JPH093673A - Pickling device and pickling method for thin steel sheet - Google Patents

Pickling device and pickling method for thin steel sheet

Info

Publication number
JPH093673A
JPH093673A JP7156160A JP15616095A JPH093673A JP H093673 A JPH093673 A JP H093673A JP 7156160 A JP7156160 A JP 7156160A JP 15616095 A JP15616095 A JP 15616095A JP H093673 A JPH093673 A JP H093673A
Authority
JP
Japan
Prior art keywords
steel plate
pickling
acid solution
temperature
steel sheet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7156160A
Other languages
Japanese (ja)
Inventor
Seiji Suga
政治 菅
Masanori Kurihara
正典 栗原
Yukio Ishiguchi
由紀男 石口
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP7156160A priority Critical patent/JPH093673A/en
Publication of JPH093673A publication Critical patent/JPH093673A/en
Pending 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

(57)【要約】 【目的】 酸洗時間の短縮化および設備の小型化を図る
ことができる薄鋼板の酸洗装置および方法を提供する。 【構成】 鋼板を加熱する鋼板加熱部と、鋼板が浸漬さ
れる酸洗槽部と、酸液の濃度及び温度を制御する酸液循
環槽部とを備え、鋼板を連続的に脱スケール処理する薄
鋼板の高速酸洗装置であって、鋼板加熱部は、前記酸洗
槽部入り側のブライドルロールと酸洗槽との間に設けら
れた鋼板加熱装置と、加熱された鋼板の温度を測定する
ための温度計と、腰折れ防止ロールと、を有し、酸洗槽
部は、鋼板浸漬時間制御用のシンクロールと、酸洗槽部
の下部より酸液、スケール、及びその他の不溶解物を排
出する手段と、を有し、循環槽部は、前記酸洗槽部の下
部に設けられ、上部酸洗槽内の酸液の濃度及び温度を調
整制御するために酸液を上部酸洗槽へ循環供給するとと
もに、鋼板から酸液へ移行した排熱を回収する熱交換器
を有する。
(57) [Abstract] [Purpose] To provide a pickling apparatus and method for a thin steel sheet capable of shortening the pickling time and downsizing the equipment. [Structure] A steel plate heating unit for heating a steel plate, a pickling tank unit in which the steel plate is immersed, and an acid solution circulation tank unit for controlling the concentration and temperature of the acid solution are provided, and the steel plate is continuously descaled. A high-speed pickling device for thin steel plates, wherein the steel plate heating unit measures the temperature of the heated steel plate with a steel plate heating device provided between the bridle roll and the pickling tank on the pickling tank entry side. Has a thermometer for preventing bending of the waist, and the pickling tank part is a sink roll for controlling the immersion time of the steel plate, and an acid solution, scale, and other insoluble matter from the bottom of the pickling tank part. And a circulation tank part is provided in the lower part of the pickling tank part, and the upper pickling solution is used to adjust and control the concentration and temperature of the pickling solution in the upper pickling tank. It has a heat exchanger that circulates and supplies it to the tank and recovers the exhaust heat transferred from the steel sheet to the acid solution.

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、薄鋼板の酸洗装置及
び酸洗方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pickling apparatus and a pickling method for thin steel sheets.

【0002】[0002]

【従来の技術】例えば、図3に示すように、従来の浸漬
式塩酸酸洗設備では、熱間圧延された鋼板1は、常温ま
で冷却された後に、入側設備のペイオフリール2から送
り出され、溶接機3、ルーパ4、ブライドル装置5並び
にスケールブレーカ6を経由して5〜6槽(全長約10
0m)で構成された塩酸槽7,8内を浸漬走行され、最
終的にテンションリール9によって巻き取られる。
2. Description of the Related Art For example, as shown in FIG. 3, in a conventional dipping-type hydrochloric acid pickling equipment, a hot-rolled steel sheet 1 is cooled to room temperature and then sent out from a payoff reel 2 of an entry-side equipment. , The welder 3, the looper 4, the bridle device 5, and the scale breaker 6 for 5 to 6 tanks (total length of about 10
(0 m), it is dipped in the hydrochloric acid tanks 7, 8 and finally wound up by the tension reel 9.

【0003】塩酸槽内の浸漬走行工程において鋼板表層
部のスケールは塩酸との化学反応により除去された後
に、鋼板1は次工程に送給されるか又は製品となる。酸
洗槽7,8は、それぞれが深さ500〜1000mm、長
さ10〜20mの大きさである。酸洗槽7,8内の塩酸
条件としては、高濃度かつ高温度であればあるほど脱ス
ケール性が向上することが知られているが、装置あるい
はコスト等の実用上の制約からこれらを無制限に高くす
ることはできず、一般的に塩酸濃度が4.0〜15.0
重量%、温度が80〜90℃程度とされている。
In the immersion traveling process in the hydrochloric acid tank, the scale of the surface layer of the steel plate is removed by a chemical reaction with hydrochloric acid, and then the steel plate 1 is fed to the next process or becomes a product. Each of the pickling tanks 7 and 8 has a depth of 500 to 1000 mm and a length of 10 to 20 m. As for the hydrochloric acid conditions in the pickling tanks 7 and 8, it is known that the higher the concentration and the higher the temperature, the more the descaling property improves. However, due to practical restrictions such as equipment or cost, these are not limited. It cannot be raised to a very high level, and the hydrochloric acid concentration is generally 4.0 to 15.0.
The weight% and the temperature are about 80 to 90 ° C.

【0004】近年では、生産性向上と設備投資抑制を狙
って酸洗処理時間の短縮化あるいは酸洗槽長を短くする
技術の開発が盛んに行われており、例えば酸洗槽入り側
にスケールブレーカを設置して表層のスケールに割れを
生じさせることにより酸液の浸透を促す酸洗方法(特開
昭56−160825号公報)や酸洗槽内に噴流を発生
させる方法(特開昭62−196387号公報)、また
は遮蔽板を設置する乱流プロモーターの設置により鋼板
近傍の酸液の新陳代謝を促進させる酸洗方法(特開平4
−59982号公報)、あるいは鋼板を酸液との反応温
度まで加熱することによりスケールと塩酸との化学反応
を促進させる酸洗方法(特開昭59−20487号公
報、特開平4−297589号公報)等が提案されてい
る。
In recent years, techniques for shortening the time of pickling treatment or shortening the length of pickling tank have been actively developed with the aim of improving productivity and restraining capital investment. A pickling method (Japanese Patent Laid-Open No. 56-160825) that promotes permeation of the acid solution by installing a breaker to cause cracks in the scale of the surface layer and a method of generating a jet flow in the pickling tank (Japanese Patent Laid-Open No. 62-62825). No. 196387), or a turbulence promoter for installing a shield plate to promote the metabolism of the acid solution in the vicinity of the steel plate (Japanese Patent Application Laid-Open No. Hei 4)
No. 59982), or a pickling method of promoting a chemical reaction between scale and hydrochloric acid by heating a steel sheet to a reaction temperature with an acid solution (JP-A-59-20487, JP-A-4-297589). ) Etc. have been proposed.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、従来の
浸漬式塩酸酸洗設備は、酸洗槽部だけでも長大な設置ス
ペースと膨大な建設費用を必要とする。また、操業及び
品質面においては、長大な酸洗槽中での酸液の温度及び
濃度を十分に制御することができず、良好な鋼板表面性
状を安定的に確保することができないという問題点があ
る。
However, the conventional immersion type hydrochloric acid pickling equipment requires a large installation space and enormous construction cost even with only the pickling tank section. Further, in terms of operation and quality, there is a problem that the temperature and concentration of the acid solution in a long pickling tank cannot be sufficiently controlled, and good steel sheet surface properties cannot be stably ensured. There is.

【0006】また、酸洗方法として実施されているスケ
ールブレーキング法では、鋼板の溶接部近傍では板破断
の危険があるために充分な効果を発揮できず、長手方向
の表面仕上りにむらが発生するとともに、酸洗時間の短
縮効果が少なく、ライン長は従来レベルのものである。
Further, the scale breaking method, which is carried out as a pickling method, cannot exert a sufficient effect because there is a risk of plate breakage in the vicinity of the welded part of the steel plate, resulting in uneven surface finish in the longitudinal direction. In addition, the effect of shortening the pickling time is small, and the line length is at the conventional level.

【0007】また、噴流方式においては、ライン長の短
縮効果は見込めるものの、耐酸ポンプ及び配管等の増設
によるコスト増によって相殺される上に、ポンプ動力費
の増大によりランニングコストも上昇するという問題点
がある。
Further, in the jet system, although the effect of shortening the line length can be expected, it is offset by the increase in cost due to the addition of the acid resistant pump and piping, and the running cost also rises due to the increase in pump power cost. There is.

【0008】この発明は、上記のような問題点を解決す
るためになされたもので、設置スペースの短縮及び設備
の建設費の低廉化が可能であるとともに、酸洗仕上りの
良好な薄鋼板を安定的に製造できる酸洗設備を得ること
を目的とする。
The present invention has been made to solve the above-mentioned problems, and it is possible to reduce the installation space and the cost of equipment construction, and at the same time, to produce a thin steel sheet having a good pickling finish. The purpose is to obtain a pickling equipment that can be stably manufactured.

