗
浄効率は更に低下してくる。
The pickling liquid L flowing close to the steel strip 1 undergoes a descaling reaction (F6203''6}ICI=2FeC13
” 3}+20 or FeO + 2HCl4 Fe
C12 + }1,0), or even after losing the cleaning activity, it continues to flow near the steel strip 1, and the fresh (with no cleaning activity) existing at a position away from wI%F1 It is thought that this prevents the cleaning liquid (which was carried by the descaling process) from flowing into the vicinity of the steel strip 1, and the descaling effect gradually decreases. In addition, this difficulty in moving fresh cleaning liquid to the vicinity of steel strip 1 also impedes heat transfer when trying to increase cleaning power by heating the surface of steel strip 1 with heated cleaning fluid. As a result, the cleaning efficiency further decreases.

これに対しターブランス(Turbulance)方式
の酸洗法は、たとえば第4図に略示する如く酸洗槽2を
浅めに構成すると共に、上M7によって酸洗[2の上部
を封鎖したものであり、この場合酸洗液Lは第3図で説
明したのと同様の随伴流を形成するが、上M7により随
伴流が乱されるため、第2図の例に比べると酸洗液Lが
拡散し易くなり、酸洗効果は若干高められる。即ち木例
では酸洗槽2が浅めに構成されており、上M7が鋼帯1
からあまり離れておらず、また高速走行する鋼帯1に対
し上M7は静止している。その為、上M7付近の随伴流
は該上M7の壁面抵抗を受けて鋼帯1付近の随伴流より
も遅くなり、それにより随伴流が乱されて乱流気味の流
れを生ずるためと考えられる。
On the other hand, in the turbulence pickling method, the pickling tank 2 is configured to be shallow as shown schematically in FIG. In this case, the pickling liquid L forms an accompanying flow similar to that explained in Fig. 3, but because the accompanying flow is disturbed by the upper M7, the pickling liquid L is more diffused than in the example of Fig. 2. The pickling effect is slightly enhanced. That is, in the wooden example, the pickling tank 2 is configured to be shallow, and the upper M7 is the steel strip 1.
The upper M7 is stationary compared to the steel strip 1 which is not far away from the steel strip 1 and is traveling at high speed. Therefore, the accompanying flow near the upper M7 is slower than the accompanying flow near the steel strip 1 due to the wall resistance of the upper M7, and this is thought to cause the accompanying flow to be disturbed and produce a somewhat turbulent flow. .

ところがこのターブランス方式でも当初期待したほどの
洗浄効果は得られず、その原因として次の様な事実が確
認された.即ちこの方式では比較的狭い酸洗槽2内を通
して鋼帯1を高速走行させるため、酸洗液Lは随伴流に
よって鋼帯1の走行方向へ押しやられ、たとえば第5図
に示す如く酸洗槽2における鋼帯1の走行方向上流側に
空陳Sができる.そしてこの空陳Sに面した酸洗液Lの
液面は上M7の壁面抵抗を受けないので、この部分にお
ける酸洗液Lの随伴流はあまり乱されず、この部分は準
層流状態となって酸洗液Lの拡散が不十分となり、第3
図で説明したのと同様の理由で洗浄効果が上がらなくな
るものと思われた。
However, even with this turbulence method, the cleaning effect that was initially expected was not obtained, and the following facts were confirmed as the cause. That is, in this method, since the steel strip 1 is run at high speed through a relatively narrow pickling tank 2, the pickling liquid L is pushed in the running direction of the steel strip 1 by the accompanying flow, and for example, as shown in FIG. A void S is formed on the upstream side in the running direction of the steel strip 1 at 2. Since the liquid surface of the pickling liquid L facing this empty surface S is not subjected to wall resistance of the upper M7, the accompanying flow of the pickling liquid L in this part is not disturbed much, and this part is in a quasi-laminar flow state. As a result, the diffusion of the pickling liquid L becomes insufficient, and the third
It was thought that the cleaning effect would not improve for the same reason as explained in the figure.

そこで本発明者らはターブランス方式に見られる上記空
MSができない様にすれば、酸洗4!2の長手方向全域
で酸洗液Lの拡散が十分に行なわれ、酸洗効果が高めら
れるという確信を持って更に研究を進めた結果、前記本
発明の構成に想到したものである。
Therefore, the present inventors believe that if the above-mentioned empty MS seen in the turbulence method is prevented from occurring, the pickling liquid L will be sufficiently diffused throughout the longitudinal direction of the pickling 4!2, and the pickling effect will be enhanced. As a result of further research with confidence, we came up with the configuration of the present invention.

