JPS60124411A - Control method of finishing temperature of rolling mill - Google Patents

Control method of finishing temperature of rolling mill

Info

Publication number
JPS60124411A
JPS60124411A JP58232746A JP23274683A JPS60124411A JP S60124411 A JPS60124411 A JP S60124411A JP 58232746 A JP58232746 A JP 58232746A JP 23274683 A JP23274683 A JP 23274683A JP S60124411 A JPS60124411 A JP S60124411A
Authority
JP
Japan
Prior art keywords
temperature
finishing
rolling
control device
mill
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
JP58232746A
Other languages
Japanese (ja)
Inventor
Nobuyuki Togashi
富樫 伸行
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.)
Hitachi Ltd
Original Assignee
Hitachi 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 Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP58232746A priority Critical patent/JPS60124411A/en
Publication of JPS60124411A publication Critical patent/JPS60124411A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B37/00Control devices or methods specially adapted for metal-rolling mills or the work produced thereby
    • B21B37/74Temperature control, e.g. by cooling or heating the rolls or the product

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Control Of Metal Rolling (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

PURPOSE:To control uniformly a temperature of material at the outlet side of finishing rolling by operating and setting a finishing rolling-speed by using a target finishing temperature of material and a measured temperature of material at the inlet side of the finishing rolling, and changing a soaking temperature in a heating furnace in accordance with the deviation of the measured temperature from a set value. CONSTITUTION:In a rolling installation furnished with a coil box 10 between a roughing mill 8 and a finishing mill; a control device 1 inputs a material temperature TS at the inlet side of a finishing rolling from a thermometer 7b, and calculates a finishing rolling-speed VF to set it to a speed control device 9 so as to achieve a target finishing temperature TFO of material given by a computor 14. Next the device 1 makes a sampling of the material temperature at the outlet side of finishing rolling by using a thermometer 11, and outputs a water-flow-rate changing command to a spray-cooling- water control device 20 when the temperature deviates from an allowable tolerance of target temperature, and outputs a soaking-time changing command to the combustion control device 2 of a heating furnace 3 when a long-term learning control is required after finishing the rolling. In this way, the whole length of material is controlled to a desired temperature at the outlet side if finishing rolling, without changing the finishing rolling-speed.

Description

【発明の詳細な説明】 〔発明の利用分野〕 本発明は熱間仕上圧延機の仕上温度制御方法に関する。[Detailed description of the invention] [Field of application of the invention] The present invention relates to a finishing temperature control method for a hot finishing rolling mill.

〔発明の背景〕[Background of the invention]

熱間仕上圧延機における仕上温度制御については、従来
仕上入側温度または、粗圧延機出側温度より仕上出側温
度を子側し、“圧延中は速度変更またはスタンド間スプ
レー冷却水による制御を行ない所定の温度を得るように
していた。ここでの考え方は、仕上圧延速度、スタンド
間スプレー冷却水量、仕上入側温度(または粗圧延機出
側温度)が与えられる入力情報であり、仕上目標温度を
達成すべく制御するパラメータとしては、仕上圧延速!
’に変えるだめの加速率、スタンド間スプレー冷却水量
および仕上圧延機入側での待機等があった。
Regarding finishing temperature control in hot finishing rolling mills, conventionally, the finishing exit temperature is set lower than the finishing entry temperature or the roughing mill exit temperature, and "During rolling, control is performed by changing the speed or using cooling water sprayed between stands." The idea here is that the finishing rolling speed, the amount of cooling water sprayed between stands, and the finishing inlet temperature (or roughing mill outlet temperature) are input information, and the finishing target is Finish rolling speed is a parameter to be controlled to achieve the desired temperature!
These included the acceleration rate of the rolling stock, the amount of cooling water sprayed between stands, and the waiting time at the entrance of the finishing mill.

