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JP6939713B2 - Steel plate temperature control device for hot endless rolling line - Google Patents
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JP6939713B2 - Steel plate temperature control device for hot endless rolling line - Google Patents

Steel plate temperature control device for hot endless rolling line Download PDF

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JP6939713B2
JP6939713B2 JP2018109939A JP2018109939A JP6939713B2 JP 6939713 B2 JP6939713 B2 JP 6939713B2 JP 2018109939 A JP2018109939 A JP 2018109939A JP 2018109939 A JP2018109939 A JP 2018109939A JP 6939713 B2 JP6939713 B2 JP 6939713B2
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induction heating
heating device
plate thickness
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tapered portion
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JP2019209372A (en
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俊人 下谷
俊人 下谷
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Toshiba Mitsubishi Electric Industrial Systems Corp
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    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B45/00Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
    • B21B45/02Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for lubricating, cooling, or cleaning
    • B21B45/0203Cooling
    • B21B45/0209Cooling devices, e.g. using gaseous coolants
    • B21B45/0215Cooling devices, e.g. using gaseous coolants using liquid coolants, e.g. for sections, for tubes
    • B21B45/0218Cooling devices, e.g. using gaseous coolants using liquid coolants, e.g. for sections, for tubes for strips, sheets, or plates

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Control Of Metal Rolling (AREA)
  • General Induction Heating (AREA)
  • Metal Rolling (AREA)

Description

本発明は、粗圧延機、誘導加熱装置、仕上げ圧延機の順に鋼板が流れる熱間エンドレス圧延ラインの鋼板温度制御装置に関し、詳しくは、仕上げ圧延機に入る鋼板の温度を誘導加熱装置の出力によって制御する鋼板温度制御装置に関する。 The present invention relates to a steel plate temperature control device for a hot endless rolling line in which steel sheets flow in the order of a rough rolling mill, an induction heating device, and a finish rolling mill. The present invention relates to a steel plate temperature control device to be controlled.

熱間圧延プロセスでは、スラブ加熱炉で所要の温度まで加熱された高温の鋼板スラブが、ライン上を搬送されて、順次圧延され、最後にコイラで巻き取られる。近年の製品仕様への要求の高度化および多様化から、仕上げ入側温度、仕上げ出側温度、巻取温度などに代表される圧延ライン上の各ポイントにおける目標温度の保証範囲は従来よりも更に厳しくなっている。 In the hot rolling process, high-temperature steel sheet slabs heated to a required temperature in a slab heating furnace are conveyed on a line, rolled in sequence, and finally wound up by a coiler. Due to the sophistication and diversification of product specifications in recent years, the guaranteed range of target temperature at each point on the rolling line represented by finish inlet temperature, finish exit temperature, take-up temperature, etc. is even greater than before. It's getting tougher.

熱間圧延プロセスにおける鋼板の温度制御のため、誘導加熱装置が導入されている。誘導加熱装置による加熱は、鋼板に鎖交する磁束を打ち消すように流れる渦電流に起因するジュール損失を利用している。誘導加熱装置は、直接加熱のためエネルギー効率がよく、また、急速加熱のため生産量の向上が期待できる。誘導加熱装置による鋼板の発熱量は、鋼板の板厚、板幅、速度により変化する。このため、誘導加熱装置による鋼板の温度制御においては、目標とする鋼板温度もしくは加熱昇温量を達成するため、鋼板の板厚、板幅、速度に応じて誘導加熱装置の出力が設定されている。 An induction heating device has been introduced to control the temperature of the steel sheet in the hot rolling process. The heating by the induction heating device utilizes the Joule loss caused by the eddy current flowing so as to cancel the magnetic flux interlinking with the steel sheet. The induction heating device is energy efficient because it is directly heated, and the production amount can be expected to be improved because it is rapidly heated. The calorific value of the steel sheet by the induction heating device changes depending on the thickness, width, and speed of the steel sheet. Therefore, in the temperature control of the steel sheet by the induction heating device, the output of the induction heating device is set according to the plate thickness, the plate width, and the speed of the steel plate in order to achieve the target steel plate temperature or the heating temperature. There is.

