JPH04168232A - Plate temperature control method - Google Patents
Plate temperature control methodInfo
- Publication number
- JPH04168232A JPH04168232A JP29676990A JP29676990A JPH04168232A JP H04168232 A JPH04168232 A JP H04168232A JP 29676990 A JP29676990 A JP 29676990A JP 29676990 A JP29676990 A JP 29676990A JP H04168232 A JPH04168232 A JP H04168232A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- plate temperature
- heating
- strip
- heating zone
- 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
Links
- 238000000034 method Methods 0.000 title claims description 23
- 238000010438 heat treatment Methods 0.000 claims description 69
- 238000000137 annealing Methods 0.000 claims description 7
- 238000007796 conventional method Methods 0.000 description 4
- 238000003466 welding Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 101150070659 tfpI gene Proteins 0.000 description 1
Landscapes
- Control Of Heat Treatment Processes (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は連続焼鈍炉の加熱炉出口におけるストリップの
板温を制御する方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for controlling the temperature of a strip at the furnace outlet of a continuous annealing furnace.
連続焼鈍炉の加熱炉では、板厚、板幅等のストリップ仕
様及び加熱炉出口における目標板温が異なる種々のスト
リップが溶接により連続させられて通板される。加熱炉
は複数の加熱帯を有し、これらの加熱帯は個別に温度制
御されるように構成されている。このように構成された
加熱炉では、夫々のストリップ仕様及び加熱炉出口の目
標板温の情報に基づいて、各加熱帯の温度を設定するこ
とにより、夫々のストリップの出口板温を制御している
。In a heating furnace of a continuous annealing furnace, various strips having different strip specifications such as plate thickness and width, and target plate temperatures at the outlet of the heating furnace are successively threaded by welding. The heating furnace has a plurality of heating zones, and these heating zones are configured to be individually temperature controlled. In a heating furnace configured in this way, the outlet plate temperature of each strip is controlled by setting the temperature of each heating zone based on the information of each strip specification and the target plate temperature at the outlet of the heating furnace. There is.
ところが上述のプリセット制御のみでは、実測した出口
板温が目標板温と一致しないので、これらの板温偏差に
基づいて各加熱帯の設定温度を変更するフィードバック
制御を行っていた。However, with only the preset control described above, the actually measured outlet plate temperature does not match the target plate temperature, so feedback control is performed to change the set temperature of each heating zone based on these plate temperature deviations.
第4図は従来の板温制御の過程を示すフローチャートで
ある。まずストリップ仕様及び加熱炉出口における目標
板温の情報を取り込む(ステップSL)。次にこの情報
に基づき各加熱帯の温度を設定する(ステップS2)。FIG. 4 is a flowchart showing the process of conventional plate temperature control. First, information on the strip specifications and the target plate temperature at the outlet of the heating furnace is taken in (step SL). Next, the temperature of each heating zone is set based on this information (step S2).
そして加熱炉の出口の板温を実測してその情報を取り込
む(ステップS3)。Then, the plate temperature at the outlet of the heating furnace is actually measured and the information is taken in (step S3).
実測板温の目標板温に対する偏差を計算する(ステップ
S4)。ステップS4で求めた偏差に基づき各加熱帯の
温度設定値変更量を演算する(ステップS5)。そして
各加熱帯の設定温度を変更する(ステップS6)。The deviation of the measured plate temperature from the target plate temperature is calculated (step S4). Based on the deviation obtained in step S4, the amount of change in the temperature setting value for each heating zone is calculated (step S5). Then, the set temperature of each heating zone is changed (step S6).
