JPH10175009A - Thickness control method for continuous hot rolling mill - Google Patents

Thickness control method for continuous hot rolling mill

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Publication number
JPH10175009A
JPH10175009A JP8333277A JP33327796A JPH10175009A JP H10175009 A JPH10175009 A JP H10175009A JP 8333277 A JP8333277 A JP 8333277A JP 33327796 A JP33327796 A JP 33327796A JP H10175009 A JPH10175009 A JP H10175009A
Authority
JP
Japan
Prior art keywords
thickness
rolling mill
rolling
target value
control
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP8333277A
Other languages
Japanese (ja)
Other versions
JP3506408B2 (en
Inventor
Minoru Nagaka
実 長加
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP33327796A priority Critical patent/JP3506408B2/en
Publication of JPH10175009A publication Critical patent/JPH10175009A/en
Application granted granted Critical
Publication of JP3506408B2 publication Critical patent/JP3506408B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【課題】 走間変更時に圧下位置修正量又は圧延荷重が
リミットにかかっても最終圧延機出側の板厚を所望の値
にする連続熱間圧延機の板厚制御方法を提供する。 【解決手段】 常時圧延機の圧下位置修正量又は圧延荷
重を監視し、それらの値がリミットにかかったときは、
当該圧延機より1つ上流側の圧延機の板厚制御目標値を
修正することにより、最終圧延機出側の板厚を所望の値
にする。
(57) [Summary] [Problem] To control the thickness of a continuous hot rolling mill so that the thickness at the exit side of a final rolling mill can be set to a desired value even when a reduction amount of a rolling position or a rolling load is limited when a running distance is changed. I will provide a. SOLUTION: The rolling position correction amount or rolling load of a rolling mill is constantly monitored, and when those values reach a limit,
By correcting the target value of the thickness control of the rolling mill one upstream of the rolling mill, the thickness of the sheet on the exit side of the final rolling mill is set to a desired value.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は連続熱間圧延機に係
り、特に最終圧延機の出側板厚を所有の値にするための
連続熱間圧延機の板厚制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous hot rolling mill and, more particularly, to a method for controlling the thickness of a continuous hot rolling mill for setting the exit side thickness of a final rolling mill to a proprietary value.

【0002】[0002]

【従来の技術】図9は従来の連続熱間圧延機の構成図で
ある。1は圧延機で圧延材10を圧延し所望の板厚の板を
得る。従来、所望の板厚の板を得るために、各圧延機1
に、そのロール間隙を任意に設定する機構として油圧圧
下装置2が設置され、各圧延機の出側に設けられた厚み
計4からの厚み計検出板厚7を板厚制御目標値6と比較
することによって、厚み制御偏差8を演算し板厚制御装
置5は、その厚み制御偏差8をなくすように油圧圧下制
御装置3に油圧圧下位置修正量9を与えることで各圧延
機1のロール間隙を制御する。
2. Description of the Related Art FIG. 9 is a block diagram of a conventional continuous hot rolling mill. 1 is a rolling mill for rolling a rolled material 10 to obtain a plate having a desired thickness. Conventionally, in order to obtain a plate having a desired thickness, each rolling mill 1
In addition, a hydraulic pressure reduction device 2 is installed as a mechanism for arbitrarily setting the roll gap, and a thickness gauge detection plate thickness 7 from a thickness gauge 4 provided on an output side of each rolling mill is compared with a thickness control target value 6. Then, the thickness control deviation 8 is calculated, and the plate thickness control device 5 gives the hydraulic pressure reduction position correction amount 9 to the hydraulic pressure reduction control device 3 so as to eliminate the thickness control deviation 8, so that the roll gap of each rolling mill 1 is adjusted. Control.

【0003】[0003]

【発明が解決しようとする課題】ところが、各圧延機の
ロール間隙は各圧延機の出側の板厚を設定計算機(図示
せず)から与えられた目標値になるように、独立に制御
されるわけであるが、上流側の圧延機の出側板厚は下流
側の圧延機の入り側の板厚であり、この入り側の板厚と
出側の板厚の差によって板を圧延するパワー(動力)が
変わり各圧延機は他の圧延機の圧延結果の影響を受け
る。また、一般に連続熱間圧延設備に於いては、最下流
圧延機出側の板厚寸法精度が最終的な製品の保証値とな
るが、予め与えられた各圧延機のロール間隙の設定誤差
等の影響により物理的に圧延機の性能の制限にかかるこ
とがある。例えば、結果的に最終圧延機の板厚制御を継
続出来ないと言ったことになり、目標の板厚を得ること
が出来ない場合が現実問題としては起こる。
However, the roll gap of each rolling mill is independently controlled so that the thickness of the sheet on the outlet side of each rolling mill becomes a target value given from a setting calculator (not shown). However, the output side thickness of the upstream rolling mill is the thickness of the entrance side of the downstream rolling mill, and the power for rolling the sheet is determined by the difference between the thickness of the entrance side and the thickness of the exit side. (Power) changes and each rolling mill is affected by the rolling results of the other rolling mills. In general, in continuous hot rolling equipment, the thickness accuracy at the exit side of the most downstream rolling mill is a guaranteed value of the final product, but there is a predetermined error such as a roll gap setting error of each rolling mill. May physically limit the performance of the rolling mill. For example, as a result, it is said that the thickness control of the final rolling mill cannot be continued, and a case where the target thickness cannot be obtained as a practical problem occurs.