【0009】[0009]

【課題を解決するための手段】本発明に係る薄鋼板の酸
洗装置は、鋼板を加熱する鋼板加熱部と、鋼板が浸漬さ
れる酸洗槽部と、酸液の濃度及び温度を制御する酸液循
環槽部とを備え、鋼板を連続的に脱スケール処理する薄
鋼板の酸洗装置であって、前記鋼板加熱部は、前記酸洗
槽部入り側のブライドルロールと酸洗槽との間に設けら
れた鋼板加熱装置と、加熱された鋼板の温度を測定する
ための温度計と、腰折れ防止ロールと、を有し、前記酸
洗槽部は、鋼板浸漬時間制御用のシンクロールと、酸洗
槽部の下部より酸液、スケール、及びその他の不溶解物
を排出する手段と、を有し、前記循環槽部は、前記酸洗
槽部の下部に設けられ、上部酸洗槽内の酸液の濃度及び
温度を調整制御するために酸液を上部酸洗槽へ循環供給
するとともに、鋼板から酸液へ移行した排熱を回収する
熱交換器を有することを特徴とする。
A pickling apparatus for a thin steel sheet according to the present invention controls a steel sheet heating section for heating a steel sheet, a pickling tank section in which the steel sheet is immersed, and a concentration and temperature of an acid solution. A pickling device for a thin steel plate, which comprises a pickling solution circulation tank part and continuously descales a steel plate, wherein the steel plate heating part comprises a bridle roll and a pickling tank on the pickling tank part side. A steel plate heating device provided between, a thermometer for measuring the temperature of the heated steel plate, and a waist bending prevention roll, and, the pickling tank portion, a sink roll for steel plate immersion time control and And means for discharging the acid solution, scale, and other insolubles from the lower part of the pickling tank part, the circulation tank part being provided in the lower part of the pickling tank part, and the upper pickling tank. The acid solution is circulated and supplied to the upper pickling tank to adjust and control the concentration and temperature of the acid solution in the steel. Characterized in that it has a heat exchanger for recovering waste heat having transferred to the acid solution from.

【0010】さらに、鋼種、鋼板温度、シンクロール位
置、酸液条件が検出データ又は初期設定データとして入
力され、これらの入力データに基づき鋼板加熱温度およ
び鋼板浸漬時間を求める演算部と、求めた鋼板加熱温度
に基づき鋼板加熱部の加熱動作を制御して鋼板浸漬時に
酸液の核沸騰状態が得られる温度域まで鋼板を加熱する
とともに、求めた鋼板浸漬時間に基づきシンクロール動
作を制御して鋼板の浸漬深さを調節する制御部と、を有
することが望ましい。
Further, a steel type, a steel plate temperature, a sink roll position, and an acid solution condition are input as detection data or initial setting data, and a calculation unit for calculating a steel plate heating temperature and a steel plate immersion time based on these input data, and the calculated steel plate. Control the heating operation of the steel plate heating unit based on the heating temperature to heat the steel plate to a temperature range where the nucleate boiling state of the acid solution is obtained during steel plate immersion, and control the sink roll operation based on the obtained steel plate immersion time to control the steel plate. And a controller for adjusting the immersion depth.

【0011】本発明に係る薄鋼板の酸洗方法は、鋼板を
加熱する鋼板加熱部と、鋼板が浸漬される酸洗槽部とを
備え、鋼板を酸液に浸漬して連続的に脱スケール処理す
る薄鋼板の酸洗方法であって、前記鋼板加熱部において
鋼板浸漬時に酸液が核沸騰状態になる温度域まで鋼板を
加熱し、加熱直後に鋼板を酸液に浸漬することを特徴と
する。
The thin steel sheet pickling method according to the present invention comprises a steel sheet heating section for heating a steel sheet and a pickling tank section in which the steel sheet is immersed, and the steel sheet is immersed in an acid solution for continuous descaling. A method for pickling a thin steel sheet to be treated, wherein the steel sheet is heated to a temperature range where the acid solution is in a nucleate boiling state when the steel sheet is immersed in the steel sheet heating section, and the steel sheet is immersed in the acid solution immediately after heating. To do.

【0012】また、本発明に係る薄鋼板の酸洗方法は、
鋼板を加熱する鋼板加熱部と、鋼板が浸漬される酸洗槽
部と、酸液の濃度及び温度を制御する酸液循環槽部とを
備え、鋼板を連続的に脱スケール処理する薄鋼板の酸洗
装置であって、前記鋼板加熱部は、前記酸洗槽部入り側
のブライドルロールと酸洗槽との間に設けられた鋼板加
熱装置と、加熱された鋼板の温度を測定するための温度
計と、腰折れ防止ロールと、を有し、前記酸洗槽部は、
鋼板浸漬時間制御用のシンクロールと、酸洗槽部の下部
より酸液、スケール、及びその他の不溶解物を排出する
手段と、を有し、前記循環槽部は、前記酸洗槽部の下部
に設けられ、上部酸洗槽内の酸液の濃度及び温度を調整
制御するために酸液を上部酸洗槽へ循環供給するととも
に、鋼板から酸液へ移行した排熱を回収する熱交換器を
有する薄鋼板の酸洗装置を用いて鋼板を酸洗処理する際
に、インヒビターを含み、かつ濃度4.0〜8.0重量
%の塩酸溶液を鋼板1トンあたり60〜150kgの割
合で酸洗槽部へ循環供給し、鋼板加熱温度を100〜3
00℃の範囲とし、酸液の液面と鋼板とのなす鋭角とし
ての鋼板侵入角度が30〜60°の範囲になるように塩
酸溶液に対して鋼板を浸漬することを特徴とする。
The method of pickling thin steel sheet according to the present invention is
A steel plate heating unit for heating a steel plate, a pickling tank unit in which the steel plate is immersed, and an acid solution circulation tank unit for controlling the concentration and temperature of the acid solution, and a thin steel plate for continuously descaling the steel plate. A pickling device, wherein the steel plate heating unit is a steel plate heating device provided between the bridle roll and the pickling tank on the pickling tank portion-entry side, and for measuring the temperature of the heated steel plate. It has a thermometer and a waist bend preventing roll, and the pickling tank part is
A sink roll for steel plate immersion time control, and means for discharging the acid solution, scale, and other insolubles from the lower part of the pickling tank section, the circulation tank section, Heat exchange that is provided in the lower part and circulates and supplies the acid solution to the upper pickling tank to adjust and control the concentration and temperature of the acid solution in the upper pickling tank, and recovers the exhaust heat transferred from the steel plate to the acid solution. When a steel sheet is pickled using a steel sheet pickling apparatus having a vessel, a hydrochloric acid solution containing an inhibitor and having a concentration of 4.0 to 8.0% by weight is used at a rate of 60 to 150 kg per ton of steel sheet. Circulating and supplying to the pickling tank, the steel plate heating temperature is 100 to 3
It is characterized in that the steel plate is immersed in a hydrochloric acid solution at a temperature of 00 ° C. so that the steel plate penetration angle as an acute angle formed by the liquid surface of the acid solution and the steel plate is in the range of 30 to 60 °.

【0013】なお、酸液がインヒビター(酸洗抑制剤)
を含む塩酸溶液である場合は、鋼板を100〜300℃
の温度域に加熱することが望ましく、150〜300℃
の温度域に加熱することが更に好ましい。このような温
度域に加熱した直後に鋼板を酸液に浸漬すると、鋼板表
面近傍で核沸騰状態が得られ、スケールに多数の微細ク
ラックが生じるので、鋼板の表面性状が良好になる。と
くに、鋼板を200〜250℃の温度域に加熱したとき
に理想的な鋼板の表面性状が得られる。
The acid solution is an inhibitor (pickling inhibitor).
In the case of a hydrochloric acid solution containing
It is desirable to heat to the temperature range of 150 to 300 ° C
It is more preferable to heat to the temperature range of. If the steel sheet is immersed in an acid solution immediately after being heated to such a temperature range, a nucleate boiling state is obtained near the surface of the steel sheet, and many fine cracks are generated in the scale, so that the steel sheet has good surface properties. Particularly, when the steel sheet is heated to a temperature range of 200 to 250 ° C., ideal surface properties of the steel sheet can be obtained.

【0014】また、鋼板侵入角度は30〜60°の範囲
とすることが望ましい。酸洗槽内の酸液に対する鋼板の
侵入角度が30°を下回る場合も60°を上回る場合も
ともに脱スケール状態が不良になるからである。
Further, it is desirable that the steel plate penetration angle is in the range of 30 to 60 °. This is because the descaling state becomes poor both when the penetration angle of the steel sheet with respect to the acid solution in the pickling tank is below 30 ° and above 60 °.