ところが加熱炉の設定温度変更に対する応答性は遅く、
特に仕様が異なるストリップの溶接点近傍(非定常域)
では、上述の制御方法を実施すると実測した板温の目標
板温に対する偏差がかえって太き(なるため、上述の制
御方法は非定常域を除く定常域のみで実施し、非定常域
については予め炉温を設定するプリセット制御のみを実
施していた。However, the response to changes in the heating furnace's set temperature is slow;
Especially near the welding point of strips with different specifications (unsteady region)
Therefore, if the above control method is implemented, the deviation of the actually measured plate temperature from the target plate temperature will become wider. Therefore, the above control method should be implemented only in the steady region excluding the unsteady region, and Only preset control was used to set the furnace temperature.
従って、ストリップの全長に亘って板温外れを減少させ
るため、非定常域も含めたストリップの全長に亘る板温
制御方法の開発が望まれていた。Therefore, in order to reduce the deviation in plate temperature over the entire length of the strip, it has been desired to develop a method for controlling the plate temperature over the entire length of the strip, including the unsteady region.
本発明は斯かる事情に鑑みてなされたものであり、スト
リップの長さ方向に定めた複数のサンプル点が加熱炉の
各加熱帯を通過するときに測定した各加熱帯の温度及び
サンプル点の各加熱帯滞在時間より加熱炉出口における
サンプル点の板温を計算し、実測したサンプル点の出口
板温の計算板温に対する偏差をもとめて温度設定値変更
量を計算し、各加熱帯の設定温度を変更することにより
、ストリップの全長に亘って板温外れを減少させ、成品
の歩留及び品質を向上させる板温制御方法を提供するこ
とを目的とする。The present invention has been made in view of the above circumstances, and the present invention is based on the temperature of each heating zone and the sample points measured when a plurality of sample points defined in the longitudinal direction of the strip pass through each heating zone of the heating furnace. The plate temperature of the sample point at the outlet of the heating furnace is calculated from the residence time of each heating zone, and the deviation of the actually measured outlet plate temperature of the sample point from the calculated plate temperature is calculated to calculate the amount of change in the temperature set value, and the temperature setting value is set for each heating zone. It is an object of the present invention to provide a sheet temperature control method that reduces sheet temperature deviation over the entire length of the strip and improves the yield and quality of finished products by changing the temperature.
本発明に係る板温制御方法は、ストリップを連続焼鈍す
る連続焼鈍炉の加熱炉内で個別に温度制御される複数の
加熱帯の温度設定値を変更して、加熱炉出口におけるス
トリップの板温を制御する板温制御方法において、スト
リップの長さ方向に定めた複数のサンプル点が前記各加
熱帯を通過したときに測定した各加熱帯の温度及び前記
サンプル点の各加熱帯滞在時間より加熱炉出口における
サンプル点の板温を計算する一方、前記サンプル点の出
口板温を測定し、実測板温の計算板温に対する偏差を求
め、該偏差より各加熱帯の温度設定値変更量を計算し、
各加熱帯の設定温度を変更することを特徴とする。The strip temperature control method according to the present invention changes the temperature setting values of a plurality of heating zones that are individually temperature-controlled in the heating furnace of a continuous annealing furnace that continuously anneales the strip, thereby increasing the temperature of the strip at the outlet of the heating furnace. In a plate temperature control method for controlling the temperature of a strip, heating is determined from the temperature of each heating zone measured when a plurality of sample points defined in the length direction of the strip pass through each heating zone and the time the sample points stay in each heating zone. While calculating the plate temperature at the sample point at the furnace outlet, measure the outlet plate temperature at the sample point, find the deviation of the actual plate temperature from the calculated plate temperature, and calculate the amount of change in the temperature setting value of each heating zone from the deviation. death,
It is characterized by changing the set temperature of each heating zone.
