JPH0577752B2 - - Google Patents

Info

Publication number
JPH0577752B2
JPH0577752B2 JP1154946A JP15494689A JPH0577752B2 JP H0577752 B2 JPH0577752 B2 JP H0577752B2 JP 1154946 A JP1154946 A JP 1154946A JP 15494689 A JP15494689 A JP 15494689A JP H0577752 B2 JPH0577752 B2 JP H0577752B2
Authority
JP
Japan
Prior art keywords
pickling
steel strip
descaling
liquid
tank
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
JP1154946A
Other languages
Japanese (ja)
Other versions
JPH0320487A (en
Inventor
Yoshinobu Nakane
Hideo Tatemichi
Shohei Tanaka
Kazusato Tanaka
Fumio Tomimatsu
Takeshi Takahashi
Hideaki Yoshimura
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)

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は長尺金属材料の酸洗処理法に関し、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。尚本発明は
連続的に走行させながら処理することのできる
種々の長尺金属材料の酸洗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 pickling treatment method for long metal materials. This invention relates to an improved method that can be carried out. The present invention can be widely used as a pickling treatment method for various long metal materials that can be treated while continuously running, but in the following explanation, a steel strip is pickled continuously. A typical example of descaling will be explained below.

[従来の技術] 鋼帯の連続生産に当たつては、熱間圧延や冷間
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洗浄化するため、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、連続処理の具体
的な方法としては、加熱塩酸の装入された複数
の酸洗槽に鋼帯を浸漬させながら連続的に走行さ
せるデイピング法(酸洗槽を浅めにした
SHALOW法ものこ方法に含まれる)と、走行
する鋼帯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
法が主流となつている。
[Prior art] In the continuous production of steel strips, pickling is used in the final process to remove and clean surface scales generated during hot rolling, cold rolling, strain relief annealing, etc. The descaling process is performed by The currently widely used method for this descaling treatment is to use heated hydrochloric acid (approximately 85 to 95 degrees Celsius) with a concentration of about 15 to 20% as the pickling solution. , a dipping method in which the steel strip is continuously run while immersed in multiple pickling tanks charged with heated hydrochloric acid (the pickling tanks are made shallower).
There are two methods: the SHALOW method (also included in the Koko method) and the spray method, in which heated hydrochloric acid is injected onto both sides of the running steel strip, but the former immersion 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の走行方向に沿つて酸洗槽2a,2b,…
…2y,2zが直列に配置されており、最下流側
の酸洗槽2zに酸洗液供給ポンプ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を経た後送給ポンプ5によつてそ
の上流側の酸洗槽2y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
酸洗槽2aから排出される。そして鋼帯1はガイ
ドロール6によつて酸洗槽2a,2b……2y,
2zの順に浸漬走行し、この間に鋼帯表面の酸化
物は熱塩酸により除去される。最下流側の酸洗槽
2zを出た鋼帯1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 immersion method.
Along the running direction of the steel strip 1, pickling tanks 2a, 2b,...
...2y, 2z are arranged in series, the pickling liquid is supplied from the pickling liquid supply pump 3 to the pickling tank 2z on the most downstream side, and the pickling liquid overflowing from the pickling tank 2z is transferred to the intermediate tank 4. After that, the pickling liquid is sent to the pickling tank 2y on the upstream side by the feed pump 5, and in the same way, the pickling liquid is sequentially sent to the pickling tanks on the upstream side, and then from the pickling tank 2a on the most upstream side. It is discharged. Then, the steel strip 1 is moved by guide rolls 6 into pickling tanks 2a, 2b...2y,
During the dipping run in the order of 2z, oxides on the surface of the steel strip are removed with hot hydrochloric acid. The steel strip 1 that has exited the pickling tank 2z on the most downstream side has the pickling liquid removed by a rinsing device (not shown), and is then 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イツピング法は、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鋼帯の走行
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
に伴つて生産性が低下し、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
ンシヨン付与、スキンパ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、鋼帯の予熱あるいは脱スケール促進の為
の予備処理(デスケラー処理等)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。
[Problems 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 steel strip or to reduce the running speed of the steel 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 is a method of preheating the steel strip before pickling.
Alternatively, a method has been implemented in which the steel strip is subjected to mechanical descaler treatment, tensioning, skin pass treatment, etc. to generate cracks in the scale, thereby facilitating subsequent descaling. However, these methods require special equipment for preheating the steel strip or for preliminary treatment to promote descaling (descaler treatment, etc.), which not only increases equipment costs but also complicates process control.