【0015】さらに、濃度4.0〜8.0重量%の塩酸
溶液を鋼板1トンあたり60〜150kgの割合で酸洗
槽部へ循環供給することが望ましい。鋼板1トンあたり
の塩酸溶液の供給量が60kgを下回る領域では鋼板の
脱スケールが不十分になり、酸液供給量が150kgを
越える領域では脱スケール効果が飽和してしまい過剰供
給となるからである。脱スケール用の酸液には塩酸溶液
を用いることが好ましい。この場合に、溶液の塩酸濃度
は4.0〜8.0重量%の範囲とする。塩酸濃度の下限
値を4.0重量%とするのは鋼板の脱スケールが不十分
になるからであり、上限値を8.0重量%とするのは鋼
板の素地が腐食されて表面性状が損われるからである。
また、酸液の温度は通常は80〜90℃の範囲に制御さ
れることが望ましい。
Further, it is desirable to circulate and supply a hydrochloric acid solution having a concentration of 4.0 to 8.0% by weight to the pickling tank section at a rate of 60 to 150 kg per ton of steel sheet. In the region where the supply amount of the hydrochloric acid solution per ton of steel plate is less than 60 kg, the descaling of the steel plate becomes insufficient, and in the region where the supply amount of the acid solution exceeds 150 kg, the descaling effect is saturated and becomes excessive supply. is there. A hydrochloric acid solution is preferably used as the acid solution for descaling. In this case, the hydrochloric acid concentration of the solution is in the range of 4.0 to 8.0% by weight. The lower limit of the hydrochloric acid concentration is 4.0% by weight because the descaling of the steel sheet is insufficient, and the upper limit of 8.0% by weight is that the base material of the steel sheet is corroded and the surface property is Because it will be damaged.
Further, it is desirable that the temperature of the acid solution is usually controlled in the range of 80 to 90 ° C.

【0016】[0016]

【作用】高温の物体を液中に浸漬すると両者の温度差に
応じて3段階の沸騰現象が現れる。先ず第1段階の比較
的低温の領域では核沸騰状態が出現する。核沸騰状態に
おいては、物体の表面全体から気泡が発生し、表面と液
相間で熱および物質の移動が活発に行われる。次にこれ
より高温の第2段階の温度域では遷移沸騰状態に移行す
る。遷移沸騰状態では物体表面の大部分から連続的に気
泡が発生するとともに部分的には蒸気膜によって覆われ
るようになり、表面と液相間の熱及び物質の移動が核沸
騰時よりも鈍くなる。さらに高温の第3段階の温度域で
は膜沸騰状態へと移行する。膜沸騰状態では物体の全表
面が蒸気膜にて覆われることとなり、熱及び物質の移動
は妨げられ、更に鈍くなる。
When a high-temperature object is immersed in a liquid, three-step boiling phenomenon appears depending on the temperature difference between the two. First, the nucleate boiling state appears in the relatively low temperature region of the first stage. In the nucleate boiling state, bubbles are generated from the entire surface of the object, and heat and mass are actively transferred between the surface and the liquid phase. Next, in the temperature range of the second stage, which is higher than this, the state transitions to the transition boiling state. In the transition boiling state, bubbles are continuously generated from most of the surface of the object and partially covered by the vapor film, and heat and mass transfer between the surface and the liquid phase becomes slower than during nucleate boiling. . In the higher temperature third stage temperature range, the film transitions to the film boiling state. In the film boiling state, the entire surface of the object is covered with the vapor film, which hinders the transfer of heat and mass, and becomes even dull.

【0017】本発明に係る薄鋼板の酸洗装置及び酸洗方
法においては、鋼板加熱部において鋼板浸漬時に酸液が
核沸騰状態になる温度域まで鋼板を予備加熱し、加熱直
後に鋼板を酸液に浸漬するので、鋼板近傍に急激な熱移
動と物質移動とを伴う核沸騰状態が出現する。この核沸
騰状態において鋼板表面に接触する酸液が短時間で迅速
に更新されるので、急速加熱と相俟って脱スケール反応
が促進される。
In the pickling apparatus and the pickling method for a thin steel sheet according to the present invention, the steel sheet is preheated to a temperature range in which the acid solution is in a nucleate boiling state when the steel sheet is immersed in the steel sheet heating section, and the steel sheet is pickled immediately after heating. Since it is immersed in the liquid, a nucleate boiling state with rapid heat transfer and mass transfer appears near the steel plate. In this nucleate boiling state, the acid solution contacting the surface of the steel sheet is rapidly renewed in a short time, so that the descaling reaction is promoted in combination with the rapid heating.

【0018】さらに、鋼板の予備加熱温度を制御するだ
けでなく、鋼板の浸漬深さと侵入角度をも制御するの
で、各鋼種ごと及び生成スケール量ごとに脱スケール時
間変化に対してそれぞれ柔軟に対処することができる。
また、酸洗槽内の酸液の温度不均一に対しても下部の循
環槽において調整量及び制御量について余裕をもたせて
いるので、きめ細かく対処することができ、良好な酸洗
仕上がりを安定的に維持することができる。以上のこと
は、鋼板の部分的な過熱状態を回避し、鋼板の幅方向両
端部の波うちや中央部の膨出などのような変形(板形状
のくずれ)が実質的に生じなくしている。
Further, not only the preheating temperature of the steel sheet is controlled, but also the immersion depth and the penetration angle of the steel sheet are controlled, so that it is possible to flexibly cope with the descaling time change for each steel type and each generated scale amount. can do.
In addition, even if the temperature of the acid solution in the pickling tank is not uniform, there is a margin for the adjustment amount and control amount in the lower circulation tank, so it is possible to take detailed measures and stabilize the good pickling finish. Can be maintained at. What has been described above avoids a partial overheated state of the steel sheet, and substantially prevents the deformation (plate shape collapse) such as corrugation at both widthwise end portions of the steel sheet and bulging of the central portion. .

【0019】また、酸液(塩酸溶液)に浸漬する場合
に、鋼板加熱温度が100〜300℃の範囲であること
がとくに好ましいのは次の理由による。第1に、酸液の
沸点以上でなければ、沸騰現象は得られないからであ
る。
Further, it is particularly preferable that the steel plate heating temperature is in the range of 100 to 300 ° C. when immersed in an acid solution (hydrochloric acid solution) for the following reason. First, the boiling phenomenon cannot be obtained unless the boiling point is higher than the boiling point of the acid solution.

【0020】第2に、鋼板加熱温度が300℃以下のと
きは、沸騰現象が核沸騰域にあるため、表層スケールへ
の微細なクラック発生を誘発し、かつ酸液の新陳代謝も
促進される。鋼板加熱温度が300℃を越えると、遷移
沸騰域から膜沸騰域へと移行し、微細なクラック発生を
妨げるとともに、新陳代謝促進も鈍化(脱スケール性悪
化)するからである。
Secondly, when the heating temperature of the steel sheet is 300 ° C. or lower, the boiling phenomenon is in the nucleate boiling region, so that the generation of fine cracks on the surface layer scale is induced and the metabolism of the acid solution is promoted. This is because when the steel plate heating temperature exceeds 300 ° C., the transition from the transition boiling region to the film boiling region is caused, the generation of fine cracks is prevented, and the promotion of metabolism is slowed down (descaling property is deteriorated).

【0021】[0021]

【実施例】以下、添付の図面を参照しながら本発明の実
施例について説明する。圧延工場で熱間圧延された薄鋼
板1は、コイル状に巻き取られて常温まで冷却された後
に、浸漬式塩酸酸洗設備に搬送される。
Embodiments of the present invention will be described below with reference to the accompanying drawings. The thin steel sheet 1 hot-rolled in a rolling mill is wound into a coil and cooled to room temperature, and then transported to an immersion type hydrochloric acid pickling equipment.

【0022】図1には浸漬式塩酸酸洗ラインの一部のみ
を示すが、この浸漬式塩酸酸洗ラインでは上流側のペイ
オフリール(図示せず)から下流側のテンションリール
(図示せず)に至るまで連続送給されており、薄鋼板1
は酸洗槽16に浸漬されるようになっている。パスライ
ン下側には多数の搬送ロール(図示せず)が並び、鋼板
1が高速で搬送されるようになっている。酸洗槽16と
ペイオフリールとの間にはブライドルロール12、誘導
加熱装置13、温度計15がこの順に設けられている。
上部酸洗槽16は下部循環槽21に配管及びポンプ25
を介して連通し、酸液の循環回路が形成されている。循
環槽21は、上部酸洗槽16の下部より酸液及び槽内沈
殿物を抜き出して酸液の温度及び濃度の制御を容易にす
る働きをもつとともに、槽内に排熱回収用の熱交換器1
9を備えている。熱交換器19のチューブ側にはほぼ室
温の水が供給されるようになっている。この供給水がシ
ェル側の酸液と熱交換して温水となり、これが水洗槽2
0に送られるようになっている。
Although only a part of the immersion type hydrochloric acid pickling line is shown in FIG. 1, in this immersion type hydrochloric acid pickling line, a payoff reel (not shown) on the upstream side and a tension reel (not shown) on the downstream side are provided. It is continuously fed up to
Is immersed in the pickling tank 16. A large number of conveying rolls (not shown) are arranged below the pass line so that the steel plate 1 can be conveyed at high speed. A bridle roll 12, an induction heating device 13, and a thermometer 15 are provided in this order between the pickling tank 16 and the payoff reel.
The upper pickling tank 16 has a pipe 25 and a pump 25 in the lower circulation tank 21.
And a circulation circuit for the acid solution is formed. The circulation tank 21 has a function of facilitating the control of the temperature and the concentration of the acid solution by extracting the acid solution and the in-tank precipitate from the lower portion of the upper pickling tank 16, and the heat exchange for recovering the exhaust heat in the tank. Bowl 1
9 is equipped. Water at almost room temperature is supplied to the tube side of the heat exchanger 19. The supplied water exchanges heat with the acid solution on the shell side to become warm water, which is the washing tank 2
0.