本発明においては、ストリップの長さ方向に定めたサン
プル点が連続焼鈍炉の加熱炉の各加熱帯を通過するとき
に測定した各加熱帯の温度及びサンプル点の各加熱帯滞
在時間を用いて各加熱帯の温度設定値変更量を算出する
ので、実際のス) IJツブの加熱条件を考慮した適正
な設定温度の補正を行うことができ、設定温度の変更に
対する応答が速くなる。In the present invention, the temperature of each heating zone measured when a sample point defined in the length direction of the strip passes through each heating zone of the heating furnace of a continuous annealing furnace and the residence time of each heating zone of the sample point are used. Since the amount of change in the temperature setting value for each heating zone is calculated, it is possible to appropriately correct the setting temperature in consideration of the actual heating conditions of the IJ tube, and the response to changes in the setting temperature becomes faster.
以下、本発明をその実施例を示す図面に基づき具体的に
説明する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below based on drawings showing embodiments thereof.
第1図は本発明方法の実施状態を示す模式図であり、図
中1は連続焼鈍炉の加熱炉である。加熱炉1には上下に
複数のハースロールが配置されており、ストリップSは
これらのハースロール間に架は渡されて矢符に示したよ
うに上下方向に折り返し走行され、加熱帯1a、lb及
び1c内を順次通板されるようになっている。FIG. 1 is a schematic diagram showing the implementation state of the method of the present invention, and in the figure, 1 is a heating furnace of a continuous annealing furnace. A plurality of hearth rolls are arranged above and below in the heating furnace 1, and a rack is passed between these hearth rolls, and the strip S is run back and forth in the vertical direction as shown by the arrow, and is heated to heating zones 1a, 1b. and 1c are sequentially threaded.
加熱帯1a、 lb及び1cは演算制御装置4から出力
された信号により個別に温度を制御される。また、加熱
帯1a、 lb及び1cには温度計2a、2b及び2c
が設けられており、ストリップSの長さ方向に定間隔又
は不均一の間隔をおいて定められたサンプル点A、B、
・・・が加熱帯1a、lb及びlc内の所定位置を通過
したときの加熱帯1a、lb及び1cの温度が温度計2
a、2b及び2cにより測定され、その情報を演算制御
装置4が取り込むようになっている。加熱炉1の出口に
は板温計3が設けられており、板温計3は前記サンプル
点A、B、・・・が板温計3の測定領域を通過したとき
の板温を測定し、その情報を演算制御装置4が取り込む
ようになっている。なお、演算制御装置4は、2つのコ
イル材が溶接により一体化された時点を起点とした位置
と、加熱帯1a内に設けられたロール回転数検出器5が
検出したストリップSの搬送距離とによりサンプル点A
、B、・・・のトラッキングを行っており、サンプル点
A、B、・・・が上述の温度測定領域を通過したことを
判断して温度情報の取り込みを行う。The temperatures of the heating zones 1a, lb and 1c are individually controlled by signals output from the arithmetic and control unit 4. In addition, thermometers 2a, 2b and 2c are installed in heating zones 1a, lb and 1c.
are provided, and sample points A, B, defined at regular or non-uniform intervals in the length direction of the strip S are provided.
The temperature of the heating zones 1a, lb, and 1c when ... passes through a predetermined position in the heating zones 1a, lb, and lc is measured by the thermometer 2.
a, 2b, and 2c, and the arithmetic and control unit 4 takes in the information. A plate thermometer 3 is provided at the outlet of the heating furnace 1, and the plate thermometer 3 measures the plate temperature when the sample points A, B, ... pass through the measurement area of the plate thermometer 3. , the information is taken in by the arithmetic and control unit 4. Note that the arithmetic and control device 4 determines the position starting from the time when the two coil materials were integrated by welding, and the transport distance of the strip S detected by the roll rotation speed detector 5 provided in the heating zone 1a. sample point A
, B, . . . , and when it is determined that the sample points A, B, .
第2図は本発明の板温制御の過程を示すフローチャート
である。まず、演算制御装置4においてストリップSの
仕様及び加熱炉出口における目標板温T、。の情報を取
り込む(ステップSl)。次に加熱帯1a、lb及び1
cの設定温度TFPiを下記(11式より求める(ステ
ップS2)。FIG. 2 is a flowchart showing the process of plate temperature control according to the present invention. First, the arithmetic and control unit 4 determines the specifications of the strip S and the target plate temperature T at the outlet of the heating furnace. (Step Sl). Next, heating zones 1a, lb and 1
The set temperature TFPi of c is determined from the following equation (11) (step S2).