そこでデイツ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
であつて、その目的は、ターブランス方式の酸洗
処理法を改善し、簡単な設備および公定で一段と
優れた酸洗効率を得ることのできる方法を提供し
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 improve the turbulence pickling treatment method and to obtain even better pickling efficiency with simple equipment and official standards. It is intended to provide a method.

[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
酸洗処理法の構成は、長尺金属材料をターブラン
ス方式により酸洗処理する方法において、酸洗槽
内に酸洗液を加圧導入し、該酸洗槽内の全域に液
圧を作用させることにより全体の酸洗液に乱流状
態を形成した状態で任意部位より該酸洗を系外へ
放出させる様に制御しつつ、該酸洗槽内に長尺金
属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 pickling treatment method according to the present invention that can solve the above problems is that in the method of pickling a long metal material by the turbulence method, an acid is placed in the pickling tank. By introducing the washing liquid under pressure and applying liquid pressure to the entire area in the pickling tank, the pickling liquid is released from any part of the system to the outside of the system while creating a turbulent flow state in the entire pickling liquid. The gist of this method is to run a long metal material at high speed in the pickling tank while controlling the pickling tank.

[作用] 本発明者らは前述の様な従来技術の問題点に鑑
み、デイツ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つた。その結果、酸洗槽にお
ける鋼帯の走行状態の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
のデイツ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1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。
[Operation] 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 (that is, the descaling effect) significantly differs depending on the flow state of the pickling solution when the steel strip is running in the pickling tank. 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、
開放された酸洗槽2内の粘性を持つた酸洗液L
は、鋼帯1の走行に伴なつて随伴流を形成し、鋼
帯1の走行方向に沿つて流動する。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 steel strip 1 runs at high speed in pickling liquid L,
The viscous pickling liquid L in the open pickling tank 2
forms an accompanying flow as the steel strip 1 runs, and 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.

そして鋼帯1に近接して流動する酸洗液Lは、
脱スケール反応(Fe2O3+6HCl→2FeCl3+3H2O
またはFeO+2HCl→FeCl2+H2O)により洗浄活
性が低下し、あるいは洗浄活性を失つた後もその
まま鋼帯1付近を流動することになり、鋼帯1か
ら離れた位置に存在する新鮮な(洗浄活性を持つ
た)洗浄液が鋼帯1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 is
Descaling reaction (Fe 2 O 3 +6HCl→2FeCl 3 +3H 2 O
or FeO + 2HCl → FeCl 2 + H 2 O), the cleaning activity decreases, or even after losing the cleaning activity, it continues to flow near the steel strip 1, and the fresh (cleaning It is thought that this prevents the active cleaning liquid from flowing into the vicinity of the steel strip 1, and that the descaling effect gradually decreases. Also, the fact that it becomes difficult for fresh cleaning liquid to migrate to the vicinity of steel strip 1 means that
Heat transfer when attempting to increase the cleaning power by heating the surface of the steel strip 1 with the heated cleaning liquid is also inhibited, and the cleaning efficiency further decreases.

これに対してターブランス(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、上蓋7によつて
酸洗槽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、上蓋7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。
On the other hand, in the Turbulance pickling method, for example, as schematically shown in FIG. In this case, the pickling liquid L forms an accompanying flow similar to that explained in FIG. 3, but since the accompanying flow is disturbed by the upper lid 7, the pickling liquid L becomes easier to diffuse, and the pickling effect is slightly enhanced.

即ち本例では酸洗槽2が浅めに構成されてお
り、上蓋7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に対し上蓋7は静止してい
る。その為、上蓋7付近の随伴流は該上蓋7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。
That is, in this example, the pickling tank 2 is configured to be shallow, the top cover 7 is not far away from the steel strip 1, and the top cover 7 is stationary with respect to the steel strip 1 running at high speed. Therefore, it is thought that the accompanying flow near the upper cover 7 is slower than the accompanying flow near the steel strip 1 due to the wall resistance of the upper cover 7, which disturbs the accompanying flow and produces 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。
However, even with this turbulence method, the cleaning effect as initially expected could not be obtained, and the following fact was confirmed as the cause.

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
流によつて鋼帯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〓Sができる。そしてこの空
〓Sに面した酸洗液Lの液面は上蓋7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
なつて酸洗液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。
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. An empty space S is formed on the upstream side of the washing tank 2 in the running direction of the steel strip 1. Since the liquid surface of the pickling liquid L facing this air S is not subjected to wall resistance of the upper lid 7, the accompanying flow of the pickling liquid L in this part is not disturbed much, and this part becomes a quasi-laminar flow state. As a result, the diffusion of the pickling liquid L became insufficient, and it was thought that the cleaning effect would not be improved for the same reason as explained in FIG. 3.