【0023】鋼板加熱部を構成する加熱装置としては、
設備長の短く温度制御性に優れている誘導加熱装置が望
ましい。例えばコイル長さは板幅と同等か又はその数倍
とすることが好ましい。このような誘導加熱装置13の
インダクションコイル13bは、パスライン上の鋼板1
を取り囲むように設けられ、交流電源13aに接続され
ている。なお、コイル電源13aは制御部40に接続さ
れ、コイル13bへの給電量が制御されるようになって
いる。コイル13bの誘導加熱によって鋼板1は瞬時に
100〜400℃の温度域まで加熱されるようになって
いる。
As a heating device constituting the steel plate heating section,
An induction heating device with short equipment length and excellent temperature controllability is desirable. For example, the coil length is preferably equal to or several times the plate width. The induction coil 13b of such an induction heating device 13 is the steel plate 1 on the pass line.
It is provided so as to surround and is connected to the AC power supply 13a. The coil power supply 13a is connected to the control unit 40 so that the amount of power supplied to the coil 13b is controlled. The steel sheet 1 is instantly heated to a temperature range of 100 to 400 ° C. by the induction heating of the coil 13b.

【0024】なお、誘導加熱装置13では均一加熱性に
関してエッジ部過加熱(目標温度±10℃)となるが、
一般的にコイル状に巻かれた薄鋼板の場合はエッジ部の
スケール厚みが中央部より厚いので、望ましい結果をも
たらす。また、誘導加熱装置13は、出側に設けた鋼板
温度計(図示せず)から得られる温度情報をフィードバ
ック制御することにより、均一加熱及びライン減速に合
わせた入/出力制御を行う。加熱装置13と酸洗槽16
との距離Lが長い場合(L≧0.5m)は、鋼板1の腰
折れ(薄鋼板の製品欠陥となる座屈)防止用にロール径
が0.32m以上の腰折れ防止ロール22を設置する必
要がある。
In the induction heating device 13, the edge portion is overheated (target temperature ± 10 ° C.) for uniform heating,
Generally, in the case of a coiled thin steel sheet, the scale thickness of the edge portion is thicker than that of the central portion, so that a desirable result is obtained. The induction heating device 13 also performs feedback control of temperature information obtained from a steel plate thermometer (not shown) provided on the outlet side to perform uniform heating and input / output control according to line deceleration. Heating device 13 and pickling tank 16
When the distance L from the sheet is long (L ≧ 0.5 m), it is necessary to install a waist bend prevention roll 22 having a roll diameter of 0.32 m or more to prevent the steel plate 1 from bending (buckling, which is a product defect of a thin steel plate). There is.

【0025】放射式の温度計15が、酸洗槽16の入側
直前で、かつパスラインの上方に設けられ、通過中の鋼
板1の温度が非接触で連続的に検出されるようになって
いる。温度計15は演算部30の入力側に接続されてい
る。演算部30の入力側にはこの他に位置センサ(図示
せず)、濃度センサ(図示せず)、液温センサ(図示せ
ず)が接続され、シンクロール位置検出信号および塩酸
条件データ信号などが入力されるようになっている。一
方、演算部30の出力側は制御部40の入力側に接続さ
れ、各種データ信号が制御部40に入力されるようにな
っている。
A radiation type thermometer 15 is provided immediately before the entrance side of the pickling tank 16 and above the pass line so that the temperature of the steel sheet 1 during passage can be continuously detected without contact. ing. The thermometer 15 is connected to the input side of the calculation unit 30. A position sensor (not shown), a concentration sensor (not shown), and a liquid temperature sensor (not shown) are also connected to the input side of the arithmetic unit 30, and a sync roll position detection signal and a hydrochloric acid condition data signal are supplied. Is entered. On the other hand, the output side of the arithmetic unit 30 is connected to the input side of the control unit 40, and various data signals are input to the control unit 40.

【0026】温度計15の直ぐ下流側には酸洗槽16及
び水洗槽20がこの順に並んで設けられている。酸洗槽
16の中には、液温80〜90℃に調整された濃度4〜
8重量%の塩酸溶液が収容されている。この塩酸溶液は
酸洗抑制剤としてインヒビターを含んでいる。塩酸溶液
中にはシンクロール17と固定ロール18とが浸漬され
ている。シンクロール17は昇降シリンダ(図示せず)
によって支持され、塩酸溶液に浸漬されたり、これから
引上げられたりされるようになっている。これにより鋼
板1の浸漬長さ及び侵入角度θが制御される。
Immediately downstream of the thermometer 15, a pickling tank 16 and a water washing tank 20 are provided side by side in this order. In the pickling tank 16, the concentration of 4 to 4 adjusted to a liquid temperature of 80 to 90 ° C.
It contains an 8 wt% hydrochloric acid solution. This hydrochloric acid solution contains an inhibitor as a pickling inhibitor. A sink roll 17 and a fixed roll 18 are immersed in the hydrochloric acid solution. The sink roll 17 is a lifting cylinder (not shown)
It is supported by and can be immersed in or pulled from a hydrochloric acid solution. Thereby, the immersion length of steel plate 1 and the penetration angle θ are controlled.

【0027】また、下方の循環槽21は、上部酸洗槽1
6の底部より酸液及び槽内沈殿物を常時抜き出して受け
入れるとともに、上部酸洗槽16への供給酸液の温度及
び濃度を制御部40及び演算部30によってきめ細かく
管理される。すなわち、L.S、鋼種、塩酸条件、シン
クロール位置、鋼板温度の入力データに基づき演算部3
0は最適の操業条件を算出し、これを制御部40へ送
る。これに基づき制御部40は濃度4.0〜8.0重量
%の塩酸溶液を鋼板1トンあたり60〜150kgの割
合で酸洗槽部16へ供給するように制御する。酸洗槽部
16へは循環槽21から循環回収される酸液とともに他
の供給源(図示せず)から新たな酸液が供給されるよう
になっている。
The lower circulation tank 21 is the upper pickling tank 1
The acid solution and the in-tank precipitate are constantly extracted from the bottom of the tank 6 and accepted, and the temperature and concentration of the acid solution supplied to the upper pickling tank 16 are finely controlled by the control unit 40 and the arithmetic unit 30. That is, L. Calculation unit 3 based on the input data of S, steel type, hydrochloric acid condition, sink roll position, and steel plate temperature
0 calculates the optimum operating condition and sends it to the control unit 40. Based on this, the control unit 40 controls to supply the hydrochloric acid solution having a concentration of 4.0 to 8.0% by weight to the pickling tank unit 16 at a rate of 60 to 150 kg per ton of steel plate. A new acid solution is supplied to the pickling tank section 16 from another supply source (not shown) together with the acid solution circulated and recovered from the circulation tank 21.

【0028】なお、熱交換器19が下部循環槽21のな
かに設けられ、熱交換器19の内部通路を通流する水と
下部循環槽21内の塩酸溶液とが熱交換されるようにな
っている。熱交換された温水は水洗槽20に送られるよ
うになっている。なお、液温測定用温度計(図示せず)
及び濃度計(図示せず)が上部酸洗槽16及び下部循環
槽21の適所にそれぞれ設けられ、塩酸溶液の温度及び
濃度がそれぞれ検出されるようになっている。
The heat exchanger 19 is provided in the lower circulation tank 21 so that the water flowing through the internal passage of the heat exchanger 19 and the hydrochloric acid solution in the lower circulation tank 21 are heat-exchanged. ing. The hot water that has undergone heat exchange is sent to the washing tank 20. A thermometer for measuring liquid temperature (not shown)
And a concentration meter (not shown) are provided at appropriate places in the upper pickling tank 16 and the lower circulation tank 21, respectively, so that the temperature and the concentration of the hydrochloric acid solution can be detected.

【0029】制御部40の出力側は、加熱装置13のコ
イル電源13aの他に、シンクロール17の昇降シリン
ダ(図示せず)の駆動電源および液温測定用温度計(図
示せず)にそれぞれ接続されている。
On the output side of the control unit 40, in addition to the coil power supply 13a of the heating device 13, a drive power supply for an elevating cylinder (not shown) of the sink roll 17 and a thermometer for liquid temperature measurement (not shown), respectively. It is connected.