ところで、熱間圧延における歩留まりの改善、薄物の安定圧延のため、連続鋳造機とミルが直結した圧延ラインによるエンドレス圧延が行われている。エンドレス圧延では、連続鋳造機から抽出された高温の鋼板スラブが、ライン上を搬送されて、順次圧延され、コイラの手前でコイル長にカットされて巻き取られる。このようなエンドレス圧延では、鋼板の板厚を走間で変更する走間板厚変更を行う場合がある。走間板厚変更を行う場合、板厚の変更開始点と終了点との間に、連続的に板厚が変化するテーパ部が発生する。 By the way, in order to improve the yield in hot rolling and stable rolling of thin materials, endless rolling is performed by a rolling line in which a continuous casting machine and a mill are directly connected. In endless rolling, a high-temperature steel plate slab extracted from a continuous casting machine is conveyed on a line, rolled in sequence, cut to a coil length in front of a coiler, and wound. In such endless rolling, the inter-run plate thickness may be changed by changing the plate thickness of the steel plate between runs. When the inter-running plate thickness is changed, a tapered portion in which the plate thickness changes continuously is generated between the plate thickness change start point and the plate thickness change end point.

鋼板のテーパ部は、最終的にはカットされて製品にはならない部位である。しかし、だからといってテーパ部に対する温度制御は不要にはならない。当然ながらテーパ部は前後の鋼板とつながっているため、テーパ部の温度制御ができていないと、テーパ部の前後の鋼板、つまり製品となる部位の品質に悪影響を及んでしまうからである。最終的にカットする部位を最小にするためには、テーパ部にも製品となる部位と同様の厳しい温度制御が求められる。 The tapered portion of the steel sheet is a portion that is finally cut and does not become a product. However, this does not mean that temperature control for the tapered portion is unnecessary. As a matter of course, the tapered portion is connected to the front and rear steel plates, and if the temperature of the tapered portion is not controlled, the quality of the steel plates before and after the tapered portion, that is, the part to be a product, is adversely affected. In order to minimize the part to be finally cut, the tapered part is also required to have the same strict temperature control as the part to be a product.

特許文献1には、先行材の尾端と後行材の先端とを接合するエンドレス圧延における鋼板の温度制御に関する方法が開示されている。特許文献1に開示された方法によれば、加熱効率と板厚との関係に基づき、仕上げ圧延機出側の目標温度を達するように接合部近傍の板厚を設定して誘導加熱装置による加熱が行われる。 Patent Document 1 discloses a method for controlling the temperature of a steel sheet in endless rolling in which the tail end of a leading material and the tip of a trailing material are joined. According to the method disclosed in Patent Document 1, based on the relationship between the heating efficiency and the plate thickness, the plate thickness near the joint is set so as to reach the target temperature on the exit side of the finish rolling mill, and the plate is heated by the induction heating device. Is done.

しかしながら、特許文献1に開示された方法は、走間板厚変更の前後で鋼板にテーパ部が生じない場合の方法である。連続鋳造機とミルが直結するエンドレス圧延において、走間板厚変更によって鋼板の板厚がテーパ状に変更するような場合には、特許文献1に開示された方法をそのまま適用することはできない。 However, the method disclosed in Patent Document 1 is a method in which a tapered portion does not occur in the steel sheet before and after the change in the running plate thickness. In endless rolling in which a continuous casting machine and a mill are directly connected, when the plate thickness of a steel plate is changed to a tapered shape by changing the plate thickness between running sheets, the method disclosed in Patent Document 1 cannot be applied as it is.