即ち本発明では、前述の如く狭小な空間(即ち酸洗槽)
内に酸洗液を加圧導入し、該酸洗槽内の全域に液圧を形
成することによって、前記第5図に示゛した様な空隙S
ができない様にし、それにより酸洗槽内の長手方向全体
に酸洗液の随伴流に対する壁面抵抗を作用させることに
よって乱流状態とする。その結果、酸洗液しは酸洗槽の
長手方向全域で酸洗液Lの拡散が十分に進行し、また熱
伝達も効率良く進行することとなり、酸洗効率は大幅に
高められる。
That is, in the present invention, as mentioned above, the narrow space (i.e. pickling tank)
By introducing the pickling liquid under pressure into the pickling tank and creating liquid pressure in the entire area inside the pickling tank, a gap S as shown in FIG. 5 is created.
This creates a turbulent flow state by applying wall resistance to the accompanying flow of the pickling solution throughout the length of the pickling tank. As a result, the pickling liquid L is sufficiently diffused throughout the length of the pickling tank, and heat transfer is also carried out efficiently, so that the pickling efficiency is greatly increased.

第1図(A)〜(C)は本発明で使用する酸洗装置を例
示する概略説明図であり、第1図(A)は縦断面図、第
1図(B)は上M7を取り外した状態の平面図、第1図
(C)は第1図(A)のc−c線縦断面相当図であり、
この装置はたとえば3〜8m程度の長尺なものとして製
作される。図中1は鋼帯、2は酸洗槽、7は上蓋、8a
,8bは酸洗液L圧入用スリットノズル、9は排液口、
10は千鳥状に配置されたスキットを夫々示す。
FIGS. 1(A) to (C) are schematic explanatory diagrams illustrating the pickling device used in the present invention, FIG. 1(A) is a longitudinal sectional view, and FIG. 1(B) is a diagram with upper M7 removed. FIG. 1(C) is a plan view corresponding to the longitudinal cross-section taken along the line c-c of FIG. 1(A).
This device is manufactured as a long device, for example, about 3 to 8 m. In the figure, 1 is the steel strip, 2 is the pickling tank, 7 is the upper lid, 8a
, 8b is a slit nozzle for press-fitting pickling liquid L, 9 is a drain port,
10 shows skits arranged in a staggered manner.

この装置を用いて酸洗を行なうに当たっては、狭小な酸
洗!M2内にスリットノズル8a,8b6xら酸洗液L
を加圧導入し、酸洗禮2の全域に液圧を形成することに
よって、酸洗槽2内に第5図で説明した様な空隙Sが形
成されるのを防止しつつ、鋼帯1を高速走行させる。そ
うすると、酸洗液Lは鋼帯1の走行方向に随伴流を形戊
するが、酸洗槽2は狭小に構成されており、鋼帯1の走
行位置に対し壁面が近い位置に存在するので、壁面側の
随伴流は抵抗を受けて流速が抑えられ、前記第4図で説
明したのと同様の理由で酸洗液Lは乱流状態となる。そ
の結果、鋼1l:1付近の酸洗液Lは常に新鮮なものと
置き代えられことになり、酸洗による前述の脱スケール
反応は効率良く進行する。しかも本発明では、酸洗液L
の加圧導入により酸洗槽2内全域に液圧が加えられるの
で、前記第5図で説明した様な空隙Sが酸洗禮2内にで
きることもなく、酸洗槽2内の全域に乱流状態が与えら
れることになり、全長に亘って酸洗を効率良く進めるこ
とが可能になる。尚、図示例では酸洗液Lを酸洗糟2の
前後端に設けたスリットノズル8a.8bから圧入する
例を示したが、圧入位置は勿論この例に限定される訳で
はなく、上M7や底面の適所から圧入することも可能で
あり、要は酸洗禮2全域に液圧を作用させて空隙を作ら
ない限りどの様な圧人手段を採用してもよい。また酸洗
液Lは底面や側壁の適所に設けた排液口9から、随時排
出することにより、酸洗液Lの酸洗力を高位に保持する
。尚上蓋7には、酸洗液Lの流れを阻害しない程度で邪
魔板を取り付けて酸洗液の乱流を促進することも有効で
ある。尚酸洗槽内の酸洗液に生ずる液圧は銅帯の走行速
度によって変わってくるので、この圧力に打ち勝つだけ
の圧力で酸洗液を導入することにより酸洗槽内に前述の
様な空隙Sができるのを防止することができる。
When performing pickling using this device, be sure to use a narrow pickling area! Pickling liquid L from slit nozzles 8a, 8b6x in M2
By introducing pressure into the pickling tank 2 and creating liquid pressure in the entire area of the pickling tank 2, the steel strip 1 is prevented from being formed in the pickling tank 2 as shown in FIG. Drive at high speed. In this case, the pickling liquid L forms an accompanying flow in the running direction of the steel strip 1, but the pickling tank 2 is constructed narrowly and the wall surface is located close to the running position of the steel strip 1. The flow rate of the accompanying flow on the wall side is suppressed due to resistance, and the pickling liquid L becomes turbulent for the same reason as explained in FIG. 4 above. As a result, the pickling liquid L in the vicinity of 1l:1 of the steel is always replaced with fresh one, and the above-mentioned descaling reaction by pickling proceeds efficiently. Moreover, in the present invention, the pickling liquid L
Since liquid pressure is applied to the entire area inside the pickling tank 2 by introducing pressure, the gap S as explained in FIG. This condition allows pickling to proceed efficiently over the entire length. In the illustrated example, the pickling liquid L is supplied through slit nozzles 8a. Although we have shown an example of press-fitting from 8b, the press-fitting position is of course not limited to this example, and it is also possible to press-fit from the upper M7 or an appropriate position on the bottom. Any pressure means may be used as long as it does not create a gap. In addition, the pickling liquid L is discharged from drain ports 9 provided at appropriate positions on the bottom and side walls at any time to maintain the pickling power of the pickling liquid L at a high level. It is also effective to attach a baffle plate to the upper lid 7 to the extent that the flow of the pickling liquid L is not obstructed to promote turbulent flow of the pickling liquid. The liquid pressure generated in the pickling solution in the pickling tank varies depending on the running speed of the copper strip, so by introducing the pickling solution with enough pressure to overcome this pressure, the above-mentioned pressure can be created in the pickling tank. The formation of voids S can be prevented.