【0030】次に、上記の浸漬式塩酸酸洗ラインにおい
て鋼板を連続的に酸洗処理する場合について説明する。
熱間圧延工程にて製造され、常温まで冷却された鋼板1
は、図示されていない入側設備を経由し、ブライドルロ
ール12に至る。鋼板1は、誘導加熱装置13により1
00〜300℃の範囲の所定の温度に加熱された後に、
腰折れ防止用の小径搬送ロール22上を通過し、酸洗槽
16に至る。酸洗槽16(20〜30m)内には、上下
可動式のシンクロール17を設置するとともに、下部循
環槽21より所定の液温度と所定の濃度に制御された酸
液の供給を受け、鋼種及びラインスピード毎の酸洗仕上
りを均一かつ安定的にする制御機能を備えている。循環
槽21内の熱交換器19にて回収された温水は、次の水
洗槽20へと導かれる。
Next, the case where the steel sheet is continuously pickled in the above-mentioned immersion type hydrochloric acid pickling line will be described.
Steel plate 1 manufactured in the hot rolling process and cooled to room temperature
Arrives at the bridle roll 12 via an entrance facility (not shown). The steel plate 1 is 1 by the induction heating device 13.
After being heated to a predetermined temperature in the range of 00 to 300 ° C,
After passing over the small-diameter transport roll 22 for preventing the waist from breaking, it reaches the pickling tank 16. In the pickling tank 16 (20 to 30 m), a vertically movable sink roll 17 is installed, and the lower circulation tank 21 receives the supply of the acid solution controlled to a predetermined liquid temperature and a predetermined concentration. It also has a control function to make the pickling finish uniform and stable for each line speed. The warm water recovered by the heat exchanger 19 in the circulation tank 21 is guided to the next washing tank 20.

【0031】加熱鋼板1を酸液中に浸漬させると、鋼板
1に接触した酸液が核沸騰状態となる。核沸騰状態にお
いては鋼板1の全表面から気泡が無数に発生し、酸液と
鋼板1との間で急激な熱移動と物質移動とが生じ、脱ス
ケール反応が十分に促進される。
When the heated steel plate 1 is dipped in the acid solution, the acid solution in contact with the steel plate 1 is in a nucleate boiling state. In the nucleate boiling state, innumerable bubbles are generated from the entire surface of the steel sheet 1, rapid heat transfer and mass transfer occur between the acid solution and the steel sheet 1, and the descaling reaction is sufficiently promoted.

【0032】上記した酸洗処理時間の短縮と設備のコン
パクト化についての課題は、浸漬式塩酸酸洗設備におい
て、入側部のブライドルロール12と酸洗槽16との間
に鋼板加熱装置13、鋼板温度計15及び腰折れ防止用
ロール22を具備する鋼板加熱部を設けて、鋼板を酸液
の沸点以上で100〜300℃の温度範囲内に加熱した
後に、酸液中に浸漬する酸洗方法(以降、高温装入酸洗
法と称す)を実施することにより解決される。
The above-mentioned problems regarding the shortening of the pickling treatment time and the downsizing of the equipment are as follows: In the immersion hydrochloric acid pickling equipment, the steel sheet heating device 13, between the bridle roll 12 and the pickling tank 16 on the inlet side, A pickling method in which a steel plate heating unit including a steel plate thermometer 15 and a waist bending preventing roll 22 is provided to heat the steel plate within a temperature range of 100 to 300 ° C. at a boiling point of the acid liquid or higher, and then immersed in the acid liquid. (Hereinafter, it will be referred to as a high-temperature charging pickling method).

【0033】次に、表1を参照しながら鋼板温度を種々
変えたときのクラック発生状況および脱スケールにつき
調べた結果を、実施例1〜5と比較例1,2、従来方
法、並びにスケールブレーキング法のそれぞれと比べて
説明する。
Next, referring to Table 1, the results of investigations on the crack occurrence state and descaling when the steel sheet temperature was variously changed were carried out, and Examples 1 to 5 and Comparative Examples 1 and 2, the conventional method, and the scale brake were examined. The explanation will be made in comparison with each of the Longing methods.

【0034】実施例1〜5は鋼板加熱温度をそれぞれ1
00℃,150℃,200℃,250℃,300℃に設
定した場合に対応する。比較例1および2は鋼板加熱温
度をそれぞれ350℃と400℃に設定した場合に対応
する。従来方法は鋼板温度をそれぞれ30℃(加熱せ
ず)及び80℃(低温加熱)に設定した場合に対応す
る。スケールブレーキング法は鋼板温度を30℃(加熱
せず)に設定した場合に対応する。なお、スケールブレ
ーキング法は特開昭56−160825号公報、特開昭
62−196387号公報、特開平4−59982号公
報にそれぞれ記載された方法に準拠している。
In Examples 1 to 5, the steel plate heating temperature was 1
It corresponds to the case of setting to 00 ° C, 150 ° C, 200 ° C, 250 ° C, 300 ° C. Comparative Examples 1 and 2 correspond to the case where the steel plate heating temperatures are set to 350 ° C. and 400 ° C., respectively. The conventional method corresponds to the case where the steel plate temperature is set to 30 ° C. (no heating) and 80 ° C. (low temperature heating), respectively. The scale breaking method corresponds to the case where the steel plate temperature is set to 30 ° C. (without heating). The scale breaking method is based on the methods described in JP-A-56-160825, JP-A-62-196387, and JP-A-4-59982.

【0035】スケールにおけるクラック発生状況と酸洗
処理時間短縮の効果について上記の場合をそれぞれ調べ
た。表中にて二重丸は微細クラックが多数生じた結果
を、一重丸はクラック数が多い結果を、三角はクラック
数が少ない結果を、バツマークは少数の大きなクラック
のみが生じた結果をそれぞれ示す。表から明らかなよう
に、鋼板加熱温度を150〜300℃の範囲とした場合
に良好な結果を得ることができ、200〜250℃の温
度範囲では最良の結果を得ることができた。
The above-mentioned cases were examined with respect to the occurrence of cracks on the scale and the effect of shortening the pickling treatment time. In the table, double circles show the results with many fine cracks, single circles show the results with many cracks, triangles show the results with few cracks, and cross marks show the results with only a few large cracks. . As is clear from the table, good results could be obtained when the steel plate heating temperature was in the range of 150 to 300 ° C, and the best results could be obtained in the temperature range of 200 to 250 ° C.

【0036】酸洗処理時間短縮の効果については鋼板温
度を30℃とする従来方法を基準100%として各方法
の結果を調べた。実施例1では50%、実施例2では3
3%、実施例3では20%、実施例4では18%、実施
例5では20%、比較例1では40%、比較例2では4
2%、従来方法(80℃低温加熱)では85%、スケー
ルブレーキング法では90%という結果を得た。
Regarding the effect of shortening the pickling treatment time, the results of each method were examined with the conventional method at a steel plate temperature of 30 ° C. as a reference of 100%. 50% in Example 1, 3 in Example 2
3%, 20% in Example 3, 18% in Example 4, 20% in Example 5, 40% in Comparative Example 1, 4 in Comparative Example 2.
The results were 2%, 85% by the conventional method (80 ° C. low temperature heating) and 90% by the scale breaking method.

【0037】ちなみに、特開平4−297589号公報
には誘導加熱により鋼板温度を酸液温度(80℃)にま
で加熱して酸洗する方法が記載されている。しかし、こ
のような誘導加熱装置にて鋼板を80℃前後に加熱し酸
洗する方法では、前述の酸洗技術よりも酸洗時間短縮効
果が85%(基準となる総所要時間の15%が短縮され
る)と少ない。
By the way, Japanese Patent Laid-Open No. 4-297589 discloses a method of heating the steel sheet to an acid solution temperature (80 ° C.) by induction heating and pickling. However, in the method of heating a steel sheet to about 80 ° C. with such an induction heating device and pickling, the effect of shortening the pickling time is 85% (15% of the standard total required time is shorter than the pickling technique described above. Shortened) and less.

【0038】得られた結果について以下に若干の考察を
加える。鋼板加熱部において、100〜300℃の範囲
で加熱された鋼板は、酸液中(液温度80〜90℃)に
浸漬され、急激に冷却されることとなり、表層部に生成
しているスケールは、熱衝撃により割れを生じるととも
に、母材との熱膨張差により剥離する。前述したスケー
ルブレーカー設置による方法と同じ役割や作用を果たす
ものであるが、鋼板の加熱温度が150〜300℃の範
囲では、実施例2〜5のほうが微細なクラックが発生す
るとともに、溶接点近傍での脱スケール性低下によるラ
インスピード減速及び操業性悪化等の制約はなく、ま
た、長手方向の表面仕上りのむらという問題も生じな
い。
Some consideration will be given to the obtained results. In the steel plate heating part, the steel plate heated in the range of 100 to 300 ° C. is immersed in the acid solution (liquid temperature 80 to 90 ° C.) and rapidly cooled, and the scale generated in the surface layer part is In addition to cracking due to thermal shock, peeling occurs due to the difference in thermal expansion from the base material. Although it fulfills the same role and action as the method by installing the scale breaker described above, in the case where the heating temperature of the steel sheet is in the range of 150 to 300 ° C., fine cracks occur in Examples 2 to 5 and the vicinity of the welding point. There is no restriction such as deceleration of line speed and deterioration of operability due to deterioration of descaling property, and there is no problem of uneven surface finish in the longitudinal direction.