そこで本発明らはターブランス方式に見られる
上記空〓Sができない様にすれば、酸洗槽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つて更に研
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, in the present invention, by preventing the above-mentioned void S seen in the turbulence method from forming, the pickling liquid L can be sufficiently diffused throughout the lengthwise direction of the pickling tank 2.
As a result of further research with the belief that the pickling effect can be enhanced, we arrived at the structure of the present invention.

即ち本発明では、前述の如くターブランス方式
による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つて、前記第
5図に示した様な空〓Sができない様にし、それ
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つて乱流状
態とする。その結果、酸洗液L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 described above, the pickling liquid is introduced under pressure into the pickling tank using the turbulence method, and by creating liquid pressure throughout the entire area in the pickling tank, the process shown in FIG. A turbulent flow state is created by preventing the formation of such voids, and by applying wall surface resistance to the accompanying flow of the pickling solution throughout the lengthwise direction of the pickling tank. As a result, the pickling liquid L is sufficiently diffused throughout the longitudinal direction of the pickling tank, and heat transfer also proceeds 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は上蓋7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、この装置はたてば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圧入用スリツト
ノズル、9は排液口、10は千鳥状に配置された
スキツトを夫々示す。
1A to 1C are schematic explanatory diagrams illustrating the pickling apparatus used in the present invention, and FIG. 1A is a longitudinal sectional view;
Fig. 1B is a plan view with the top cover 7 removed, and Fig. 1C is a longitudinal cross-sectional view taken along line C-C in Fig. 1A. It is produced as a thing. In the figure, 1 is a steel strip, 2 is a pickling tank,
7 is an upper lid, 8a and 8b are slit nozzles for press-fitting the pickling liquid L, 9 is a drain port, and 10 is a slit arranged in a staggered manner.

この装置を用いて酸洗を行なうに当たつては、
酸洗槽2内にスリツトノズル8a,8bから酸洗
液Lを加圧導入し、酸洗槽2の全域に液圧を形成
することによつて、酸洗槽2内に第5図で説明し
た様な空〓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成するが、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。
When performing pickling using this equipment,
By introducing the pickling liquid L into the pickling tank 2 under pressure from the slit nozzles 8a and 8b and creating liquid pressure in the entire area of the pickling tank 2, the process described in FIG. To run a steel strip 1 at high speed while preventing the formation of such a void S. Then, the pickling liquid L forms an accompanying flow in the running direction of the steel strip 1, but the pickling tank 2
has a narrow structure and the wall surface is located close to the running position of the steel strip 1, so the accompanying flow on the wall side is resisted and the flow velocity is suppressed, similar to what was explained in Fig. 4 above. For this reason, the pickling liquid L is in a turbulent state.

その結果、鋼帯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るので、前記第5図で説明し
た様な空〓Sが酸洗槽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、全長に亘つ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を酸洗槽2
の前後端に設けたスリツトノズル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、上蓋7や底面の適所から
圧入することも可能であり、要は酸洗槽2全域に
液圧を作用させて空〓を作らない限りどの様な圧
入手段を採用してもよい。
As a result, the pickling liquid L near the steel strip 1 is always replaced with fresh one, and the above-mentioned descaling reaction by pickling proceeds efficiently. Moreover, in the present invention, liquid pressure is applied to the entire area inside the pickling tank 2 by pressurized introduction of the pickling liquid L, so that a void S as explained in FIG. 5 above may be formed in the pickling tank 2. Without,
A turbulent flow condition is given to the entire area inside the pickling tank 2, and it becomes possible to proceed with pickling efficiently over the entire length. In the illustrated example, the pickling liquid L is transferred to the pickling tank 2.
Although an example is shown in which press fitting is performed from the slit nozzles 8a and 8b provided at the front and rear ends of Any press-fitting means may be used as long as it does not create a void by applying hydraulic pressure to the entire area of the pickling tank 2.

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鋼帯の走行速度に
よつて代わつてくるので、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〓Sができるのを防止することが
できる。
In addition, the pickling liquid L is kept at a high level by draining the pickling liquid L from drain ports 9 provided at appropriate locations on the bottom and side walls. 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 liquid in the pickling tank varies depending on the running speed of the steel strip, so by introducing the pickling liquid with enough pressure to overcome this pressure, the above-mentioned effect can be achieved in the pickling tank. It is possible to prevent the formation of such empty spaces.