第1図(A)〜(C)に示した装置は本発明で使用され
る好ましい装置の1例を示しただけのものであって、も
とより本発明を制限する性格のものではなく、要は狭小
な酸洗槽内の全域に酸洗液の液圧が作用する様に酸洗?
1t Lを加圧導入しつつ、鋼帯1を高速走行させ得る
ものであれば、装置の具体的な構成は任意に設計変更す
ることができる。
The devices shown in FIGS. 1(A) to (C) are merely examples of preferred devices used in the present invention, and are not intended to limit the present invention. Pickling so that the liquid pressure of the pickling liquid acts on the entire area inside the narrow pickling tank?
The specific configuration of the device can be arbitrarily changed as long as it allows the steel strip 1 to travel at high speed while introducing 1 t L under pressure.

[実施例] 次に本発明の効果を確認するため次の様な実験を行なっ
た。
[Example] Next, the following experiment was conducted to confirm the effects of the present invention.

即ち第1図(A)〜(C)に示した様な酸洗4!(幅:
300mm.銅帯走行位置と上蓋下面間のギャップ:1
50a+m)を使用し、幅200mmX厚み2mmの鋼
帯(CAL材二連続焼鈍向け材)を脱スケールすること
とし、そのときの塩酸濃度.酸洗時問,温度等を変えた
場合の脱スケール効果を、従来のディッピング方式を採
用したときの脱スケール効果と比較した。
That is, pickling 4 as shown in FIGS. 1(A) to (C)! (width:
300mm. Gap between copper band running position and bottom surface of top cover: 1
50a+m) was used to descale a steel strip of width 200mm x thickness 2mm (material for CAL material double continuous annealing), and the hydrochloric acid concentration at that time. The descaling effect when changing the pickling time, temperature, etc. was compared with the descaling effect when a conventional dipping method was adopted.

まず第6図(A)〜(D)は、酸洗温度を85℃に設定
し、脱スケール促進のためテンションレベラーによって
銅帯に加えられる伸び率をO%,1%.3%.5%に変
えた場合について、酸洗時間および塩酸濃度と脱スケー
ル所要時間(&iA−IIF表面の黒いスケールが肉眼
観察できなくなるまでの時間)の関係を示したものであ
る。
First, in FIGS. 6(A) to 6(D), the pickling temperature is set at 85°C, and the elongation rate applied to the copper strip by a tension leveler to promote descaling is 0%, 1%. 3%. The figure shows the relationship between the pickling time, hydrochloric acid concentration, and the time required for descaling (the time until the black scale on the surface of &iA-IIF can no longer be observed with the naked eye) when the acid pickling time was changed to 5%.