【0039】従来より、脱スケール性向上のためには酸
液の高濃度化および高温度化が効果的であることが知ら
れているが、装置上、あるいはコスト上の制約により実
行化されてはいない。しかし、高温装入酸洗法では鋼板
温度を酸液の沸点以上に加熱し酸液中へ浸漬することに
より、鋼板近傍においてのみ高濃度化および高温度化し
て、脱スケール化学反応の理想状態に達し、従来の技術
では得られなかった酸洗条件及び効果を得ることができ
る。
It has been conventionally known that increasing the concentration and temperature of the acid solution is effective for improving the descaling property, but it is realized by the limitation of the apparatus or the cost. There isn't. However, in the high-temperature charging pickling method, by heating the steel plate temperature above the boiling point of the acid solution and immersing it in the acid solution, the concentration and temperature are increased only near the steel plate, making it ideal for descaling chemical reactions. It is possible to obtain the pickling conditions and effects which cannot be obtained by the conventional technique.

【0040】次に、図2及び図3を参照しながら本実施
例の酸洗装置について説明する。図2は縦軸に酸洗槽の
時定数(分)をとり各槽ごとに応答性につき調べた結果
示すグラフ図である。酸洗槽の長さは20m、1つあた
りの槽容積は50m3 の条件である。図から明らかなよ
うに従来のような5〜6槽程度で構成される酸洗槽にお
いては、塩酸濃度・温度の応答性が遅く、きめ細かな制
御・管理が不可能であり、製品品質の安定供給が不可能
であった。しかし、本実施例の装置では、循環槽を採用
することにより数分以内に応答する結果が得られ、応答
性は著しく改善されるとともに製品品質の安定化が可能
となった。
Next, the pickling apparatus of this embodiment will be described with reference to FIGS. 2 and 3. FIG. 2 is a graph showing the results of examining the response of each tank with the time constant (minutes) of the pickling tank on the vertical axis. The length of the pickling tank is 20 m, and the tank volume per one is 50 m 3 . As is clear from the figure, in the conventional pickling tank consisting of about 5 to 6 tanks, the response of hydrochloric acid concentration and temperature is slow, and detailed control / management is not possible, resulting in stable product quality. The supply was impossible. However, in the apparatus of the present embodiment, the use of the circulation tank resulted in a response within a few minutes, and the responsiveness was remarkably improved and the product quality could be stabilized.

【0041】図3は横軸に処理鋼板1トンあたりの塩酸
供給量(kg/トン)をとって脱スケール性をA,B,
Cのランクをつけて評価した。図中にて白丸は濃度8.
0重量%の塩酸溶液(温度80℃)の結果を示し、白三
角は濃度4.0重量%の塩酸溶液(温度80℃)の結果
を示す。図から明らかなように塩酸溶液供給量の最適範
囲は60〜160(kg/トン)であることが判明し
た。また、最適範囲内では濃度8.0重量%の塩酸溶液
の場合はすべてAランク評価となったが、濃度4.0重
量%の塩酸溶液の場合はBランクからAランクまでにバ
ラツキを生じた。
In FIG. 3, the horizontal axis indicates the supply amount of hydrochloric acid per ton of treated steel sheet (kg / ton), and the descaling properties are A, B, and
It was evaluated by ranking C. In the figure, the white circles indicate the density 8.
The results of a 0 wt% hydrochloric acid solution (temperature 80 ° C.) are shown, and the open triangles show the results of a 4.0 wt% concentration hydrochloric acid solution (temperature 80 ° C.). As is clear from the figure, it was found that the optimum supply range of the hydrochloric acid solution was 60 to 160 (kg / ton). In the optimum range, all the hydrochloric acid solutions having a concentration of 8.0 wt% were ranked A, but the hydrochloric acid solutions having a concentration of 4.0 wt% were varied from rank B to rank A. .

【0042】次に、図4を参照しながら脱スケール性と
鋼板加熱温度との関係について説明する。図4は横軸に
鋼板加熱温度をとり、縦軸に脱スケール性をとって両者
の関係について調べた結果を示すグラフ図である。温度
80℃で濃度8重量%の塩酸溶液に同一の浸漬時間で鋼
板を浸漬して調べた。脱スケール性はA,B,C,D,
Eの5段階で評価した。図から明らかなように、脱スケ
ール性の評価は100〜300℃の温度域で良好であ
り、とくに150〜300℃の温度域ではAまたはBの
評価が得られた。
Next, the relationship between the descaling property and the steel plate heating temperature will be described with reference to FIG. FIG. 4 is a graph showing the results of examining the relationship between the two with the horizontal axis representing the steel plate heating temperature and the vertical axis representing the descaling property. A steel plate was immersed in a hydrochloric acid solution having a concentration of 8% by weight at a temperature of 80 ° C. for the same immersion time and examined. Descalability is A, B, C, D,
The evaluation was made in 5 grades of E. As is clear from the figure, the evaluation of the descaling property was good in the temperature range of 100 to 300 ° C, and the evaluation of A or B was obtained particularly in the temperature range of 150 to 300 ° C.

【0043】図5は、横軸に浸漬直前の鋼板と液面との
なす侵入角度θをとり、脱スケール性をA,B,Cのラ
ンクをつけて評価した。図中にて白丸は鋼板の両面とも
優秀な結果が得られたものを、黒丸は鋼板の両面とも劣
悪な結果となったものを、黒三角は鋼板の上面が劣悪な
結果となったものを、黒四角は鋼板の下面が劣悪な結果
となったものをそれぞれ示す。図から明らかなように、
侵入角度により酸洗性が影響を受けていることがわか
り、侵入角度θが30〜60゜の範囲のものはすべてA
ランク評価の結果が得られた。この要因としては、沸騰
時の気泡の影響が主なものであり、この影響を回避する
ためには侵入角度θを30〜60゜の範囲内に規定する
ことが不可欠である。
In FIG. 5, the horizontal axis represents the penetration angle θ formed by the steel plate and the liquid surface immediately before immersion, and the descaling property was evaluated by ranking A, B, and C. In the figure, white circles indicate that excellent results were obtained on both sides of the steel sheet, black circles indicate that both sides of the steel sheet were inferior, and black triangles indicate that the top surface of the steel sheet was inferior. , The black squares show the results that the lower surface of the steel plate was inferior. As is clear from the figure,
It can be seen that the pickling property is affected by the penetration angle, and A is for all penetration angles θ in the range of 30-60 °.
The result of rank evaluation was obtained. The main cause of this is the effect of bubbles during boiling, and in order to avoid this effect, it is essential to define the penetration angle θ within the range of 30 to 60 °.

【0044】得られた結果について以下に若干の考察を
加える。浸漬式酸洗反応の支配要因として、鋼板近傍の
酸液の新陳代謝の鈍化があり、従来技術においては噴流
・遮蔽板等の乱流プロモーターを備えることにより、酸
液を拡散させて問題解決にあたっている。高温装入酸洗
法では、以上の作用をも兼備している。加熱した鋼板を
酸液中に浸漬することにより、鋼板近傍は急激な熱移動
と物質移動を伴う沸騰現象(核沸騰域)となり、酸液の
新陳代謝が促進される。効果としては、物質移動が熱移
動(熱伝達率)にて置き換え可能であるとすると、乱流
プロモーター付加によるものの約10倍程度はあるもの
と推定される。
Some consideration will be given below to the obtained results. As a controlling factor of the immersion type pickling reaction, the metabolism of the acid solution near the steel plate is slowed down.In the conventional technology, the solution is diffused by providing a turbulent flow promoter such as a jet flow and a shielding plate to solve the problem. . The high-temperature charging pickling method also has the above-mentioned effects. By immersing the heated steel sheet in the acid solution, a boiling phenomenon (nucleate boiling region) accompanied by rapid heat transfer and mass transfer occurs near the steel sheet, and metabolism of the acid solution is promoted. As an effect, assuming that mass transfer can be replaced by heat transfer (heat transfer coefficient), it is estimated that there is about 10 times that due to the addition of a turbulent promoter.

【0045】上記の実施例の方法によれば従来方法より
も大幅な酸洗時間の短縮効果を得るとともに、設備のコ
ンパクト化を達成することができた。また、鋼板加熱部
にて鋼板加熱温度(鋼種別)、酸洗槽部にてラインスピ
ード、浸漬時間、塩酸条件(温度、濃度)を制御可能と
したことにより、均一かつ良好な薄鋼板を安定的に製造
することができる。
According to the method of the above-mentioned embodiment, the effect of shortening the pickling time to a great extent can be obtained as compared with the conventional method, and the equipment can be made compact. In addition, by controlling the steel plate heating temperature (steel type) in the steel plate heating part and the line speed, dipping time, and hydrochloric acid conditions (temperature, concentration) in the pickling tank part, uniform and good thin steel plate can be stabilized. Can be manufactured in a simple manner.