Tvp= = f Ci (Tso) −(1
1但し、fci:各加熱帯により定まる関数次に、スト
リップSの長さ方向に定めたサンプル点A、B、・・・
が加熱帯1a、Ib及び1cを通過したときに測定した
加熱帯1a、lb及び1cの温度を取り込み、一方サン
プル点A、B、・・・の加熱帯1a、lb及び1cにお
ける滞在時間を算出する(ステ・7プS3)。Tvp= = f Ci (Tso) −(1
1 However, fci: a function determined by each heating zone Next, sample points A, B, . . . determined in the length direction of the strip S
The temperatures of the heating zones 1a, lb and 1c measured when passing through the heating zones 1a, Ib and 1c are taken in, and the residence time of the sample points A, B, ... in the heating zones 1a, lb and 1c is calculated. (Step 7 S3).
そして、加熱炉出口の板温T’scをサンプル点A。Then, the plate temperature T'sc at the outlet of the heating furnace is sampled at point A.
B、・・・夫々について下記(2)式、(3)式より求
める(ステップS4)。B, . . . are determined from the following equations (2) and (3) (step S4).
但し、G:フィードバックゲイン
Ts
そして最後に加熱帯1a、 lb及び1cの温度設定値
変更量TFFに基づき加熱帯1a、lb及びICの設定
温度を変更する(ステップS8)。However, G: Feedback gain Ts And finally, the set temperatures of the heating zones 1a, lb and IC are changed based on the temperature set value change amount TFF of the heating zones 1a, lb and 1c (step S8).
第3図はコイルα、β及びTを溶接により一体化し、従
来方法及び本発明方法によりその温度を制御した場合の
目標板温及び実測板温を示すグラフである。第3図(a
)定常部FB (フィードハック)制御、山)全長FB
!II?Il及び(e)板温偏差は従来方法により板温
を制御した場合のグラフ、第3図fd)は本発明方法に
より算出した計算板温を示すグラフ、第3図(e)全長
FB制御及び(f)板温偏差は本発明方法により板温を
制御した場合のグラフを示す。なお図中、比較例は予め
炉温を設定するプリセット制御のみを実施した場合の実
測板温を示す。FIG. 3 is a graph showing the target plate temperature and the measured plate temperature when the coils α, β, and T are integrated by welding and the temperature is controlled by the conventional method and the method of the present invention. Figure 3 (a
) Steady part FB (feed hack) control, mountain) Full length FB
! II? Il and (e) Plate temperature deviation is a graph when the plate temperature is controlled by the conventional method, Fig. 3 (fd) is a graph showing the calculated plate temperature calculated by the method of the present invention, Fig. 3 (e) Full length FB control and (f) Plate temperature deviation shows a graph when the plate temperature is controlled by the method of the present invention. In addition, in the figure, the comparative example shows the actually measured plate temperature when only the preset control for setting the furnace temperature in advance is performed.
第3図(a)は溶接部近傍を除く定常域のみ、従来のフ
ィードバック制御を行った場合の板温を示したグラフで
ある。この場合、定常域のみ制御を行っているので、実
測板温が目標板温と一致する範囲は短い。FIG. 3(a) is a graph showing the plate temperature when conventional feedback control is performed only in the steady region excluding the vicinity of the weld. In this case, since control is performed only in the steady range, the range in which the actual plate temperature matches the target plate temperature is short.