【0004】また、近年、圧延途中に於いて板厚の設定
を変更することにより、通板の難しい薄い板厚の製造を
可能ならしめる走間板厚変更という操業形態が増加して
いる。従来、上記に述べた板厚制御方法では走間板厚変
更に対する制御の継続方法あるいは目標値の切替方法が
提供されていないという問題があった。
[0004] In recent years, an operation mode of changing a running strip thickness, which enables production of a thin sheet having difficulty in threading by changing the setting of the sheet thickness during rolling, has been increasing. Conventionally, the above-described sheet thickness control method has a problem that a method of continuing control or a method of switching a target value for a change in sheet thickness during running has not been provided.

【0005】本発明は上記の事情に鑑みなされたもの
で、設定計算機の指示に基づく最終圧延機の出側目標板
厚を維持することが出来る連続熱間圧延機の板厚制御方
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 provides a method for controlling the thickness of a continuous hot rolling mill capable of maintaining a target thickness on the exit side of a final rolling mill based on instructions from a setting computer. The purpose is to:

【0006】[0006]

【課題を解決するための手段】本発明は上記の目的を達
成するために、次のような方法により連続熱間圧延機の
板厚制御方法を構成する。請求項1に対応する発明は、
出側に厚み計を有する圧延機を複数具備する連続熱間圧
延機において、常時圧延機の圧下位置修正量を監視し予
め圧延機の能力から定まるリミット値をその修正量が越
える場合には当該圧延機より1つ上流側の板厚制御目標
値を修正するとともに走間板厚変更開始点が当該圧延機
に到達時に当該圧延機の板厚制御を中止し、走間板厚変
更終了点が当該圧延機の出側厚み計に到達時に当該圧延
機の板厚制御を再開することにより設定時の誤差に拘ら
ず最終圧延機出側の板厚を所望の値にすることができ
る。
In order to achieve the above object, the present invention provides a method for controlling the thickness of a continuous hot rolling mill by the following method. The invention corresponding to claim 1 is:
In a continuous hot rolling mill equipped with a plurality of rolling mills having a thickness gauge on the delivery side, the amount of reduction of the rolling position of the rolling mill is constantly monitored, and when the correction amount exceeds a limit value previously determined from the capacity of the rolling mill, the corresponding amount is corrected. When the thickness control target value on the upstream side of the rolling mill is corrected and the running thickness change start point reaches the rolling mill, the thickness control of the rolling mill is stopped, and the running thickness change end point is changed. By restarting the control of the thickness of the rolling mill when it reaches the output thickness gauge of the rolling mill, the thickness of the output side of the final rolling mill can be set to a desired value regardless of an error at the time of setting.

【0007】請求項2に対応する発明は、請求項1にお
いて、当該圧延機に対して板厚制御を再開する場合、走
間板厚変更終了点が当該圧延機出側の厚み計に到達した
時この厚み計にて検出した板厚値から走間板厚変更後の
板厚目標値に目標値をテーパ状に変更することにより所
望の板厚を得ることができる。
According to a second aspect of the present invention, in the first aspect, when the thickness control is restarted for the rolling mill, the end point of the change in the running strip thickness has reached the thickness gauge on the rolling mill exit side. The desired thickness can be obtained by changing the target value into a tapered shape from the thickness value detected by the thickness gauge to the target thickness value after changing the running thickness.

【0008】請求項3に対応する発明は、出側に厚み計
を有する圧延機を複数具備する連続熱間圧延機におい
て、常時圧延機の圧下荷重を監視し予め圧延機の能力か
ら定まるリミット値をその荷重が越える場合には当該圧
延機より1つ上流側の圧延機の板厚制御目標値を修正す
るとともに、走間板厚変更開始点が当該圧延機に到達時
に当該圧延機の板厚制御を中止し、走間板厚変更終了点
が当該圧延機の出側厚み計に到達時に当該圧延機の板厚
制御を再開することにより設定時の誤差に拘らず最終圧
延機出側の板厚を所望の値にすることができる。
According to a third aspect of the present invention, there is provided a continuous hot rolling mill including a plurality of rolling mills each having a thickness gauge on an output side, wherein a rolling load is constantly monitored and a limit value determined in advance from the capacity of the rolling mill. When the load exceeds the rolling mill, the thickness control target value of the rolling mill one upstream of the rolling mill is corrected, and the thickness of the rolling mill is changed when the starting point of the change in the running distance reaches the rolling mill. The control is stopped, and the thickness control of the rolling mill is resumed when the end point of the change in the running thickness reaches the output thickness gauge of the rolling mill. The thickness can be set to a desired value.