最近、鉄鋼のプロセスは大量生産万代より小品種小量生
産に移らざる會得ない状況となっておシ、更に従来に増
し省エネルギー圧延および商品質材生産がめられつつあ
る。このような要求に答えるべく熱間圧延プロセスにお
いて近年新開発されたものにコイルボックスがある。こ
の原理は第1図の10に示すように一種のコイル巻取装
置で、粗圧延機8と仕上圧延機6の間に設置され、粗圧
延機で圧延しながらこのコイルボックスに巻取ってゆく
ものである。粗圧延機における圧延が終了し巻取った後
、第2図に示すように今度は仕上圧延機で圧延を開始す
る。このコイルボックスの効果は次のとおりである。す
なわち、第1に従来のプロセスより粗圧延機と仕上圧延
機の間の距離が短くなり設備費が少なくなること、第2
に非常に重要なことであるが仕上圧延機に入る材料の全
長にわたって温度が一定になること、いいかえると仕上
温度が一定となることである。これを第3図金用囚説明
する。
Recently, the steel manufacturing process has been forced to shift from mass production to small-variety, small-lot production, and more energy-saving rolling and commodity material production are being sought than ever before. A coil box has been newly developed in recent years in the hot rolling process to meet these demands. This principle is based on a type of coil winding device, as shown in 10 in Figure 1, which is installed between a rough rolling mill 8 and a finishing mill 6, and winds the coil into this coil box while being rolled by the rough rolling mill. It is something. After the rolling in the rough rolling mill is completed and the material is wound up, rolling is started in the finishing mill as shown in FIG. The effects of this coil box are as follows. In other words, firstly, the distance between the roughing mill and finishing mill is shorter than in the conventional process, resulting in lower equipment costs;
What is very important in this process is that the temperature be constant over the entire length of the material entering the finishing mill, or in other words, that the finishing temperature be constant. This will be explained in Figure 3.

第3図は従来のプロセスにおける仕上圧延機入側での材
料温度と粗圧延機出側温度との関係ケ示す。通常粗圧延
機出側温度TRは材料の全長にわたりほぼ同一の温度を
示す。しかし仕上入側温度は材料の圧延の進行につれ低
下する。その理由は、材料表面からの熱放射、空中への
熱伝導による温腋低下のためである。すなわち、厚みH
の材料がt時間仕上圧延機入側で放置されると、材料温
度は次のような式で表わされるように温度は低下してゆ
く。
FIG. 3 shows the relationship between the material temperature at the entrance of the finishing mill and the temperature at the exit of the roughing mill in the conventional process. Normally, the rough rolling mill outlet temperature TR is approximately the same temperature over the entire length of the material. However, the finishing entry temperature decreases as the rolling of the material progresses. The reason for this is that heat radiation from the material surface and heat conduction into the air reduce armpit temperature. That is, the thickness H
When the material is left at the entry side of the finishing mill for t hours, the material temperature decreases as expressed by the following equation.

Ts’仕上入側での材料温度 Tn’粗圧延機出側での材料温度 第3図における仕上入側温度の場合、粗圧延機出側から
仕上入側まで到達する時間(tl−1I1分すでに温度
降下している。そして更に(”4 ’2)時間かかつて
全ての材料が仕上圧延機に入ってゆく。
Ts'Material temperature at the finishing input side Tn'Material temperature at the exit side of the rough rolling millIn the case of the finishing input side temperature in Figure 3, the time to reach from the exit side of the rough rolling mill to the finishing input side (tl-1I1 minute already The temperature is dropping and after another (4'2) hours all the material enters the finishing mill.

第4図は、コイルポックおの場合の温度曲線を示す。コ
イルボックスに巻取られた材料の場合、ボックスによる
保温効果に加え、コイル状となった材料が自らを温める
ためコイル全体が一定の温度に保たれ、仕上圧延される
場合も仕上入側温度はほぼ初期値を保つことができる。
Figure 4 shows the temperature curve for the coil pock case. In the case of a material wound into a coil box, in addition to the heat insulation effect of the box, the coiled material warms itself, so the entire coil is kept at a constant temperature, and even when finishing rolling is performed, the temperature at the finishing input side remains constant. It is possible to maintain almost the initial value.