第6図(A)〜(D)からも明らかな様に、本発明法と
従来のディッピング法を比較すると、本発明法は特に塩
酸濃度の低い領域で優れた脱スケール効果を示しており
、塩酸濃度をかなり下げた場合でも十分な脱スケール効
果を享受し得ることが分かる. 次に第7図(A> .  (B)は上記方法に準拠し、
脱スケール促進のためテンションレベラーにより酸洗前
の鋼帯に与えられる伸び率を変えた場合の効果を、本発
明法と従来のディッピング法につき対比して示したグラ
フである。
As is clear from FIGS. 6(A) to (D), when the method of the present invention is compared with the conventional dipping method, the method of the present invention shows an excellent descaling effect especially in the region of low hydrochloric acid concentration. It can be seen that a sufficient descaling effect can be obtained even when the hydrochloric acid concentration is considerably lowered. Next, FIG. 7 (A>.(B)) is based on the above method,
1 is a graph showing the effect of changing the elongation rate given to a steel strip before pickling by a tension leveler in order to promote descaling, comparing the method of the present invention and the conventional dipping method.

このグラフからも明らかである様に、本発明法[第7図
(A)]では伸び率を変えた場合でも脱スケール所要時
間は殆ど変わっていないの(対じ、従来のディッピング
法[第7図(B)]の場合は伸び率によって脱スケール
所要時間はかなり異ってきており、この傾向は塩酸濃度
を下げたときに顕著に表われている。即ちこれらの結果
より、本発明を採用すれば、脱スケール促進の為の予m
処理(スケール膜に亀裂を与える為の処理)を省略した
場合でも優れた脱スケール効果を享受し得ることが分か
る。
As is clear from this graph, in the method of the present invention [Figure 7 (A)], the time required for descaling hardly changes even when the elongation rate is changed (in contrast, in the conventional dipping method [Figure 7 In the case of Figure (B)], the time required for descaling varies considerably depending on the elongation rate, and this tendency becomes more noticeable when the hydrochloric acid concentration is lowered.In other words, from these results, it is clear that the present invention was adopted. If so, preparations for promoting descaling can be made.
It can be seen that an excellent descaling effect can be obtained even when the treatment (treatment for cracking the scale film) is omitted.

第8図は、塩酸濃度を3.0%、温度を85℃、テンシ
ョンレベラーによって加えられる伸び率を5%、酸洗槽
のギャップを60mm、槽内における塩酸の流速を1.
0m/secに設定した他は前述の方法と同様にして、
鋼帯を予備加熱(85℃)した場合と予備加熱しなかっ
た場合について酸洗時間と脱スケール率の関係を調べた
結果を示したものである。
In Figure 8, the hydrochloric acid concentration is 3.0%, the temperature is 85°C, the elongation rate applied by the tension leveler is 5%, the gap in the pickling tank is 60 mm, and the flow rate of hydrochloric acid in the tank is 1.
Same as the above method except that it was set to 0m/sec,
This figure shows the results of investigating the relationship between pickling time and descaling rate for cases where the steel strip was preheated (85° C.) and cases where the steel strip was not preheated.

この図からも明らかである様に、本発明法を採用した場
合でも、酸洗時間の短いとき(即ち脱スケールの初期段
階)には、予備加熱により脱スケール率が若干高くなっ
ているが、酸洗時間の末期(脱スケールの後半)になる
と予備加熱の有無をによる脱スケール率の差は全くなく
なっている。即ちこの図より、本発明によれば、通常の
酸洗時間を採用する限る銅帯の予熱をせずども十分な脱
スケール効果が得られることを確認できる。
As is clear from this figure, even when the method of the present invention is adopted, the descaling rate is slightly higher due to preheating when the pickling time is short (i.e., in the initial stage of descaling), but At the end of the pickling time (the second half of descaling), there is no difference in the descaling rate between the presence and absence of preheating. That is, from this figure, it can be confirmed that according to the present invention, a sufficient descaling effect can be obtained without preheating the copper strip as long as the usual pickling time is used.