特開2000−271607号公報Japanese Unexamined Patent Publication No. 2000-271607

本発明は、上述のような課題に鑑みてなされたものであり、エンドレス圧延中に鋼板の板厚を走間で変更する走間板厚変更を行う場合において、鋼板のテーパ部の温度を適切に制御することによってテーパ部近傍の製品品質の向上をはかることができる熱間エンドレス圧延ラインの鋼板温度制御装置を提供することを目的とする。 The present invention has been made in view of the above-mentioned problems, and when the inter-run sheet thickness is changed during endless rolling, the temperature of the tapered portion of the steel sheet is appropriately adjusted. It is an object of the present invention to provide a steel sheet temperature control device for a hot endless rolling line, which can improve the product quality in the vicinity of the tapered portion by controlling the temperature.

本発明に係る熱間エンドレス圧延ラインの鋼板温度制御装置は、粗圧延機、誘導加熱装置、仕上げ圧延機の順に鋼板が流れる熱間エンドレス圧延ラインにおいて、仕上げ圧延機に入る鋼板の温度を誘導加熱装置の出力によって制御する鋼板温度制御装置である。本発明に係る熱間エンドレス圧延ラインの鋼板温度制御装置は、鋼板の板厚を走間で変更する走間板厚変更を行う場合、以下に詳細を述べるテーパ部板厚計算処理と誘導加熱装置出力計算処理とを実行することを特徴とする。 The steel sheet temperature control device for the hot endless rolling line according to the present invention induces and heats the temperature of the steel sheet entering the finish rolling mill in the hot endless rolling line in which the steel sheet flows in the order of the rough rolling mill, the induction heating device, and the finish rolling mill. It is a steel sheet temperature control device that is controlled by the output of the device. The steel plate temperature control device for the hot endless rolling line according to the present invention is a taper plate thickness calculation process and an induction heating device described in detail below when the inter-run plate thickness is changed by changing the plate thickness of the steel plate between runs. It is characterized by executing output calculation processing.

テーパ部板厚計算処理は、粗圧延機の板厚変更動作によって生じる鋼板のテーパ部の板厚を計算する処理である。例えば、走間板厚変更の前後での鋼板の目標板厚、テーパ部の設定長、そして、鋼板の搬送速度が分かれば、誘導加熱装置を通過するテーパ部の板厚は時間の関数で表すことができる。テーパ部板厚計算処理では、例えば、テーパ部の開始点から終了点まで連続的に変化する板厚を計算してもよい。或いは、テーパ部板厚計算処理では、テーパ部の開始点と終了点の板厚のみを計算してもよい。また、テーパ部板厚計算処理では、テーパ部の圧延方向に複数の中間目標点を設定し、テーパ部の開始点と終了点の板厚に加えて、各中間目標点における板厚を計算してもよい。 The taper portion plate thickness calculation process is a process of calculating the plate thickness of the taper portion of the steel plate caused by the plate thickness changing operation of the rough rolling mill. For example, if the target plate thickness of the steel plate before and after the change in the running plate thickness, the set length of the tapered portion, and the transport speed of the steel plate are known, the plate thickness of the tapered portion passing through the induction heating device is expressed as a function of time. be able to. In the taper portion plate thickness calculation process, for example, a plate thickness that continuously changes from the start point to the end point of the tapered portion may be calculated. Alternatively, in the taper portion plate thickness calculation process, only the plate thickness at the start point and the end point of the taper portion may be calculated. Further, in the taper portion plate thickness calculation process, a plurality of intermediate target points are set in the rolling direction of the tapered portion, and in addition to the plate thicknesses at the start point and end point of the tapered portion, the plate thickness at each intermediate target point is calculated. You may.

誘導加熱装置出力計算処理は、テーパ部が誘導加熱装置を通過する際の誘導加熱装置の出力を計算する処理である。この計算は、目標温度又は目標昇温量を達成するための鋼板の板厚と誘導加熱装置の出力との関係を規定したマップ又は関数を用いて、テーパ部板厚計算処理で計算されたテーパ部の板厚に基づいて行われる。誘導加熱装置出力計算処理で計算された誘導加熱装置の出力は、誘導加熱装置を制御する誘導加熱装置制御装置に対して設定される。 The induction heating device output calculation process is a process of calculating the output of the induction heating device when the tapered portion passes through the induction heating device. This calculation uses a map or function that defines the relationship between the plate thickness of the steel plate to achieve the target temperature or the target temperature rise amount and the output of the induction heating device, and the taper calculated by the taper plate thickness calculation process. It is done based on the plate thickness of the part. The output of the induction heating device calculated by the induction heating device output calculation process is set for the induction heating device control device that controls the induction heating device.