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つ
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
作用する様に酸洗液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 apparatus shown in FIGS. 1A to 1C is merely an example of a preferable apparatus used in the present invention, and is not intended to limit the present invention. While introducing the pickling liquid L under pressure so that the liquid pressure of the pickling liquid acts on the entire area in the tank, the steel strip 1 is
The specific configuration of the device can be arbitrarily changed as long as it can run at high speed.

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

即ち第1図A〜Cに示した様な酸洗槽(幅:
300mm、鋼帯走行位置と上蓋下面間のギヤツプ:
150mm)を使用し、幅200mm×厚み2mmの鋼帯
(CAL材: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、酸洗時間、温度等
を代えた場合の脱スケール効果を、従来のデイツ
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, a pickling tank (width:
300mm, gap between the steel strip running position and the bottom surface of the top cover:
150mm) to descale a steel strip (CAL material: material for continuous annealing) with a width of 200mm and a thickness of 2mm, and the descaling effect when changing the hydrochloric acid concentration, pickling time, temperature, etc. was compared with the descaling effect when using the conventional descaling method.

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ヨンレベラーに
よつて鋼帯に加えられる伸び率を0%、1%、3
%、5%に代えた場合について、酸洗時間および
塩酸濃度と脱スケール所要時間(鋼帯表面の黒い
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 Figures 6A to 6D, the pickling temperature is set at 85℃, and the elongation rate applied to the steel strip by a tension leveler to promote descaling is 0%, 1%, and 3.
% and 5%, the relationship between the pickling time, hydrochloric acid concentration, and the time required for descaling (time until black scale on the surface of the steel strip can no longer be observed with the naked eye) is shown.

第6図A〜Dからも明らかな様に、本発明法と
従来のデイツ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。
As is clear from FIGS. 6A to 6D, 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, and the method of the present invention can significantly reduce the concentration of hydrochloric acid. It can be seen that a sufficient descaling effect can be enjoyed even when the temperature is lowered.

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ヨンレベラーより酸洗前の
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イツピング法につき対比して
示したグラフである。
Next, Figures 7A and 7B show the effect of changing the elongation rate given to the steel strip before pickling by a tension leveler to promote descaling, in accordance with the above method.
1 is a graph showing a comparison between the method of the present invention and a 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つていないのに対し、従
来のデイツピング法[第7図B]の場合は伸び率
によつて脱スケール所要時間はかなり異つてきて
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備処理(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, the descaling time required for the method of the present invention [Fig. 7A] remains almost the same even when the elongation rate is changed, whereas the time required for descaling with the conventional descaling method [Fig. 7B] ], 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. That is, from these results, it can be seen that by employing the present invention, an excellent descaling effect can be enjoyed even if the preliminary treatment for promoting descaling (treatment for creating cracks in the scale film) is omitted.

第8図は、塩酸濃度を3.0%、温度を85℃、テ
ンシヨンレベラーによつて加えられる伸び率を5
%、酸洗槽のギヤツプを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
予備加熱しなかつ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。
Figure 8 shows the hydrochloric acid concentration at 3.0%, the temperature at 85℃, and the elongation rate applied by the tension leveler at 5.
%, the gap in the pickling tank was set to 60 mm, and the flow rate of hydrochloric acid in the tank was set to 1.0 m/sec, but the method was the same as described above, and the steel strip was preheated (85℃) and without preheating. This figure shows the results of investigating the relationship between pickling time and descaling rate for the following cases.

この図からも明らかである様に、本発明を採用
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
ル率が若干高くなつているが、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つている。
即ちこの図より、本発明によれば、通常の酸洗時
間を採用する限り鋼帯の予熱をせずとも十分な脱
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 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 the descaling rate is slightly higher due to preheating. At the end of the washing 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 steel strip as long as a normal pickling time is used.

次に第9図は、塩酸濃度を3.0%、温度を85℃、
テンシヨ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図に示した様な酸性槽の上流側に空
〓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 hydrochloric acid concentration is 3.0%, the temperature is 85℃,
Figure 5 shows the case where the elongation rate by the tension leveler is set to 3%, the steel strip is not preheated, and the inside of the pickling tank is filled with water by adjusting the introduction pressure of hydrochloric acid (method of the present invention). This figure shows the results of investigating the relationship between the pickling time and the descaling rate in the case (comparative example) in which an empty space S is formed on the upstream side of the acid tank as shown in FIG.