【0046】次に、表2を参照して本発明の実施例を比
較例と比べながら効果について説明する。表2は、鋼板
加熱温度を種々変えて板形状のくずれ及び蛇行について
評価した。なお、総合評価は板形状のくずれ及び蛇行の
各評価を勘案して決定したものである。表中にて丸は良
好な結果を示し、三角は実用上とくに問題ない結果を示
し、バツマークは実用上に問題がある結果を示す。
Next, referring to Table 2, the effects will be described while comparing the embodiment of the present invention with the comparative example. In Table 2, the steel plate heating temperature was variously changed and the deformation and the meandering of the plate shape were evaluated. The comprehensive evaluation is determined in consideration of the evaluation of the plate shape collapse and the meandering. In the table, circles indicate good results, triangles indicate results that are not particularly problematic for practical use, and cross marks indicate results that are problematic for practical use.

【0047】鋼板加熱温度が100〜300℃の温度域
では良好な結果が得られたが、300℃以上の温度域に
なる350℃及び400℃では板形状のくずれ(温度差
などに起因する局部座屈変形などによる板形状の乱れ)
が大きく、実用に供することができない。このように鋼
板加熱温度(300℃以上)と酸液温度(80〜90
℃)との温度差が250℃以上になると、急激な温度変
化による板形状のくずれを生じて、通板性が悪化するこ
とが判明した。また、鋼板を100℃以上に加熱すると
腰折れ(薄鋼板の製品欠陥となる座屈)が発生するが、
図1の実施例のようにパスを縦型として、ロール径に制
約(φ≧0.32)を設けることで解消した。
Good results were obtained in the temperature range of the steel sheet heating temperature of 100 to 300 ° C., but at 350 ° C. and 400 ° C. in which the temperature range of 300 ° C. or higher was reached, the shape of the plate was distorted (local difference due to temperature difference, etc.). Distortion of plate shape due to buckling deformation)
Is too large to be put to practical use. In this way, the steel plate heating temperature (300 ° C or higher) and the acid liquid temperature (80 to 90
It has been found that when the temperature difference between the temperature and the temperature is 250 ° C. or more, the plate shape is collapsed due to a rapid temperature change and the sheet passing property is deteriorated. Further, when the steel sheet is heated to 100 ° C. or higher, waist bending (buckling which is a product defect of thin steel sheet) occurs,
As in the embodiment of FIG. 1, the path is vertical and the roll diameter is restricted (φ ≧ 0.32) to solve the problem.

【0048】以上を実施し採用することにより、酸洗処
理時間の短縮及び設備のコンパクト化が可能となり、酸
洗仕上りが良好で表面性状に優れた鋼板を製造すること
ができる。なお、この発明の技術は、金属材料全般にわ
たる脱スケール方法に応用することが可能である。
By carrying out and adopting the above, it becomes possible to shorten the pickling time and make the equipment compact, and it is possible to manufacture a steel sheet having a good pickling finish and excellent surface properties. The technique of the present invention can be applied to a descaling method for all metal materials.

【0049】[0049]

【表1】 [Table 1]

【0050】[0050]

【表2】 [Table 2]

【0051】[0051]

【発明の効果】この発明によれば、誘導加熱装置を酸洗
槽の前段に設置し、酸洗槽へ装入される鋼板を酸液の沸
点以上の温度範囲に加熱して、脱スケール処理を行うよ
うにしたので、大幅な酸洗処理時間の短縮及び酸洗槽の
数の減少が可能になるとともに、大幅な設備費の低廉化
効果を得ることができる。
According to the present invention, the induction heating device is installed in the preceding stage of the pickling tank, and the steel sheet charged into the pickling tank is heated to a temperature range not lower than the boiling point of the acid solution to perform descaling treatment. As a result, it is possible to significantly shorten the pickling time and the number of pickling tanks, and it is possible to significantly reduce the cost of equipment.

【0052】また、鋼板加熱部にて鋼板加熱温度(鋼種
別)、酸洗槽部にてラインスピード、浸漬時間、塩酸条
件(温度、濃度)を制御可能としたことにより、均一か
つ良好な薄鋼板を安定的に製造することができる。
Further, by controlling the steel sheet heating temperature (steel type) in the steel sheet heating section and the line speed, immersion time, and hydrochloric acid conditions (temperature, concentration) in the pickling tank section, uniform and good thinness can be achieved. A steel plate can be manufactured stably.

【0053】とくに酸洗槽内にシンクロールを設け、シ
ンクロールによって液中への鋼板の浸漬時間を制御する
こと、および酸液濃度制御、および鋼板温度制御の組合
せにより可能である。
In particular, it is possible by providing a sink roll in the pickling tank, controlling the immersion time of the steel sheet in the liquid by the sink roll, and controlling the acid solution concentration control and the steel plate temperature control.

【0054】さらに、酸洗槽内には高温装入酸洗法実施
による液温度上昇を防止する熱交換器を設けるととも
に、回収した熱水は出側のリンス水へと利用することに
より省エネルギーを図ることができる。
Furthermore, a heat exchanger is provided in the pickling tank to prevent the temperature rise of the liquid due to the high temperature charging pickling method, and the recovered hot water is used as the rinse water on the outlet side to save energy. Can be planned.

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

【図1】本発明の実施例に係る薄鋼板の酸洗装置が用い
られた酸洗ラインの一部を示す模式図。
FIG. 1 is a schematic view showing a part of a pickling line in which a pickling apparatus for thin steel sheets according to an embodiment of the present invention is used.

【図2】各酸洗槽における応答性の結果を示すグラフ
図。
FIG. 2 is a graph showing the results of responsiveness in each pickling tank.

【図3】酸液必要供給量により脱スケール性を評価した
結果を示すグラフ図。
FIG. 3 is a graph showing the results of evaluation of descaling property based on the required supply amount of acid solution.

【図4】鋼板加熱温度と脱スケール性との相関関係につ
いて調べた結果を示すグラフ図。
FIG. 4 is a graph showing the results of examining the correlation between the steel plate heating temperature and the descaling property.

【図5】鋼板侵入角度と脱スケール性との相関関係につ
いて調べた結果を示すグラフ図。
FIG. 5 is a graph showing the results of examining the correlation between the steel plate penetration angle and the descaling property.

【図6】従来の酸洗装置を示す模式図である。FIG. 6 is a schematic view showing a conventional pickling apparatus.

【符号の説明】[Explanation of symbols]