【0009】請求項4に対応する発明は、請求項3にお
いて、当該圧延機に対して板厚制御を再開する場合、走
間板厚変更終了点が当該圧延機出側の厚み計に到達した
時この厚み計にて検出した板厚値から走間板厚変更後の
板厚目標値に目標値をテーパ状に変更することにより所
望の板厚を得ることができる。
According to a fourth aspect of the present invention, in the third aspect, when the thickness control is restarted for the rolling mill, the end point of the change in the running thickness has reached the thickness gauge on the rolling mill exit side. The desired thickness can be obtained by changing the target value into a tapered shape from the thickness value detected by the thickness gauge to the target thickness value after changing the running thickness.

【0010】請求項5に対応する発明は、出側に厚み計
を有する圧延機を複数具備する連続熱間圧延機におい
て、常時圧延機の油圧圧下位置修正量及び圧延荷重を監
視し予め圧延機の能力から定まるリミット値をその油圧
圧下位置修正量又は圧延荷重が越える場合には当該圧延
機より1つ上流側の圧延機の板厚制御目標値を修正する
とともに、走間板厚変更開始点が当該圧延機に到達時に
当該圧延機の板厚制御を中止し、走間板厚変更終了点が
当該圧延機の出側厚み計に到達時に当該圧延機の板厚制
御を再開することにより設定時の誤差に拘らず最終圧延
機出側の板厚を所望の値にすることができる。
According to a fifth aspect of the present invention, there is provided a continuous hot rolling mill including a plurality of rolling mills having a thickness gauge on an output side, wherein a hydraulic rolling position correction amount and a rolling load of the rolling mill are constantly monitored and the rolling load is monitored in advance. If the hydraulic pressure reduction position correction amount or the rolling load exceeds the limit value determined by the capacity of the rolling mill, the target value of the thickness control of the rolling mill one upstream of the rolling mill is corrected, and the starting point of the change in the running thickness is determined. Is set by stopping the thickness control of the rolling mill when reaching the rolling mill, and restarting the thickness control of the rolling mill when the end point of the change in the running thickness reaches the exit thickness gauge of the rolling mill. Regardless of the time error, the sheet thickness on the exit side of the final rolling mill can be set to a desired value.

【0011】請求項6に対応する発明は、請求項5にお
いて、当該圧延機に対して板厚制御を再開する場合、走
間板厚変更終了点が当該圧延機出側の厚み計に到達した
時この厚み計にて検出した板厚値から走間板厚変更後の
板厚目標値に目標値をテーパ状に変更することにより所
望の板厚を得ることができる。
According to a sixth aspect of the present invention, in the fifth aspect, when the thickness control for the rolling mill is restarted, the end point of the change in the running thickness reaches the thickness gauge on the rolling mill exit side. The desired thickness can be obtained by changing the target value into a tapered shape from the thickness value detected by the thickness gauge to the target thickness value after changing the running thickness.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施の形態を図面
を参照して説明する。図1は本発明の原理を説明するた
めの概念図である。目標値変更制御装置11は、常時、圧
延機の油圧圧下位置修正量9を監視し、予め圧延機の能
力から定めたリミット値を越えた場合には、目標値変更
制御出力装置20により一つ上流側の圧延機の板厚制御目
標値6を修正することにより当該圧延機入り側板厚を変
更し、当該圧延機の入り側板厚と出側の板厚制御目標値
とのバランスを変更し予め圧延機の能力から定めたリミ
ット値内で当該圧延機の板厚制御装置5による制御を可
能とし、所望の板厚の製品を製造することが可能とな
る。当然ながら、最下流圧延機出側の板厚を目標値に制
御することが優先されるので、本発明では、上記の目標
値変更は下流側から上流側の板厚制御装置5に対して行
われる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a conceptual diagram for explaining the principle of the present invention. The target value change control device 11 constantly monitors the hydraulic pressure reduction position correction amount 9 of the rolling mill, and when the limit value exceeds a limit value determined in advance from the capacity of the rolling mill, the target value change control output device 20 By modifying the thickness control target value 6 of the upstream rolling mill, the thickness at the entrance of the rolling mill is changed, and the balance between the thickness control target value at the entrance and the thickness at the exit side of the rolling mill is changed. The control by the thickness control device 5 of the rolling mill can be performed within a limit value determined from the capacity of the rolling mill, and a product having a desired thickness can be manufactured. Naturally, controlling the thickness of the sheet on the outlet side of the most downstream rolling mill to the target value is given priority. Therefore, in the present invention, the above-described change of the target value is performed from the downstream side to the thickness control device 5 on the upstream side. Will be