上記内容のテーパ部板厚計算処理と誘導加熱装置出力計算処理とを実行することにより、鋼板のテーパ部が誘導加熱装置を通過する際の誘導加熱装置の出力を、連続的に変化するテーパ部の板厚に応じて適切に制御することができる。 By executing the taper portion thickness calculation process and the induction heating device output calculation process of the above contents, the taper portion that continuously changes the output of the induction heating device when the tapered portion of the steel sheet passes through the induction heating device. It can be appropriately controlled according to the plate thickness of.

誘導加熱装置出力計算処理では、テーパ部の開始点の板厚とテーパ部の終了点の板厚とに基づき、テーパ部が誘導加熱装置を通過する際の誘導加熱装置の出力を計算してもよい。テーパ部の開始点と終了点の板厚に加えて、テーパ部の圧延方向に設定された複数の中間目標点における板厚にも基づき、テーパ部が誘導加熱装置を通過する際の誘導加熱装置の出力を計算してもよい。 In the induction heating device output calculation process, even if the output of the induction heating device when the tapered portion passes through the induction heating device is calculated based on the plate thickness at the start point of the tapered portion and the plate thickness at the end point of the tapered portion. good. Induction heating device when the tapered part passes through the induction heating device based on the plate thickness at the start point and end point of the taper part as well as the plate thickness at a plurality of intermediate target points set in the rolling direction of the taper part. The output of may be calculated.

誘導加熱装置出力計算処理では、テーパ部の開始点の板厚に応じた誘導加熱装置の出力から、テーパ部の終了点の板厚に応じた誘導加熱装置の出力へ、誘導加熱装置の出力を連続的に変化させてもよい。或いは、誘導加熱装置出力計算処理では、テーパ部の開始点の板厚に応じた誘導加熱装置の出力から、テーパ部の終了点の板厚に応じた誘導加熱装置の出力へ、誘導加熱装置の出力を段階的に変化させてもよい。 In the induction heating device output calculation process, the output of the induction heating device is output from the output of the induction heating device according to the plate thickness at the start point of the tapered portion to the output of the induction heating device according to the plate thickness at the end point of the tapered portion. It may be changed continuously. Alternatively, in the induction heating device output calculation process, the output of the induction heating device according to the plate thickness at the start point of the tapered portion is changed to the output of the induction heating device according to the plate thickness at the end point of the tapered portion. The output may be varied stepwise.

誘導加熱装置出力計算処理では、誘導加熱装置に入る鋼板の温度条件に応じて誘導加熱装置の出力を補正してもよい。例えば、鋼板の温度制御が目標温度を用いて行われるのであれば、誘導加熱装置の上流側に設置した温度計から鋼板の入側実績温度を収集し、マップ又は関数の前提となる鋼板の入側計画温度と入側実績温度との偏差に応じて誘導加熱装置の出力を補正してもよい。鋼板の温度制御が目標昇温量を用いて行われるのであれば、誘導加熱装置の上流側に設置した温度計から鋼板の入側実績昇温量を収集し、マップ又は関数の前提となる鋼板の入側計画昇温量と入側実績昇温量との偏差に応じて誘導加熱装置の出力を補正してもよい。 In the induction heating device output calculation process, the output of the induction heating device may be corrected according to the temperature condition of the steel plate entering the induction heating device. For example, if the temperature of the steel sheet is controlled using the target temperature, the actual temperature on the side of the steel sheet is collected from the thermometer installed on the upstream side of the induction heating device, and the temperature of the steel sheet, which is the premise of the map or function, is inserted. The output of the induction heating device may be corrected according to the deviation between the side planned temperature and the incoming side actual temperature. If the temperature of the steel sheet is controlled using the target temperature rise amount, the actual temperature rise amount on the entry side of the steel sheet is collected from the thermometer installed on the upstream side of the induction heating device, and the steel sheet is the premise of the map or function. The output of the induction heating device may be corrected according to the deviation between the planned temperature rise amount on the entrance side and the actual temperature rise amount on the entrance side.