第3図(b)はストリップの全長に亘って従来のフィー
ドバック制御を行った場合の板温を示したグラフであり
、第3図(C)はこの場合の実測板温の目標板温に対す
る偏差を示したグラフである。このとき、溶接部近傍(
非定常域)における実測板温の目標板温に対する偏差が
大きく、これが起因して炉温の設定温度変更に対する応
答がさらに遅れて実測板温の目標板温に対するハンチン
グ現象が生じている。Figure 3 (b) is a graph showing the plate temperature when conventional feedback control is performed over the entire length of the strip, and Figure 3 (C) is a graph showing the deviation of the measured plate temperature from the target plate temperature in this case. This is a graph showing At this time, the vicinity of the weld (
The deviation of the measured plate temperature from the target plate temperature in the unsteady region is large, and this causes a further delay in response to changes in the furnace temperature setting, resulting in a hunting phenomenon in which the measured plate temperature is relative to the target plate temperature.
第3図(dlは本発明方法により計算した板温を示した
グラフである。第3図(e)はストリップの全長に亘っ
て本発明のフィードバック制御を行った場合の板温を示
したグラフであり、第3図(C)はこの場合の実測板温
の計算板温に対する偏差を示したグラフである。第3図
(elにより本発明方法の適用により板温外れが減少し
、ストリップの略全長に亘って板温の制御ができること
が解る。Fig. 3 (dl is a graph showing the plate temperature calculated by the method of the present invention. Fig. 3 (e) is a graph showing the plate temperature when the feedback control of the present invention is performed over the entire length of the strip. Figure 3 (C) is a graph showing the deviation of the measured plate temperature from the calculated plate temperature in this case. Figure 3 (el) shows that application of the method of the present invention reduces plate temperature deviations and increases the It can be seen that the plate temperature can be controlled over almost the entire length.
以上の如く本発明においては、ストリップの長さ方向に
定めた複数のサンプル点が加熱炉の各加熱帯を通過する
時に測定した各加熱帯の温度及びサンプル点の各加熱帯
滞在時間より加熱炉出口におけるサンプル点の板温を計
算し、実測したサンプル点の出口板温の計算板温に対す
る偏差を求めて各加熱帯の温度設定値変更量を計算し、
各加熱帯の設定温度を変更するので、実際の炉況を考慮
した適正な設定温度補正を行うことができる。As described above, in the present invention, the temperature of each heating zone measured when a plurality of sample points defined in the length direction of the strip pass through each heating zone of the heating furnace and the residence time of each heating zone of the sample points are determined. Calculate the plate temperature at the sample point at the outlet, find the deviation of the actually measured outlet plate temperature at the sample point from the calculated plate temperature, and calculate the amount of change in the temperature setting value for each heating zone.
Since the set temperature of each heating zone is changed, it is possible to appropriately correct the set temperature in consideration of the actual furnace condition.
その結果、ストリップの全長に亘って板温外れが減少し
、製品の歩留及び品質が向上する等、本発明は優れた効
果を奏するものである。As a result, the present invention exhibits excellent effects, such as reducing plate temperature deviation over the entire length of the strip and improving product yield and quality.
第1図は本発明方法の実施状態を示す模式図、第2図は
本発明の板温制御の過程を示すフローチャート、第3図
は従来方法及び本発明方法により板温を制御した場合の
目標板温及び実測板温を示すグラフ、第4図は従来の板
温制御の過程を示すフローチャートである。
1・・・連続焼鈍炉 2a、2b、2c・・・温度計
3・・・板温計 4・・・演算制御装置 S・
・・ストリップ特 許 出願人 住友金属工業株式会
社代理人 弁理士 河 野 登 夫S
第 1 図
第 2 図
〈従来方法〉
(a)
(b)
(c)
第
く本発明方法〉
(d)
(e)
3図
第 4 図Fig. 1 is a schematic diagram showing the implementation state of the method of the present invention, Fig. 2 is a flowchart showing the process of plate temperature control of the present invention, and Fig. 3 is the target when plate temperature is controlled by the conventional method and the method of the present invention. A graph showing the plate temperature and the measured plate temperature, and FIG. 4 is a flowchart showing the process of conventional plate temperature control. 1... Continuous annealing furnace 2a, 2b, 2c... Thermometer 3... Plate thermometer 4... Arithmetic control device S.