【0013】走間変更時には、圧延中に板厚をある設定
された時間でテーパー上に変更するわけであるが、板厚
制御を行う場合には制御の操作端である油圧圧下位置制
御装置3と検出端である厚み計が離れて設置されている
ので本発明では、走間変更時目標値変更制御装置11によ
って、図2に示すように板厚制御の板厚目標値を走間変
更部が当該の圧延機を通過時に切り替える。また、走間
変更部が当該圧延機に到達してから当該圧延機出側の厚
み計を通過する迄の期間、図3に示すように板厚制御を
切にする。走間変更部が当該圧延機出側の厚み計を通過
後に、板厚制御を入にする。また、厚み計は一般に厚み
の目標値によってキャリブレーションする機能(同じ偏
差でもその偏差の重みは異なるのでそれを調節する機
能)を有しているために厚み計目標値を走間変更部が当
該圧延機出側の厚み計を通過後に、板厚制御を入にする
前に走間変更後のストリップの目標板厚に切り替える。
When the running distance is changed, the plate thickness is changed to a taper at a certain set time during rolling. When the plate thickness is controlled, the hydraulic pressure lowering position control device 3 which is an operation end of the control is used. In the present invention, as shown in FIG. 2, the target thickness change value of the thickness control is changed by the travel distance change unit by the target value change control device 11 when the travel distance is changed. Switch when passing through the rolling mill. In addition, during the period from when the running distance changing section reaches the rolling mill to when it passes through the thickness gauge on the rolling mill exit side, the sheet thickness control is turned off as shown in FIG. After the running distance changing section has passed through the thickness gauge on the rolling mill exit side, the sheet thickness control is turned on. Also, since the thickness gauge generally has a function of calibrating according to the target value of the thickness (a function of adjusting the weight of the deviation even if the deviation is the same), the running distance changing unit sets the target value of the thickness gauge to the distance. After passing through the thickness gauge on the exit side of the rolling mill, before turning on the thickness control, the strip is switched to the target thickness of the strip after the change in running distance.

【0014】また、走間変更時には、圧延中に板厚をあ
る設定された時間でテーパ状に走間変更後の圧下位置目
標値に変更するわけであるが、その時の当該スタッドの
出側板厚は出側目標値には必ずしも一致しない。当該ス
タッドの出側板厚が目標値になる様な圧下位置目標値を
一般に設定計算機(図示せず)により算出して設定す
る。走間変更部が当該圧延機出側の厚み計を通過後に、
板厚制御を入にするが、その際に出側目標値と厚み計で
検出された出側板厚とに大きな偏差があると、積分制御
器にチャージされる偏差の時間積分量が大きくなり結果
的にオーバーシュート状の制御動向が発生する。これを
解決し、滑らかに走間変更後の圧下位置目標値に出側板
厚を制御するのに、本発明では走間板厚変更終了点が当
該の圧延機出側に設置された厚み計に到達時に当該の圧
延機に対するモニター板厚制御を再開する際に厚み計で
検出した板厚値から走間板厚変更後の板厚の目標値にテ
ーパ状に目標値を変更しながら制御を再開する。
At the time of changing the running distance, the thickness of the plate is changed to a target value of the reduced position after the changing of the running distance in a tapered shape at a certain set time during rolling. Does not always coincide with the delivery target value. In general, a target value of the rolling position such that the exit side plate thickness of the stud becomes the target value is calculated and set by a setting calculator (not shown). After the running distance change section has passed the thickness gauge on the rolling mill exit side,
When thickness control is turned on, if there is a large deviation between the output target value and the output plate thickness detected by the thickness gauge at that time, the amount of time integration of the deviation charged to the integral controller becomes large and the result An overshoot-like control trend occurs. In order to solve this and smoothly control the exit side sheet thickness to the target value of the rolling position after the running distance change, in the present invention, the end point of the running thickness change is set to the thickness gauge installed on the rolling mill exit side. When the monitor thickness control for the rolling mill concerned is resumed, the control is restarted while changing the tapered target value from the thickness value detected by the thickness gauge to the target value of the thickness after the change in running thickness when restarting the monitor thickness control for the rolling mill. I do.