誘導加熱装置出力計算処理では、誘導加熱装置から出た鋼板の温度条件に応じて誘導加熱装置の出力を補正してもよい。例えば、鋼板の温度制御が目標温度を用いて行われるのであれば、誘導加熱装置の下流側に設置した温度計から鋼板の出側実績温度を収集し、目標温度と出側実績温度との偏差に応じて誘導加熱装置の出力を補正してもよい。鋼板の温度制御が目標昇温量を用いて行われるのであれば、誘導加熱装置の下流側に設置した温度計から鋼板の出側実績昇温量を収集し目標昇温量と出側実績昇温量との偏差に応じて誘導加熱装置の出力を補正してもよい。 In the induction heating device output calculation process, the output of the induction heating device may be corrected according to the temperature condition of the steel plate output from the induction heating device. For example, if the temperature of the steel sheet is controlled using the target temperature, the actual temperature on the exit side of the steel sheet is collected from the thermometer installed on the downstream side of the induction heating device, and the deviation between the target temperature and the actual temperature on the exit side is obtained. The output of the induction heating device may be corrected accordingly. If the temperature of the steel sheet is controlled using the target temperature rise amount, the target temperature rise amount and the output side actual temperature increase are collected from the thermometer installed on the downstream side of the induction heating device. The output of the induction heating device may be corrected according to the deviation from the temperature.

本発明に係る熱間エンドレス圧延ラインの鋼板温度制御装置によれば、鋼板のテーパ部が誘導加熱装置を通過する際の誘導加熱装置の出力を、連続的に変化するテーパ部の板厚に応じて適切に制御することができる。これにより、仕上げ圧延機に入る鋼板のテーパ部において目標温度又は目標昇温量を達成することができ、テーパ部近傍の製品品質を向上させることができる。 According to the steel plate temperature control device for the hot endless rolling line according to the present invention, the output of the induction heating device when the tapered portion of the steel sheet passes through the induction heating device depends on the plate thickness of the continuously changing tapered portion. Can be controlled appropriately. As a result, the target temperature or the target temperature rise amount can be achieved in the tapered portion of the steel sheet entering the finish rolling mill, and the product quality in the vicinity of the tapered portion can be improved.

熱間エンドレス圧延ラインの構成の一例を示す図である。It is a figure which shows an example of the structure of a hot endless rolling line. エンドレス圧延における走間板厚変更によって鋼板の板厚が変更される様子を模式的に示す図である。It is a figure which shows typically the mode that the plate thickness of a steel plate is changed by changing the plate thickness between running in endless rolling. 本発明の各実施の形態に共通の鋼板温度制御装置の構成を示す図である。It is a figure which shows the structure of the steel plate temperature control apparatus common to each embodiment of this invention. 本発明の実施の形態1の誘導加熱装置出力計算処理について説明する図である。It is a figure explaining the induction heating apparatus output calculation process of Embodiment 1 of this invention. 本発明の実施の形態2の誘導加熱装置出力計算処理について説明する図である。It is a figure explaining the induction heating apparatus output calculation process of Embodiment 2 of this invention. 本発明の実施の形態3の誘導加熱装置出力計算処理について説明する図である。It is a figure explaining the induction heating apparatus output calculation process of Embodiment 3 of this invention. 本発明の実施の形態3の誘導加熱装置出力計算処理について説明する図である。It is a figure explaining the induction heating apparatus output calculation process of Embodiment 3 of this invention. 本発明の実施の形態4の誘導加熱装置出力計算処理について説明する図である。It is a figure explaining the induction heating apparatus output calculation process of Embodiment 4 of this invention. 本発明の実施の形態5の誘導加熱装置出力計算処理について説明する図である。It is a figure explaining the induction heating apparatus output calculation process of Embodiment 5 of this invention.