次に第9図は、塩酸濃度を3.0%,温度を85℃、テ
ンションレベラーによる伸び率を3%、鋼帯の予熱なし
、の条件を設定し、塩酸の導入圧力を調整して酸洗槽内
を満水状態にした場合(本発明法)と、第5図に示した
様に酸性槽の上流側に空隙Sを形成した場合(比較例)
について、酸洗時間を脱スケール率の関係を調べた結果
を示したものである。
Next, in Figure 9, the following conditions are set: the hydrochloric acid concentration is 3.0%, the temperature is 85°C, the elongation rate by the tension leveler is 3%, and the steel strip is not preheated. When the inside of the washing tank is filled with water (method of the present invention) and when a void S is formed on the upstream side of the acid tank as shown in Fig. 5 (comparative example)
This figure shows the results of investigating the relationship between pickling time and descaling rate.

この図からも明らかである様に、酸洗槽内に空隙Sがで
きるか否かによって脱スケール効果は著しく変わり、酸
洗槽内の液圧を略大気圧状態にして空陣Sができる様な
条件(比較例)の場合の脱スケール効果はかなり低いの
に対し、酸洗槽内の液圧を高めて空隙Sができない様に
したとき(本発明)の脱スケール効果は非常に優れたも
のであることが分かる。
As is clear from this figure, the descaling effect changes significantly depending on whether or not voids S are created in the pickling tank. The descaling effect was quite low under these conditions (comparative example), whereas the descaling effect was very good when the liquid pressure in the pickling tank was increased to prevent the formation of voids S (the present invention). I can see that it is something.

[発明の効果] 本発明は以上の様に構成されており、狭小な酸洗禮内に
酸洗液を加圧導入し、該槽内に空隙かで\ない様な条件
で銅帯を高速走行させて酸洗を行なうことにより、脱ス
ケールを極めて効率良く遂行することができる。しかも
この方法を採用すれば、脱スケール促進の為の予備処理
(テンションレベラーによる延伸やデスケラー処理等)
が不要になるばかりでなく、鋼帯の予熱も不要となり、
更には酸洗の為の酸濃度も下げることができ、工程を簡
潔化すると共に酸消費量も少なくすることができる. また本発明は、先に説明した様に洗浄槽内に生ずる洗浄
液の随伴流を乱して乱流状態とし、槽内における洗浄液
の拡散をよくすることによって前述の様な効果を発揮さ
せるものであり、こうした作用効果からも容易に理解で
きる様に、本発明は図示した様な銅帯の脱スケール処理
に限定されず、種々の長尺金属材の脱脂、アルカリ処理
等の表面処理をはじめ、プラスチック材等様々の表面処
理にも広く応用することができる。
[Effects of the Invention] The present invention is constructed as described above, and the pickling liquid is introduced under pressure into a narrow pickling tank, and the copper strip is run at high speed under conditions such that there are no voids in the tank. By carrying out pickling, descaling can be carried out extremely efficiently. Moreover, if this method is adopted, preliminary treatment to promote descaling (stretching with a tension leveler, descaling treatment, etc.)
Not only does this eliminate the need for preheating the steel strip,
Furthermore, the acid concentration for pickling can be lowered, simplifying the process and reducing acid consumption. Further, as explained above, the present invention disturbs the accompanying flow of the cleaning liquid that occurs in the cleaning tank to create a turbulent flow state, and improves the diffusion of the cleaning liquid in the tank, thereby achieving the above-mentioned effects. As can be easily understood from these effects, the present invention is not limited to the descaling treatment of copper strips as shown in the figure, but also includes surface treatments such as degreasing and alkali treatment of various long metal materials. It can also be widely applied to various surface treatments such as plastic materials.