【0015】図4は本発明の板厚制御方法を実施する構
成図である。1は圧延機で、圧延材10を圧延し所望の板
厚の板を得る。所望の板厚の板を得るために、各圧延機
1に、そのロール間隙を任意に設定する機構として油圧
圧下装置2が設置され、各圧延機の出側に設けられた厚
み計4からの厚み計検出板厚7を板厚制御目標値6と比
較することによって、厚み制御偏差8を演算し、板厚制
御装置5は、その厚み制御偏差8をなくすように油圧圧
下制御装置3に油圧圧下位置修正量9を与えることで各
圧延機1のロール間隙を制御する。目標値変更制御装置
11は、常時、圧延機の油圧圧下位置修正量9を監視し、
予め圧延機の能力から定めたリミット値を越えた場合に
は、前述した図1の目標値変更制御出力装置20により一
つ上流側の圧延機の板厚制御目標値6を修正する。
FIG. 4 is a configuration diagram for carrying out the thickness control method of the present invention. A rolling mill 1 rolls a rolled material 10 to obtain a plate having a desired thickness. In order to obtain a plate having a desired thickness, each rolling mill 1 is provided with a hydraulic pressure reduction device 2 as a mechanism for arbitrarily setting a roll gap between the rolling mills 1 and a thickness gauge 4 provided on an output side of each rolling mill. The thickness control deviation 8 is calculated by comparing the thickness gauge detection plate thickness 7 with the thickness control target value 6, and the thickness control device 5 sends the hydraulic pressure reduction control 3 to the hydraulic pressure reduction control device 3 so as to eliminate the thickness control deviation 8. The roll gap of each rolling mill 1 is controlled by giving the rolling position correction amount 9. Target value change control device
11 constantly monitors the hydraulic press down position correction amount 9 of the rolling mill,
If the limit exceeds a predetermined value based on the capacity of the rolling mill, the target value change control output device 20 shown in FIG.

【0016】走間変更時には、走間変更時目標値変更制
御装置40により、板厚目標値6を走間変更部が当該の圧
延機を通過時に切り替える。また、走間変更部が当該圧
延機に到達してから当該圧延機出側の厚み計を通過する
迄の期間、図3に示すように板厚制御装置5に対して走
間変更時制御入/切信号41によって制御を切にする。走
間変更部が当該圧延機出側の厚み計を通過後に、板厚制
御装置5に対して走間変更時制御入/切信号41によって
図3に示すように制御を入にする。また、厚み計は一般
に厚みの目標値によってキャリブレーションする機能を
有しているために厚み計目標値42を走間変更部が当該圧
延機出側の厚み計を通過後であって、板厚制御装置5に
対して走間変更時制御入/切信号41によって制御を入に
する前に走間変更後の圧延材の目標板厚に切り替える。
At the time of changing between running distances, the target value for thickness change 6 is switched by the running distance changing section when the running distance changing section passes through the rolling mill by the target value change control device 40 during running change. In addition, during a period from when the travel change section arrives at the rolling mill to pass through the thickness gauge on the exit side of the rolling mill, as shown in FIG. The control is turned off by the / off signal 41. After the running distance changing section has passed through the thickness gauge on the rolling mill exit side, the control is turned on as shown in FIG. In addition, since the thickness gauge generally has a function of calibrating with a thickness target value, the thickness gauge target value 42 is not changed after the travel distance changing unit has passed the thickness gauge on the exit side of the rolling mill. Before the control is turned on by the control change on / off signal 41 at the time of change of travel to the control device 5, the target thickness of the rolled material after the change of travel is switched.

【0017】また、走間変更部が当該圧延機出側の厚み
計を通過後に、板厚制御装置5に対して走間変更時制御
入/切信号41によって制御を入にする際に、厚み計4で
検出した板厚フィードバック値をロックオンメモリし5
0、そのロックオンメモリ50から走間板厚変更後の板厚
の目標値にテーパ状に目標値を変更しながら制御を再開
する装置51を組み合わした実施例を図5に示す。
Further, after the running distance changing unit passes the thickness gauge on the rolling mill exit side, when the control is turned on by the running time change control on / off signal 41 to the sheet thickness control device 5, the thickness is changed. Lock-on-memory the thickness feedback value detected by 4 in total and 5
FIG. 5 shows an embodiment in which a device 51 for restarting control while changing the target value in a tapered manner from the lock-on memory 50 to the target value of the sheet thickness after the change of the running sheet thickness is used is shown in FIG.

【0018】次に本発明の第2の実施の形態を図6に示
す。1は、圧延機で圧延材10を圧延し所望の板厚の板を
得る。所望の板厚の板を得るために、各圧延機1に、そ
のロール間隙を任意に設定する機構として油圧圧下装置
2が設置され、各圧延機の出側に設けられた厚み計4か
らの厚み計検出板厚7を板厚制御目標値6と比較するこ
とによって、厚み制御偏差8を演算し板厚制御装置5
は、その厚み制御偏差8をなくすように油圧圧下制御装
置3に油圧圧下位置修正量9を与えることで各圧延機1
のロール間隙を制御する。荷重検出目標値変更制御装置
12は、常時、圧延機の圧延荷重30を監視し、図7に示す
ように予め圧延機の能力から定めたリミット値を越えた
場合には、荷重検出目標値変更制御出力装置21により一
つ上流側の圧延機の板厚制御目標値6を修正する。
Next, a second embodiment of the present invention is shown in FIG. 1 is to roll the rolled material 10 by a rolling mill to obtain a plate having a desired thickness. In order to obtain a plate having a desired thickness, each rolling mill 1 is provided with a hydraulic pressure reduction device 2 as a mechanism for arbitrarily setting a roll gap between the rolling mills 1 and a thickness gauge 4 provided on an output side of each rolling mill. The thickness control deviation 8 is calculated by comparing the thickness gauge detection plate thickness 7 with the thickness control target value 6, and the thickness control device 5
Gives the hydraulic pressure reduction position correction amount 9 to the hydraulic pressure reduction control device 3 so as to eliminate the thickness control deviation 8 so that each rolling mill 1
Control of the roll gap. Load detection target value change control device
12 monitors the rolling load 30 of the rolling mill at all times, and when the load exceeds a limit value determined in advance from the capacity of the rolling mill as shown in FIG. The thickness control target value 6 of the upstream rolling mill is corrected.