これは空中に放射、伝熱される熱量が少ないためであり
、またコイル状のため巻きほどして込つでも最後の部分
の材料は保温効果により温度降下が少ないからである。
This is because the amount of heat that is radiated and transferred into the air is small, and because it is coiled, even if it is unwound, the temperature of the last part of the material will not drop much due to its heat retention effect.

このようにコイルボックスの重要な効果は仕上入側温度
を全長にわたり一定にできることである。
As described above, the important effect of the coil box is that the finishing entrance temperature can be kept constant over the entire length.

効果としての第一3点は省エネルギーの特徴である。第
2の効果の所でも説明したが、−コイルボックスには保
温効果があることである。このことは次のことを意味す
る。すなわち、仕上入側温度を変えないとすると、コイ
ルボックスの場合紘粗出側温度が低くともよく、その発
願熱炉抽出温度を低くしてもよいことである。
The first three effects are energy saving features. As explained in the second effect, the coil box has a heat retention effect. This means: That is, assuming that the finishing input side temperature is not changed, the coil box output side temperature may be low, and the heating furnace extraction temperature thereof may be low.

このように多くの特徴を持ったコイルボックスの機能會
うまく生がした仕上圧延機制御ケ行なう必要がある。仕
上入側温度が一定値の時は、仕上出側温度も一定値のま
ま圧延することができ、またホットランテーブルでのス
プレー冷却水制御を容易にまた精度よく制御できること
が期待でき結果として高品質の圧延材を生産できる。
It is necessary to control a finishing rolling mill that takes advantage of the functions of a coil box that has many of these features. When the finishing inlet temperature is constant, the finishing outlet temperature can be rolled at a constant value, and it is expected that the spray cooling water on the hot run table can be controlled easily and accurately, resulting in high quality. can produce rolled material.

〔発明の目的〕[Purpose of the invention]

本発明は、コイルボックスの特徴である材料温度一定値
を生かし、仕上圧延速度を変化させずに定められた仕上
出側温度に材料全長がなるよう制御し省エネルギーと高
品質材の生産を実現するKある。
The present invention takes advantage of the constant material temperature, which is a feature of the coil box, and controls the entire length of the material so that it reaches a predetermined finishing exit temperature without changing the finishing rolling speed, thereby saving energy and producing high-quality materials. There is K.

〔発明の概要〕[Summary of the invention]

本発明の特徴は粗圧延機と仕上圧延機との間にコイルボ
ックスを設けた圧延設備において、仕上圧延温度を設定
し、コイルボックスから仕上圧延機への入側被圧延機速
度を検出し、前記温度換出値から仕上圧延速度を演算設
定し、前記仕上圧延温度設定値と前記仕上圧延機出側温
度との偏差に応じて加熱炉の均熱時間全変更し、前記仕
上圧延機出側温度を制御することにある。
The feature of the present invention is that in a rolling equipment in which a coil box is provided between a rough rolling mill and a finishing rolling mill, the finishing rolling temperature is set, the speed of the rolling mill on the entry side from the coil box to the finishing rolling mill is detected, A finish rolling speed is calculated and set from the converted temperature value, the soaking time of the heating furnace is completely changed according to the deviation between the finish rolling temperature set value and the finish rolling mill exit temperature, and the finishing rolling speed is set at the finishing rolling mill exit side. The purpose is to control the temperature.

〔発明の実施例〕[Embodiments of the invention]

はじめに本発明の基本的事項にっ^て述べる。 First, the basic matters of the present invention will be described.

仕上圧延速度は以下のように決定される。The finish rolling speed is determined as follows.

従来の制御装置は、材料仕様などより与えられる入力情
報であったが、本発明では所定の仕上温度に制御するた
め制御装置側で仕上出側温度Tyと仕上圧延速度V’y
 k次の関係式により決定する。
In the conventional control device, the input information was given from material specifications, etc., but in the present invention, in order to control the finishing temperature to a predetermined value, the control device side inputs the finishing exit temperature Ty and finishing rolling speed V'y.
Determined by a k-th order relational expression.