この図からも明らかである様に、酸洗槽内に空
〓Sができるか否かによつ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〓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〓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 air is created in the pickling tank. The descaling effect is quite low under conditions where the pickling tank can be formed (comparative example), whereas the descaling effect is quite low when the liquid pressure in the pickling tank is increased to prevent the formation of empty water (the present invention). It turns out that it is very good.

[発明の効果] 本発明は以上の様に構成されており、ターブラ
ンス方式による狭小な酸洗槽内に酸洗液を加圧導
入し、該槽内に空〓ができない様な条件で鋼帯を
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(テンシヨンレベラーによる延伸やデ
スケラー処理等)が不用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。
[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 using the turbulence method, and the steel strip is processed under conditions such that no empty space is formed in the tank. By running at high speed and performing pickling, descaling can be accomplished extremely efficiently. Moreover, if this method is adopted, not only does pretreatment to promote descaling (stretching using a tension leveler, descaling treatment, etc.) become unnecessary, but preheating of the steel strip becomes unnecessary, and furthermore, it becomes unnecessary to preheat the steel strip. The acid concentration can also be lowered, simplifying the process and reducing the amount of acid consumed.

また本発明は、先に説明した様に洗浄層内に生
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つて前
述の様な効果を発揮させるものであり、種々の長
尺金属材料の酸洗処理法として極めて有効に活用
できる。
Further, as explained above, the present invention disturbs the accompanying flow of the cleaning liquid generated in the cleaning layer to create a turbulent flow state, and improves the diffusion of the cleaning liquid in the tank, thereby achieving the above-mentioned effects. This method can be used extremely effectively as a pickling treatment method for various long metal materials.

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

第1図A〜Cは本発明で使用されるターブラン
ス方式の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図は従来のデイツピン
グ式酸洗法を示す概念図、第3図は該デイツピン
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は本発明法とデイツピ
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
明法とデイツ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図は酸洗槽内における空〓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……上蓋、8
a,8b……スリツトノズル、9……排液口、1
0……スキツト、L……酸洗液。
1A to 1C illustrate a turbulence type pickling apparatus used in the present invention, in which FIG. 1A is a schematic vertical sectional view, FIG. 1B is a schematic plan view with the top lid open, FIG. 1C is a view corresponding to the longitudinal section taken along the line CC in FIG. 1A. 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 Figures 4 and 5 are turbulence type pickling. Explanatory diagrams showing the situation, Figures 6A to 6D are graphs comparing the relationship between hydrochloric acid concentration and pickling time when the method of the present invention and the date piing method are adopted, and Figures 7A and B are graphs showing the relationship between the method of the present invention and the pickling time. A graph showing the relationship between the elongation rate and pickling time when the dipping method is adopted, Figure 8 is a graph showing the relationship between the presence or absence of preheating before pickling and the descaling rate, and Figure 9 is a graph showing the relationship between the descaling rate and the presence or absence of preheating before pickling. It is a graph showing the influence of the presence or absence of empty S on the descaling rate. 1...Steel strip, 2...Pickling tank, 7...Top lid, 8
a, 8b...Slit nozzle, 9...Drain port, 1
0...Skitt, L...Pickling liquid.

Claims (1)

【特許請求の範囲】[Claims] 1 長尺金属材料をターブランス方式により酸洗
処理する方法において、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作用させるこ
とにより全体の酸洗液に乱流状態を形成した状態
で任意部位より該酸洗液を系外へ放出させる様に
制御しつつ、該酸洗槽内に長尺金属材料を高速走
行させることを特徴とする長尺金属材料の酸洗処
理法。
1 In a method of pickling long metal materials by the turbulence method, a pickling solution is introduced under pressure into a pickling tank, and the entire pickling solution is A long metal material characterized in that the long metal material is made to run at high speed in the pickling tank while controlling the pickling liquid to be discharged from an arbitrary part to the outside of the system while forming a turbulent flow state. Pickling treatment method for materials.
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 JPH0320487A (en) 1991-01-29
JPH0577752B2 true 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)

Families Citing this family (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

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7507484A (en) * 1975-06-23 1976-12-27 Shell Int Research PROCESS FOR CONVERTING HYDROCARBONS.
JPS6279878U (en) * 1985-10-31 1987-05-21
DE3629894A1 (en) * 1986-08-29 1988-03-03 Mannesmann Ag SYSTEM FOR THE SURFACE TREATMENT OF CONTINUOUSLY CONTINUOUS TAPES, IN PARTICULAR BEATING SYSTEM
JPS63266083A (en) * 1987-04-22 1988-11-02 Nippon Steel Corp Surface treatment of metallic strip

Also Published As

Publication number Publication date
JPH0320487A (en) 1991-01-29

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