【0019】走間変更時には、走間変更時目標値変更制
御装置40により、板厚目標値6を走間変更部が当該の圧
延機を通過時に切り替える。また、走間変更部が当該圧
延機に到達してから当該圧延機出側の厚み計を通過する
迄の期間、板厚制御装置5に対して走間変更時制御入/
切信号41によって制御を図8に示すように切にする。走
間変更部が当該圧延機出側の厚み計を通過後に、板厚制
御装置5に対して走間変更時制御入/切信号41によって
制御を図8に示すように入にする。また、厚み計は一般
に厚みの目標値によってキャリブレーションする機能を
有しているために厚み計目標値42を目標値変更制御装置
40によって走間変更部が当該圧延機出側の厚み計を通過
後に、板厚制御装置5に対して走間変更時制御入/切信
号41によって制御を入にする前に図8に示すように走間
変更後のストリップの目標板厚に切り替える。
At the time of changing the running distance, the target value for thickness change 6 is switched by the running distance changing section when the running distance changing section passes through the rolling mill by the target value changing control device 40 for changing the running distance. Further, during a period from when the travel change section arrives at the rolling mill to when the travel change section passes through the thickness gauge on the exit side of the rolling mill, control input / output during the travel change to the sheet thickness controller 5 is performed.
The control is turned off by the turn-off signal 41 as shown in FIG. After the running distance changing unit has passed the thickness gauge on the rolling mill exit side, the control is turned on to the sheet thickness control device 5 by the running time changing control on / off signal 41 as shown in FIG. Further, since the thickness gauge generally has a function of calibrating according to the target value of the thickness, the thickness gauge target value 42 is set to the target value change control device.
As shown in FIG. 8, after the travel change unit passes through the thickness gauge on the exit side of the rolling mill by 40 and before the control is turned on by the travel on / off change control on / off signal 41 to the sheet thickness control device 5, as shown in FIG. Then, switch to the target thickness of the strip after changing the running distance.

【0020】また、第1の実施例にて図5を使って説明
したような次のこともできる。即ち、走間変更部が当該
圧延機出側の厚み計を通過後に、板厚制御装置5に対し
て走間変更時モニター制御入/切信号41によって制御を
入にする際に、厚み計4で検出した板厚フィードバック
をロックオンメモリし50、そのロックオンメモリ50から
走間板厚変更後の板厚の目標値にテーパ状に目標値を変
更しながら制御を再開する装置51を組み合わせ実施する
ことは当然ながら可能である。
The following can also be performed as described with reference to FIG. 5 in the first embodiment. That is, after the travel change unit passes the thickness gauge on the rolling mill exit side, when the control is turned on by the monitor control on / off signal 41 at the time of travel change to the sheet thickness control device 5, the thickness gauge 4 Lock-on-memory the thickness feedback detected in step 50, and a device 51 that restarts control while changing the target value in a tapered manner from the lock-on memory 50 to the target value of the thickness after changing the running thickness It is of course possible to do so.

【0021】次に本発明の第3の実施の形態について簡
単に説明する。本形態は、第1の実施の形態と第2の実
施の形態を組合せたもので、常時圧延機の油圧圧下位置
修正量及び圧延荷重を監視し、この両値又はいずれか一
方がリミット値を越える場合前述の各々の板厚制御を行
うものである。
Next, a third embodiment of the present invention will be briefly described. This embodiment is a combination of the first embodiment and the second embodiment, and constantly monitors the hydraulic pressure reduction position correction amount and the rolling load of the rolling mill, and either or both of these values limit the limit value. If it exceeds, the above-mentioned thickness control is performed.

【0022】[0022]

【発明の効果】以上説明したように本発明によれば、設
定時の誤差に拘らず常時圧延機の圧下位置修正量又は圧
延荷重を監視し、その値がリミット値を越える場合当該
圧延機の1つ上流の圧延機の各々目標値を変更するよう
にしたので、最終圧延機出側の板厚を所望の値にするこ
とができる。
As described above, according to the present invention, the rolling position correction amount or the rolling load of the rolling mill is constantly monitored regardless of the error at the time of setting, and when the value exceeds the limit value, the rolling mill is controlled. Since the target value of each of the upstream rolling mills is changed, the sheet thickness on the exit side of the final rolling mill can be set to a desired value.