これによりVνをめると ここでTrは所定の仕上出口温度、Hは材料厚みである
。また、圧延時の制御は圧延時仕上出口温度が所定値を
中心とする許容公差内に入らない時に仕上圧延機のスタ
ンド間スプレー流量1に変えて制御を行なう。
As a result, Vv is calculated, where Tr is the predetermined finishing exit temperature and H is the material thickness. Further, control during rolling is performed by changing the inter-stand spray flow rate of the finishing rolling mill to 1 when the finishing outlet temperature during rolling does not fall within an allowable tolerance centered on a predetermined value.

オだ仕上出側温度TFの定周期サンプリングを圧延中に
行ない、サンプリングされた温度データkTr+とする
と% TF+の平均値と目標値Troからのずれの二乗
平均値をめ温度の安定性を確める。
Periodic sampling of the finishing exit temperature TF is performed during rolling, and the temperature stability is confirmed by determining the average value of %TF+ and the root mean square value of the deviation from the target value Tro, where the sampled temperature data is kTr+. Ru.

捷ずTyの平均値〒rは n;サンプリング回数 次に、目標値からのずれの二乗平均値をめるそして学習
制御の考え方は次のとうりである。
The average value of unselected Ty 〒r is n; the number of samplings. Next, calculate the root mean square value of the deviation from the target value.The idea of learning control is as follows.

TFとTPOの差が許容公差をオーバした時I ’I’
vo TF l =IΔTrl>ΔTPO−・・−−−
−(6)すなわち、この時はβ番×ΔTyを仕上圧延速
度式(3)にフィードバックし次の材料への短期学習制
御とする。次に72に関しある値γより大きい時72≧
γ ・・・・・・・・・・・・・・・・・・・・・・・
団・・旧・・(7)この時は、長期的な学習として炉燃
焼制御装置へフィードバックし材料の在炉時間ケ長くし
均熱状態を保ち材料内に温度むらをなくすようにする。
I 'I' when the difference between TF and TPO exceeds the allowable tolerance
vo TF l =IΔTrl>ΔTPO−・・−−
-(6) That is, at this time, β number x ΔTy is fed back to the finish rolling speed formula (3) to perform short-term learning control for the next material. Next, when 72 is larger than a certain value γ, 72≧
γ・・・・・・・・・・・・・・・・・・・・・・・・
Group... Old... (7) At this time, as a long-term study, feed back to the furnace combustion control device to lengthen the time the material is in the furnace, maintain a uniform heat state, and eliminate temperature unevenness within the material.

以上の本発明の概要を第5図のフロー図で示す。An overview of the present invention described above is shown in the flow diagram of FIG.

次に本発明の実施例?第6図に示す。第6図においてl
は本発明に係る圧延機制御装置で計算機などが用いられ
る。2は加熱炉燃焼制御装置、3は加熱炉である。8は
粗圧延機、lOはコイルボックス、6は仕上圧延機ケ示
す。7aは粗圧延機出側温度計、71)は仕上入側温度
計、9は仕上圧延速度制御装置、20はスタンド間スプ
レー冷却水制御装置を示す。11は仕上出側温度計、1
2はランアウトテーブルスプレー冷却水装置、13はダ
ウンコイラー會示す。
Next, an example of the present invention? It is shown in FIG. In Figure 6, l
A computer or the like is used in the rolling mill control device according to the present invention. 2 is a heating furnace combustion control device, and 3 is a heating furnace. 8 is a rough rolling mill, IO is a coil box, and 6 is a finishing mill. 7a is a rough rolling mill exit side thermometer, 71) is a finishing inlet side thermometer, 9 is a finish rolling speed control device, and 20 is an inter-stand spray cooling water control device. 11 is the finish exit side thermometer, 1
2 is a run-out table spray cooling water system, and 13 is a down coiler system.