...Strip patent Applicant Sumitomo Metal Industries Co., Ltd. Agent Patent attorney Noboru Kono S Figure 1 Figure 2 <Conventional method> (a) (b) (c) Method of the present invention> (d) ( e) Figure 3 Figure 4
Claims (1)
個別に温度制御される複数の加熱帯の温度設定値を変更
して、加熱炉出口におけるストリップの板温を制御する
板温制御方法において、 ストリップの長さ方向に定めた複数のサンプル点が前記
各加熱帯を通過したときに測定した各加熱帯の温度及び
前記サンプル点の各加熱帯滞在時間より加熱炉出口にお
けるサンプル点の板温を計算する一方、前記サンプル点
の出口板温を測定し、実測板温の計算板温に対する偏差
を求め、該偏差より各加熱帯の温度設定値変更量を計算
し、各加熱帯の設定温度を変更することを特徴とする板
温制御方法。[Claims] 1. Control the plate temperature of the strip at the outlet of the heating furnace by changing the temperature setting values of a plurality of heating zones whose temperatures are individually controlled in the heating furnace of a continuous annealing furnace that continuously anneales the strip. In the plate temperature control method, the heating furnace outlet temperature is determined based on the temperature of each heating zone measured when a plurality of sample points defined in the length direction of the strip pass through each heating zone and the residence time of each heating zone of the sample points. While calculating the plate temperature of the sample point at the sample point, measure the outlet plate temperature of the sample point, find the deviation of the actual plate temperature from the calculated plate temperature, and calculate the amount of change in the temperature setting value of each heating zone from the deviation, A plate temperature control method characterized by changing the set temperature of each heating zone.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29676990A JPH04168232A (en) | 1990-10-31 | 1990-10-31 | Plate temperature control method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29676990A JPH04168232A (en) | 1990-10-31 | 1990-10-31 | Plate temperature control method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04168232A true JPH04168232A (en) | 1992-06-16 |
Family
ID=17837891
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29676990A Pending JPH04168232A (en) | 1990-10-31 | 1990-10-31 | Plate temperature control method |
Country Status (1)
Country | Link |
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JP (1) | JPH04168232A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013100578A (en) * | 2011-11-08 | 2013-05-23 | Jfe Steel Corp | Method and device for controlling continuous annealing line |
CN104451118A (en) * | 2014-10-27 | 2015-03-25 | 燕山大学 | Forecasting method for segmental evolution of strip steel shape in continuous annealing process |
JP6146553B1 (en) * | 2016-01-28 | 2017-06-14 | Jfeスチール株式会社 | Steel plate temperature control device and temperature control method |
WO2017130508A1 (en) * | 2016-01-28 | 2017-08-03 | Jfeスチール株式会社 | Steel sheet temperature control device and temperature control method |
-
1990
- 1990-10-31 JP JP29676990A patent/JPH04168232A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013100578A (en) * | 2011-11-08 | 2013-05-23 | Jfe Steel Corp | Method and device for controlling continuous annealing line |
CN104451118A (en) * | 2014-10-27 | 2015-03-25 | 燕山大学 | Forecasting method for segmental evolution of strip steel shape in continuous annealing process |
JP6146553B1 (en) * | 2016-01-28 | 2017-06-14 | Jfeスチール株式会社 | Steel plate temperature control device and temperature control method |
WO2017130508A1 (en) * | 2016-01-28 | 2017-08-03 | Jfeスチール株式会社 | Steel sheet temperature control device and temperature control method |
US11466340B2 (en) | 2016-01-28 | 2022-10-11 | Jfe Steel Corporation | Steel sheet temperature control device and temperature control method |
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