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

【図1】本発明の原理を説明するための概念図。FIG. 1 is a conceptual diagram for explaining the principle of the present invention.

【図2】油圧圧下位置修正量がリミットにかかった場合
とその場合の処理を示すタイミングチャート。
FIG. 2 is a timing chart showing a case where a hydraulic pressure reduction position correction amount reaches a limit and processing in that case.

【図3】油圧圧下位置修正量がリミットにかかった場合
とその場合の処理を示すタイミングチャート。
FIG. 3 is a timing chart showing a case where the hydraulic pressure reduction position correction amount reaches a limit and processing in that case.

【図4】本発明の板厚制御方法を実施するための構成
図。
FIG. 4 is a configuration diagram for implementing a sheet thickness control method of the present invention.

【図5】ロックオンメモリ方法を実施するための構成
図。
FIG. 5 is a configuration diagram for implementing a lock-on-memory method.

【図6】本発明の他の実施の形態を示す構成図。FIG. 6 is a configuration diagram showing another embodiment of the present invention.

【図7】圧延荷重がリミットにかかった場合とその場合
の処理を示すタイミングチャート。
FIG. 7 is a timing chart showing a case where a rolling load is applied to a limit and processing in that case.

【図8】圧延荷重がリミットにかかった場合とその場合
の処理を示すタイミングチャート。
FIG. 8 is a timing chart showing a case where a rolling load is applied to a limit and a process in that case.

【図9】従来例を示す構成図。FIG. 9 is a configuration diagram showing a conventional example.

【符号の説明】[Explanation of symbols]

1…圧延機 2…油圧圧下装置 3…油圧圧下位置制御装置 4…厚み計 5…板厚制御装置 11…目標値変更制御装置 12…荷重検出目標値変更制御装置 40…走間変更時目標値変更制御装置 DESCRIPTION OF SYMBOLS 1 ... Rolling machine 2 ... Hydraulic reduction device 3 ... Hydraulic reduction position control device 4 ... Thickness gauge 5 ... Thickness control device 11 ... Target value change control device 12 ... Load detection target value change control device 40 ... Target value at the time of change during running Change control device