第6図において、圧延機制御装置lは仕上入側温度計7
bより実際の仕上入側温度Tsk入力し、ビジネスコン
ピュータ14より与えられた仕上目標温度Trok達成
すべく(3)式により仕上圧延速度Vvk計算し、仕上
圧延速度制御装置9に仕上圧延速度全設定する。圧延が
始まり、材料が仕上用1i111速度制御装置9は特別
な装置ではなく通常用いられているような速度制御装置
があればよく、詳細については省略している。圧延がけ
じ捷り、材料が出側温度計11に達したのち実際の仕上
出側温度ケ圧延機制御装#lはサンプリングを行なう。
In FIG. 6, the rolling mill control device l is a finishing entry side thermometer 7.
Enter the actual finish entry temperature Tsk from b, calculate the finish rolling speed Vvk using equation (3) to achieve the target finish temperature Trok given by the business computer 14, and set all finish rolling speeds to the finish rolling speed control device 9. do. Rolling is started and the material is finished 1i111 The speed control device 9 is not a special device and may be any speed control device commonly used, and its details are omitted. After the rolling is interrupted and the material reaches the exit thermometer 11, the rolling mill control system #1 samples the actual finishing exit temperature.

この時目標温度許容公差からはずれた場合はスタンド間
スプレー冷却水制御装置ioに対し水量変更指令音出力
する。圧延が終了した後、圧延機制御装置lは(4)、
 (5)、 (6)式により学習制御’i11に行ない
長期学習制御が必要な場合は加熱炉燃焼制御装置2に対
し均熱時間変更指令倉出し、短期学習制御が心太な場合
は自分自身に対し次材料へのフィードバック指令を出す
At this time, if the target temperature deviates from the allowable tolerance, a water amount change command sound is output to the inter-stand spray cooling water control device io. After the rolling is finished, the rolling mill control device l (4)
(5) and (6) are used in the learning control 'i11. If long-term learning control is required, a soaking time change command is sent to the heating furnace combustion control device 2, and if short-term learning control is insufficient, it is sent to the In response, a feedback command is issued to the next material.

このようにしてコイルボックスの特徴を生かした制御ヲ
行ない、仕上出側温度が一定で結果として高品質の材料
?得ることができる。
In this way, we perform control that takes advantage of the characteristics of the coil box, resulting in a constant finishing exit temperature and a high quality material. Obtainable.

〔発明の効果〕〔Effect of the invention〕

本発明によるとコイルボックス付圧延設備における仕上
温度の効率のよい制御をおこなうことができる。
According to the present invention, it is possible to efficiently control the finishing temperature in a rolling equipment equipped with a coil box.

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

第1図はコイルポックスケ用いた粗圧延の例?示す。第
2図はコイルボックスを用いた仕上圧延の例全示す。第
3図は従来の熱間圧延における粗圧延機出側温度TRと
仕上入側温度Tsとの時間変化を示す図である。第4図
はコイルポックスケ用いた場合の粗圧延他出1則幅夏T
Rと仕上入側温度Tsとの時間変化を示す図である。第
5図は本発明の原理ケフローで示したものである。第6
図は本発明の実施例を示す。 l・・・計算機、3・・・加熱炉、9・・・圧延速度制
御装置、茅 1 目 茅3目 茅4− 目 ’Iy5 口
Is Figure 1 an example of rough rolling using a coil pox? show. FIG. 2 shows a complete example of finish rolling using a coil box. FIG. 3 is a diagram showing changes over time in the rough rolling mill outlet temperature TR and the finishing input side temperature Ts in conventional hot rolling. Figure 4 shows the width and summer T of rough rolling when using a coil pox.
It is a figure which shows the time change of R and finishing entry side temperature Ts. FIG. 5 is a diagram illustrating the principle of the present invention. 6th
The figure shows an embodiment of the invention. l...Calculator, 3...Heating furnace, 9...Rolling speed control device, grass 1 eye 3 eyes 4- eyes 'Iy5 mouth

Claims (1)