以下、図面を参照して本発明の実施の形態について説明する。ただし、以下に示す実施の形態において各要素の個数、数量、量、範囲等の数に言及した場合、特に明示した場合や原理的に明らかにその数に特定される場合を除いて、その言及した数にこの発明が限定されるものではない。また、以下に示す実施の形態において説明する構造は、特に明示した場合や明らかに原理的にそれに特定される場合を除いて、この発明に必ずしも必須のものではない。 Hereinafter, embodiments of the present invention will be described with reference to the drawings. However, when the number, quantity, quantity, range, etc. of each element is referred to in the embodiment shown below, the reference is made unless otherwise specified or clearly specified by the number in principle. The present invention is not limited to the number of cases. In addition, the structure described in the embodiments shown below is not necessarily essential to the present invention, except when explicitly stated or when it is clearly specified in principle.

1.熱間エンドレス圧延ラインの構成
先ず、本発明に係る鋼板温度制御装置が適用される熱間エンドレス圧延ラインについて説明する。図1は、熱間エンドレス圧延ラインの構成の一例を示す図である。連続鋳造機1から抽出された鋼板6は、スラブ加熱炉2で加熱され、圧延ラインに抽出される。圧延ラインにおいてエッジャ3を通過した鋼板6は、粗圧延機4及び仕上げ圧延機9にて、所望の厚さまで薄く延ばされると同時に、所望の幅に加工される。
1. 1. Configuration of Hot Endless Rolling Line First, a hot endless rolling line to which the steel sheet temperature control device according to the present invention is applied will be described. FIG. 1 is a diagram showing an example of the configuration of a hot endless rolling line. The steel plate 6 extracted from the continuous casting machine 1 is heated in the slab heating furnace 2 and extracted into a rolling line. The steel plate 6 that has passed through the edger 3 in the rolling line is thinly rolled to a desired thickness by the rough rolling mill 4 and the finish rolling mill 9, and at the same time, is processed into a desired width.

粗圧延機4は、1又は複数の圧延スタンドから構成され、上流から下流への一方向で鋼板6を圧延し、鋼板6の板厚や板幅を製品寸法に近づける。粗圧延機4では、鋼板温度を測定する粗出側温度計5が付属することもある。誘導加熱装置7は、粗圧延機4と仕上げ圧延機9の間のライン上に設置され、誘導加熱装置7を通過する鋼板6を加熱する。 The rough rolling mill 4 is composed of one or a plurality of rolling stands, and rolls the steel plate 6 in one direction from upstream to downstream to bring the thickness and width of the steel plate 6 close to the product dimensions. The rough rolling mill 4 may be provided with a roughing side thermometer 5 for measuring the temperature of the steel sheet. The induction heating device 7 is installed on a line between the rough rolling mill 4 and the finishing rolling mill 9, and heats the steel plate 6 passing through the induction heating device 7.

仕上げ圧延機9は、複数の圧延スタンドから構成され、上流から下流への一方向で鋼板6を圧延し、鋼板の板厚や板幅などの寸法に関する最終品質を決定づける。仕上げ圧延後の鋼板温度は、仕上げ出側温度計10により測定される。また、仕上げ入側温度計8が、誘導加熱装置7と仕上げ圧延機9との間に設置されることもある。 The finish rolling mill 9 is composed of a plurality of rolling stands, rolls the steel plate 6 in one direction from upstream to downstream, and determines the final quality regarding dimensions such as plate thickness and plate width of the steel plate. The temperature of the steel sheet after finish rolling is measured by the finish side thermometer 10. Further, the finish-in side thermometer 8 may be installed between the induction heating device 7 and the finish rolling mill 9.

仕上げ圧延機9の下流には冷却テーブル11が設置されている。冷却テーブル11は、鋼板6に注水して鋼板6の温度を下げる。冷却テーブル11を通った鋼板6は、コイラ前シャー12でコイル長に切断されてコイラ13でコイル状に巻かれる。 A cooling table 11 is installed downstream of the finish rolling mill 9. The cooling table 11 injects water into the steel plate 6 to lower the temperature of the steel plate 6. The steel plate 6 that has passed through the cooling table 11 is cut to a coil length by the shear 12 in front of the coiler and wound into a coil by the coiler 13.