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 出側に厚み計を有する圧延機を複数具備
する連続熱間圧延機において、設定時の誤差に拘らず最
終圧延機出側の板厚を所望の値にするために常時圧延機
の圧下位置修正量を監視し予め圧延機の能力から定まる
リミット値をその修正量が越える場合には当該圧延機よ
り1つ上流側の圧延機の板厚制御目標値を修正するとと
もに、走間板厚変更開始点が当該圧延機に到達時に当該
圧延機の板厚制御を中止し、走間板厚変更終了点が当該
圧延機の出側厚み計に到達時に当該圧延機の板厚制御を
開始することを特徴とする連続熱間圧延機の板厚制御方
法。
In a continuous hot rolling mill having a plurality of rolling mills having a thickness gauge on an output side, a continuous rolling mill is used to keep the thickness of the output side of a final rolling mill to a desired value regardless of an error at the time of setting. The correction amount of the rolling position of the rolling mill is monitored, and when the correction amount exceeds a limit value determined in advance from the capacity of the rolling mill, the target value of the thickness control of the rolling mill one upstream from the rolling mill is corrected, and the running is performed. When the start point of the change in the thickness of the rolling mill reaches the rolling mill, the control of the thickness of the rolling mill is stopped. A method for controlling the thickness of a continuous hot rolling mill.
【請求項2】 当該圧延機に対して板厚制御を再開する
場合、前記走間板厚変更終了点が当該圧延機出側の厚み
計に到達した時この厚み計にて検出した板厚値から走間
板厚変更後の板厚目標値に目標値をテーパ状に変更する
ことを特徴とする請求項1記載の連続熱間圧延機の板厚
制御方法。
2. When the thickness control for the rolling mill is restarted, the thickness value detected by the thickness gauge when the end point of change in the running thickness reaches the thickness gauge on the exit side of the rolling mill. 2. The method for controlling a thickness of a continuous hot rolling mill according to claim 1, wherein the target value is changed into a tapered shape from the target value to the target value after the change in the running thickness.
【請求項3】 出側に厚み計を有する圧延機を複数具備
する連続熱間圧延機において、設定時の誤差に拘らず最
終圧延機出側の板厚を所望の値にするために、常時圧延
機の圧下荷重量を監視し予め圧延機の能力から定まるリ
ミット値をその荷重量が越える場合には当該圧延機より
1つ上流側の圧延機の板厚制御目標値を修正するととも
に、走間板厚変更開始点が当該圧延機に到達時に当該圧
延機の板厚制御を中止し、走間板厚変更終了点が当該圧
延機の出側厚み計に到達時に当該圧延機の板厚制御を再
開することを特徴とする連続熱間圧延機の板厚制御方
法。
3. In a continuous hot rolling mill having a plurality of rolling mills having a thickness gauge on the delivery side, in order to make the thickness of the delivery side of the final rolling mill a desired value regardless of an error at the time of setting. The rolling load of the rolling mill is monitored, and when the load exceeds a limit value determined in advance from the capacity of the rolling mill, the target value of the thickness control of the rolling mill one upstream of the rolling mill is corrected, and the running is performed. When the start point of the change in the thickness of the rolling mill reaches the rolling mill, the control of the thickness of the rolling mill is stopped. And a method for controlling the thickness of a continuous hot rolling mill.
【請求項4】 当該圧延機に対して板厚制御を再開する
場合、前記走間板厚変更終了点が当該圧延機出側の厚み
計に到達した時この厚み計にて検出した板厚値から走間
板厚変更後の板厚目標値に目標値をテーパ状に変更する
ことを特徴とする請求項3記載の連続熱間圧延機の板厚
制御方法。
4. When the thickness control is restarted for the rolling mill, the thickness value detected by the thickness gauge when the running thickness change end point reaches the thickness gauge on the exit side of the rolling mill. 4. The method for controlling a thickness of a continuous hot rolling mill according to claim 3, wherein the target value is changed in a tapered shape from the target value to the target value after the change in the running thickness.
【請求項5】 出側に厚み計を有する圧延機を複数具備
する連続熱間圧延機において、設定時の誤差に拘らず最
終圧延機出側の板厚を所望の値にするために、常時圧延
機の油圧圧下位置修正量及び圧延荷重を監視し予め圧延
機の能力から定まるリミット値をその油圧圧下位置修正
量又は圧延荷重が越える場合には当該圧延機より1つ上
流側の圧延機の板厚制御目標値を修正するとともに、走
間板厚変更開始点が当該圧延機に到達時に当該圧延機の
板厚制御を中止し、走間板厚変更終了点が当該圧延機の
出側厚み計に到達時に当該圧延機の板厚制御を再開する
ことを特徴とする連続熱間圧延機の板厚制御方法。
5. In a continuous hot rolling mill having a plurality of rolling mills having a thickness gauge on the delivery side, in order to keep the thickness of the delivery side on the final rolling mill to a desired value regardless of an error at the time of setting. When the hydraulic rolling position correction amount and the rolling load exceed the limit value determined in advance from the capacity of the rolling mill and the hydraulic rolling position correction amount and the rolling load exceed the limit value determined in advance by the rolling mill, the rolling mill of one upstream side from the rolling mill concerned. In addition to correcting the target value of the thickness control, the thickness control of the rolling mill is stopped when the start point of the running thickness change reaches the rolling mill, and the end point of the running thickness change is set to the exit side thickness of the rolling mill. A sheet thickness control method for a continuous hot rolling mill, wherein the sheet thickness control of the rolling mill is restarted when the total number reaches a total value.
【請求項6】 当該圧延機に対して板厚制御を再開する
場合、前記走間板厚変更終了点が当該圧延機出側の厚み
計に到達した時この厚み計にて検出した板厚値から走間
板厚変更後の板厚目標値に目標値をテーパ状に変更する
ことを特徴とする請求項5記載の連続熱間圧延機の板厚
制御方法。
6. When the thickness control for the rolling mill is restarted, when the end point of the change in the running thickness reaches the thickness gauge on the exit side of the rolling mill, the thickness value detected by the thickness gauge. 6. The method for controlling the thickness of a continuous hot rolling mill according to claim 5, wherein the target value is changed in a tapered shape from the target value to the target value after the change in the running thickness.
JP33327796A 1996-12-13 1996-12-13 Thickness control method of continuous hot rolling mill Expired - Fee Related JP3506408B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33327796A JP3506408B2 (en) 1996-12-13 1996-12-13 Thickness control method of continuous hot rolling mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33327796A JP3506408B2 (en) 1996-12-13 1996-12-13 Thickness control method of continuous hot rolling mill

Publications (2)

Publication Number Publication Date
JPH10175009A true JPH10175009A (en) 1998-06-30
JP3506408B2 JP3506408B2 (en) 2004-03-15

Family

ID=18264302

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3506408B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106862276A (en) * 2017-02-07 2017-06-20 山西太钢不锈钢股份有限公司 Hot tandem rolling special steel main transmission overload control method
WO2024241433A1 (en) * 2023-05-22 2024-11-28 株式会社Tmeic Overload avoidance support system for rolling facility

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106862276A (en) * 2017-02-07 2017-06-20 山西太钢不锈钢股份有限公司 Hot tandem rolling special steel main transmission overload control method
WO2024241433A1 (en) * 2023-05-22 2024-11-28 株式会社Tmeic Overload avoidance support system for rolling facility
JPWO2024241433A1 (en) * 2023-05-22 2024-11-28

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