1…鋼板、12…ブライドルロール、13…誘導加熱装
置、15…温度計、16…酸洗槽、17…シンクロー
ル、18…固定ロール、20…リンス槽、22…腰折れ
防止ロール、30…演算部、40…制御部。
DESCRIPTION OF SYMBOLS 1 ... Steel plate, 12 ... Bridle roll, 13 ... Induction heating device, 15 ... Thermometer, 16 ... Pickling tank, 17 ... Sink roll, 18 ... Fixed roll, 20 ... Rinse tank, 22 ... Waist-bending prevention roll, 30 ... Calculation Part, 40 ... Control part.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 鋼板を加熱する鋼板加熱部と、鋼板が浸
漬される酸洗槽部と、酸液の濃度及び温度を制御する酸
液循環槽部とを備え、鋼板を連続的に脱スケール処理す
る薄鋼板の酸洗装置であって、 前記鋼板加熱部は、前記酸洗槽部入り側のブライドルロ
ールと酸洗槽との間に設けられた鋼板加熱装置と、加熱
された鋼板の温度を測定するための温度計と、腰折れ防
止ロールと、を有し、 前記酸洗槽部は、鋼板浸漬時間制御用のシンクロール
と、酸洗槽部の下部より酸液、スケール、及びその他の
不溶解物を排出する手段と、を有し、 前記循環槽部は、前記酸洗槽部の下部に設けられ、上部
酸洗槽内の酸液の濃度及び温度を調整制御するために酸
液を上部酸洗槽へ循環供給するとともに、鋼板から酸液
へ移行した排熱を回収する熱交換器を有することを特徴
とする薄鋼板の酸洗装置。
1. A steel plate heating unit for heating a steel plate, a pickling tank unit in which the steel plate is immersed, and an acid solution circulation tank unit for controlling the concentration and temperature of the acid solution, and the steel plate is continuously descaled. A pickling device for a thin steel plate to be processed, wherein the steel plate heating unit is a steel plate heating device provided between the bridle roll and the pickling tank on the side of the pickling tank, and the temperature of the heated steel plate. A thermometer for measuring, and a waist bending prevention roll, and, the pickling tank part, a sink roll for steel plate immersion time control, an acid solution from the bottom of the pickling tank part, scale, and other And a means for discharging insoluble matter, wherein the circulation tank section is provided in a lower portion of the pickling tank section, and the acid solution for adjusting and controlling the concentration and temperature of the acid solution in the upper pickling tank. Circulates and supplies it to the upper pickling tank, and has a heat exchanger to recover the exhaust heat transferred from the steel plate to the acid solution. A pickling device for thin steel sheets, which is characterized by:
【請求項2】 さらに、鋼種、鋼板温度、シンクロール
位置、酸液条件が検出データまたは初期設定データとし
て入力され、これらの入力データに基づき鋼板加熱温度
および鋼板浸漬時間を求める演算部と、 求めた鋼板加熱温度に基づき鋼板加熱部の加熱動作を制
御して鋼板浸漬時に鋼板に接する酸液が核沸騰状態にな
る温度域まで鋼板を酸液浸漬前に加熱するとともに、求
めた鋼板浸漬時間に基づきシンクロール動作を制御して
鋼板の浸漬深さを調節する制御部と、を有することを特
徴とする請求項1記載の薄鋼板の酸洗装置。
2. Further, a steel type, a steel plate temperature, a sink roll position, and an acid solution condition are inputted as detection data or initial setting data, and a calculation unit for calculating a steel plate heating temperature and a steel plate immersion time based on these input data, The heating operation of the steel plate heating part is controlled based on the steel plate heating temperature, and the steel plate is heated to a temperature range in which the acid liquid contacting the steel plate during the steel plate immersion is in the nucleate boiling state before the steel plate is immersed in the steel plate. 2. A pickling apparatus for thin steel sheet according to claim 1, further comprising: a control unit that controls a sink roll operation based on the control unit to adjust the immersion depth of the steel sheet.
【請求項3】 鋼板を加熱し、加熱した鋼板を酸液中に
浸漬して連続的に脱スケール処理する薄鋼板の酸洗方法
であって、 鋼板浸漬時に鋼板に接する酸液が核沸騰状態になる温度
域まで鋼板を酸液浸漬前に加熱し、加熱直後に鋼板を酸
液に浸漬することを特徴とする薄鋼板の酸洗方法。
3. A pickling method for a thin steel sheet, comprising heating a steel sheet, immersing the heated steel sheet in an acid solution, and continuously performing descaling, wherein the acid solution in contact with the steel sheet during immersion is in a nucleate boiling state. A method for pickling a thin steel sheet, which comprises heating the steel sheet to a temperature range of 1% before being immersed in the acid solution, and immediately immersing the steel sheet in the acid solution.
【請求項4】 鋼板加熱温度を100〜300℃の範囲
とし、インヒビターを含む塩酸溶液に対して鋼板を浸漬
する際に液面と鋼板とのなす鋭角としての鋼板侵入角度
を30〜60°の範囲とすることを特徴とする請求項3
記載の薄鋼板の酸洗方法。
4. The steel plate heating temperature is set in the range of 100 to 300 ° C., and when the steel plate is immersed in a hydrochloric acid solution containing an inhibitor, the steel plate penetration angle as an acute angle between the liquid surface and the steel plate is 30 to 60 °. It is set as the range.
A method for pickling a thin steel sheet as described above.
【請求項5】 濃度4.0〜8.0重量%の塩酸溶液を
鋼板1トンあたり60〜150kgの割合で酸洗槽部へ
循環供給することを特徴とする請求項4記載の薄鋼板の
酸洗方法。
5. The thin steel sheet according to claim 4, wherein a hydrochloric acid solution having a concentration of 4.0 to 8.0% by weight is circulated and supplied to the pickling tank section at a rate of 60 to 150 kg per ton of steel sheet. Pickling method.
【請求項6】 鋼板を加熱する鋼板加熱部と、鋼板が浸
漬される酸洗槽部と、酸液の濃度及び温度を制御する酸
液循環槽部とを備え、鋼板を連続的に脱スケール処理す
る薄鋼板の酸洗装置であって、前記鋼板加熱部は、前記
酸洗槽部入り側のブライドルロールと酸洗槽との間に設
けられた鋼板加熱装置と、加熱された鋼板の温度を測定
するための温度計と、腰折れ防止ロールと、を有し、前
記酸洗槽部は、鋼板浸漬時間制御用のシンクロールと、
酸洗槽部の下部より酸液、スケール、及びその他の不溶
解物を排出する手段と、を有し、前記循環槽部は、前記
酸洗槽部の下部に設けられ、上部酸洗槽内の酸液の濃度
及び温度を調整制御するために酸液を上部酸洗槽へ循環
供給するとともに、鋼板から酸液へ移行した排熱を回収
する熱交換器を有する薄鋼板の酸洗装置を用いて鋼板を
酸洗処理する際に、 インヒビターを含み、かつ濃度4.0〜8.0重量%の
塩酸溶液を鋼板1トンあたり60〜150kgの割合で
酸洗槽部へ循環供給し、 鋼板加熱温度を100〜300℃の範囲とし、 酸液の液面と鋼板とのなす鋭角としての鋼板侵入角度が
30〜60°の範囲になるように塩酸溶液に対して鋼板
を浸漬することを特徴とする薄鋼板の酸洗方法。
6. A steel plate heating unit for heating a steel plate, a pickling tank unit in which the steel plate is immersed, and an acid solution circulating tank unit for controlling the concentration and temperature of the acid solution, and continuously descaling the steel plate. A pickling device for a thin steel plate to be treated, wherein the steel plate heating unit is a steel plate heating device provided between the bridle roll and the pickling tank on the side of the pickling tank, and the temperature of the heated steel plate. A thermometer for measuring, and a waist bend preventing roll, and the pickling tank part, a sink roll for steel plate immersion time control,
Means for discharging the acid solution, scale, and other insolubles from the lower part of the pickling tank part, the circulation tank part is provided in the lower part of the pickling tank part, and in the upper pickling tank In order to regulate and control the concentration and temperature of the acid solution, the acid solution is circulated and supplied to the upper pickling tank, and a pickling device for thin steel sheets having a heat exchanger that recovers the exhaust heat transferred from the steel sheet to the acid solution When a steel sheet is subjected to pickling treatment using, a hydrochloric acid solution containing an inhibitor and having a concentration of 4.0 to 8.0% by weight is circulated and supplied to the pickling tank portion at a rate of 60 to 150 kg per ton of the steel sheet. The heating temperature is set in the range of 100 to 300 ° C., and the steel plate is immersed in the hydrochloric acid solution so that the steel plate penetration angle as an acute angle formed by the acid liquid surface and the steel plate is in the range of 30 to 60 °. Pickling method for thin steel sheet.
JP7156160A 1995-06-22 1995-06-22 Pickling device and pickling method for thin steel sheet Pending JPH093673A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7156160A JPH093673A (en) 1995-06-22 1995-06-22 Pickling device and pickling method for thin steel sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7156160A JPH093673A (en) 1995-06-22 1995-06-22 Pickling device and pickling method for thin steel sheet

Publications (1)

Publication Number Publication Date
JPH093673A true JPH093673A (en) 1997-01-07

Family

ID=15621665

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7156160A Pending JPH093673A (en) 1995-06-22 1995-06-22 Pickling device and pickling method for thin steel sheet

Country Status (1)

Country Link
JP (1) JPH093673A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100419784B1 (en) * 1999-12-29 2004-02-21 주식회사 포스코 Apparatus for eliminating scale of stainless steal strip
KR100470410B1 (en) * 2002-05-29 2005-02-07 주식회사 포스코 Pickling method for reducing hot spot of cold rolled strip surface
WO2017104926A1 (en) * 2015-12-18 2017-06-22 주식회사 포스코 Pickling apparatus and pickling method
CN108560010A (en) * 2018-01-18 2018-09-21 广东嘉元科技股份有限公司 A kind of pickling mechanism and its control method
CN111390570A (en) * 2020-03-31 2020-07-10 日照宝华新材料有限公司 Method for mutual conversion between acid pickling coil and hot rolling leveling on acid leveling line

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100419784B1 (en) * 1999-12-29 2004-02-21 주식회사 포스코 Apparatus for eliminating scale of stainless steal strip
KR100470410B1 (en) * 2002-05-29 2005-02-07 주식회사 포스코 Pickling method for reducing hot spot of cold rolled strip surface
WO2017104926A1 (en) * 2015-12-18 2017-06-22 주식회사 포스코 Pickling apparatus and pickling method
US10704151B2 (en) 2015-12-18 2020-07-07 Posco Pickling apparatus and pickling method
CN108560010A (en) * 2018-01-18 2018-09-21 广东嘉元科技股份有限公司 A kind of pickling mechanism and its control method
CN108560010B (en) * 2018-01-18 2023-06-27 广东嘉元科技股份有限公司 Pickling mechanism and control method thereof
CN111390570A (en) * 2020-03-31 2020-07-10 日照宝华新材料有限公司 Method for mutual conversion between acid pickling coil and hot rolling leveling on acid leveling line
CN111390570B (en) * 2020-03-31 2021-07-06 日照宝华新材料有限公司 Method for mutual conversion between acid pickling coil and hot rolling leveling on acid leveling line

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