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

第1図(^)〜(C)は本発明で使用される酸洗装置を
例示するもので、第1図(A)は概略縦断面図、第1図
(B)は上蓋を開放して示す概略平面図、第1図(C)
は第1図(A)におけるC−C線縦断面相当図である。 第2図は従来のディッピング式酸洗法を示す概念図、第
3図は該ディッピング式酸洗法を採用したときの酸洗状
況を示す説明図、第4.5図はターブランス方式の酸洗
状況を示す説明図、第6図(A)〜(D)は本発明法と
ディッピイング法を採用した場合の塩酸濃度と酸洗時間
の関係を対比して示すグラフ、第7図(A) , (B
)は本発明法とディッピング法を採用したときの伸び率
と酸洗時間の関係を示すグラフ、第8図は酸洗前の予備
加熱の有無と脱スケール率の関係を示すグラフ、第9図
は酸洗禮内における空隙Sの有無が脱スケール率に及ぼ
す影響を示すグラフである。 1・・・鋼帯     2・・・酸洗槽7・・・上ii
      8a, 8b・・・スリットノズル9・・
・排液口    lO・・・スキットL・・・酸洗液 第6茜(A) 第6図(B)
Figures 1 (^) to (C) illustrate the pickling apparatus used in the present invention, with Figure 1 (A) being a schematic vertical cross-sectional view and Figure 1 (B) showing the pickling device with the top lid open. Schematic plan view shown in Figure 1 (C)
is a view corresponding to a longitudinal cross-section taken along the line CC in FIG. 1(A). Figure 2 is a conceptual diagram showing the conventional dipping type pickling method, Figure 3 is an explanatory diagram showing the pickling situation when the dipping type pickling method is adopted, and Figure 4.5 is a turbulence type pickling method. Explanatory diagrams showing the situation, Figures 6 (A) to (D) are graphs showing a comparison of the relationship between hydrochloric acid concentration and pickling time when the method of the present invention and the dipping method are adopted, and Figure 7 (A), (B
) is a graph showing the relationship between the elongation rate and pickling time when the method of the present invention and the dipping method are adopted, FIG. 8 is a graph showing the relationship between the presence or absence of preheating before pickling and the descaling rate, and FIG. 9 is a graph showing the influence of the presence or absence of voids S in the pickling slag on the descaling rate. 1... Steel strip 2... Pickling tank 7... Upper ii
8a, 8b...Slit nozzle 9...
・Drain port IO...Skit L...Pickling liquid No. 6 Akane (A) Figure 6 (B)

Claims (1)

【特許請求の範囲】[Claims] (1)狭小空間内に処理液を加圧導入し、該狭小空間内
の全域において液圧を形成した状態で任意部位より該処
理液を系外へ放出させる様に制御しつつ、該狭小空間内
に長尺材料を高速走行させることを特徴とする長尺材料
の表面処理方法。
(1) A processing liquid is introduced under pressure into a narrow space, and the processing liquid is controlled to be discharged from any part to the outside of the system with a liquid pressure formed throughout the narrow space. A method for surface treatment of a long material, characterized by running the long material at high speed inside the material.
JP15494689A 1989-06-16 1989-06-16 Surface treatment of long-size material Granted JPH0320487A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15494689A JPH0320487A (en) 1989-06-16 1989-06-16 Surface treatment of long-size material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15494689A JPH0320487A (en) 1989-06-16 1989-06-16 Surface treatment of long-size material

Publications (2)

Publication Number Publication Date
JPH0320487A true JPH0320487A (en) 1991-01-29
JPH0577752B2 JPH0577752B2 (en) 1993-10-27

Family

ID=15595381

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15494689A Granted JPH0320487A (en) 1989-06-16 1989-06-16 Surface treatment of long-size material

Country Status (1)

Country Link
JP (1) JPH0320487A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5803981A (en) * 1997-01-13 1998-09-08 Danieli Wean, A Division Of Danieli Corporation Method and apparatus for continuous pickling of metal strip
NL1009863C2 (en) * 1998-08-14 2000-02-15 Hoogovens Corporate Services B Removing iron oxide layer from hot rolled strip steel, by subjecting the strip to consecutive pickling and mechanical surface treatment steps

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS523604A (en) * 1975-06-23 1977-01-12 Shell Int Research Method of converting hydrocarbon
JPS6279878U (en) * 1985-10-31 1987-05-21
JPS63266083A (en) * 1987-04-22 1988-11-02 Nippon Steel Corp Surface treatment of metallic strip
JPH01501009A (en) * 1986-08-29 1989-04-06 マンネスマン・アクチエンゲゼルシャフト A device that performs surface treatment on continuously running strips.

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS523604A (en) * 1975-06-23 1977-01-12 Shell Int Research Method of converting hydrocarbon
JPS6279878U (en) * 1985-10-31 1987-05-21
JPH01501009A (en) * 1986-08-29 1989-04-06 マンネスマン・アクチエンゲゼルシャフト A device that performs surface treatment on continuously running strips.
JPS63266083A (en) * 1987-04-22 1988-11-02 Nippon Steel Corp Surface treatment of metallic strip

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5803981A (en) * 1997-01-13 1998-09-08 Danieli Wean, A Division Of Danieli Corporation Method and apparatus for continuous pickling of metal strip
NL1009863C2 (en) * 1998-08-14 2000-02-15 Hoogovens Corporate Services B Removing iron oxide layer from hot rolled strip steel, by subjecting the strip to consecutive pickling and mechanical surface treatment steps

Also Published As

Publication number Publication date
JPH0577752B2 (en) 1993-10-27

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