【特許請求の範囲】[Claims] 1、粗圧延機と仕上圧延機の間にコイルポックスケ有す
る圧延設備の仕上温度制御方法において、与えられた仕
上目標温度と測定した粗圧延機出側温度または、仕上入
側温度を用い仕上圧延速度全演算設定し、測定した仕上
出側温度と設定値との偏差によシ加熱炉燃焼制御装置に
対し均熱時間全変更し、仕上用側温[−所定の目標値と
なるよう制御すること匂特徴とする圧延機の仕上温度制
御方法。
1. In a finishing temperature control method for a rolling equipment that has a coil box between a rough rolling mill and a finishing mill, finish rolling is performed using a given finishing target temperature and the measured rough rolling mill exit temperature or finishing entry temperature. All speed calculations are set, and depending on the deviation between the measured finishing outlet temperature and the set value, the soaking time is changed in the heating furnace combustion control device, and the finishing side temperature is controlled to a predetermined target value. A method for controlling the finishing temperature of a rolling mill, which is characterized by the smell.
JP58232746A 1983-12-12 1983-12-12 Control method of finishing temperature of rolling mill Pending JPS60124411A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58232746A JPS60124411A (en) 1983-12-12 1983-12-12 Control method of finishing temperature of rolling mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58232746A JPS60124411A (en) 1983-12-12 1983-12-12 Control method of finishing temperature of rolling mill

Publications (1)

Publication Number Publication Date
JPS60124411A true JPS60124411A (en) 1985-07-03

Family

ID=16944108

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58232746A Pending JPS60124411A (en) 1983-12-12 1983-12-12 Control method of finishing temperature of rolling mill

Country Status (1)

Country Link
JP (1) JPS60124411A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62199209A (en) * 1986-02-28 1987-09-02 Nisshin Steel Co Ltd Cold rolling method for metastable austenitic stainless steel and surface temperature measuring instrument for steel strip during cold rolling
US4991418A (en) * 1988-09-20 1991-02-12 Kabushiki Kaisha Toshiba Method for determining temperature of metal to be rolled by hot strip mill and apparatus for performing the same
WO1995005904A1 (en) * 1993-08-26 1995-03-02 Davy Mckee (Poole) Limited Rolling of metal strip
KR101067758B1 (en) 2008-12-30 2011-09-28 주식회사 포스코 System and method for endless hot rolling
JP2013252531A (en) * 2012-06-06 2013-12-19 Kobe Steel Ltd Operation support system of heating furnace
CN108645233A (en) * 2018-05-15 2018-10-12 首钢集团有限公司 A method of it reduces and heats the time to be rolled
US11033942B2 (en) 2016-08-09 2021-06-15 Toshiba Mitsubishi-Electric Industrial Systems Corporation Rolling mill exit side temperature control system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62199209A (en) * 1986-02-28 1987-09-02 Nisshin Steel Co Ltd Cold rolling method for metastable austenitic stainless steel and surface temperature measuring instrument for steel strip during cold rolling
JPH0636923B2 (en) * 1986-02-28 1994-05-18 日新製鋼株式会社 Method for cold rolling metastable austenitic stainless steel and apparatus for measuring surface temperature of steel strip during cold rolling
US4991418A (en) * 1988-09-20 1991-02-12 Kabushiki Kaisha Toshiba Method for determining temperature of metal to be rolled by hot strip mill and apparatus for performing the same
WO1995005904A1 (en) * 1993-08-26 1995-03-02 Davy Mckee (Poole) Limited Rolling of metal strip
KR101067758B1 (en) 2008-12-30 2011-09-28 주식회사 포스코 System and method for endless hot rolling
JP2013252531A (en) * 2012-06-06 2013-12-19 Kobe Steel Ltd Operation support system of heating furnace
US11033942B2 (en) 2016-08-09 2021-06-15 Toshiba Mitsubishi-Electric Industrial Systems Corporation Rolling mill exit side temperature control system
CN108645233A (en) * 2018-05-15 2018-10-12 首钢集团有限公司 A method of it reduces and heats the time to be rolled

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