鋼板6の板厚を走間で変更する走間板厚変更を行う場合、粗圧延機4の各圧延スタンドのロールギャップを段階的に変更し、或いは、粗圧延機4及び仕上げ圧延機9の各圧延スタンドのロールギャップを段階的に変更し、操業を止めることなく板厚を変更する。図2は、エンドレス圧延における走間板厚変更によって鋼板6の板厚が変更される様子を模式的に示す図である。図2に示すように、走間板厚変更中においては、粗圧延機4の板厚変更動作によって、スタンド間に鋼板6の板厚が連続的に変化する部位が発生する。この部位が最終スタンドの出側まで残ったものが鋼板6のテーパ部6aとなる。 When changing the running plate thickness of the steel plate 6 between runs, the roll gap of each rolling stand of the rough rolling mill 4 is changed stepwise, or the rough rolling mill 4 and the finish rolling mill 9 are used. The roll gap of each rolling stand is changed step by step, and the plate thickness is changed without stopping the operation. FIG. 2 is a diagram schematically showing how the plate thickness of the steel plate 6 is changed by changing the running plate thickness in endless rolling. As shown in FIG. 2, during the running plate thickness change, a portion where the plate thickness of the steel plate 6 continuously changes is generated between the stands due to the plate thickness changing operation of the rough rolling mill 4. The portion where this portion remains up to the protruding side of the final stand is the tapered portion 6a of the steel plate 6.

2.鋼板温度制御装置の構成
次に、本発明の各実施の形態に共通の鋼板温度制御装置の構成について図3を用いて説明する。図3は、鋼板温度制御装置の構成の一例を示す図である。熱間エンドレス圧延ラインには、圧延に係る各種パラメータを設定する圧延設定装置15が設けられる。圧延設定装置15は、例えば、少なくとも1つのプロセッサと少なくとも1つのメモリとを備えるコンピュータである。メモリに記憶されたプログラムがプロセッサで実行されることにより、コンピュータである圧延設定装置15は鋼板温度制御装置として機能する。
2. Configuration of Steel Sheet Temperature Control Device Next, the configuration of the steel sheet temperature control device common to each embodiment of the present invention will be described with reference to FIG. FIG. 3 is a diagram showing an example of the configuration of the steel sheet temperature control device. The hot endless rolling line is provided with a rolling setting device 15 for setting various parameters related to rolling. The rolling setting device 15 is, for example, a computer including at least one processor and at least one memory. When the program stored in the memory is executed by the processor, the rolling setting device 15 which is a computer functions as a steel sheet temperature control device.

鋼板温度制御装置としての圧延設定装置15は、板厚設定計算部17と誘導加熱装置出力計算部19とを備える。板厚設定計算部17は、走間板厚変更計算部16を含む。これらの計算部16、17、19は、ハードウェアとして存在するものではなく、圧延設定装置15のメモリに記憶されたプログラムによってソフトウェア的に実現される。以下、鋼板温度制御装置としての圧延設定装置15を構成する各計算部16、17、19の機能について説明する。 The rolling setting device 15 as a steel plate temperature control device includes a plate thickness setting calculation unit 17 and an induction heating device output calculation unit 19. The plate thickness setting calculation unit 17 includes a running plate thickness change calculation unit 16. These calculation units 16, 17, and 19 do not exist as hardware, but are realized by software by a program stored in the memory of the rolling setting device 15. Hereinafter, the functions of the calculation units 16, 17, and 19 constituting the rolling setting device 15 as the steel sheet temperature control device will be described.

圧延設定装置15は、上位計算機30と通信する。上位計算機30には、鋼板6の目標板厚を設定する目標板厚設定部31と、鋼板の目標温度を設定する目標温度設定部32とを備える。目標板厚と目標温度とは、製品の仕様及び要求品質に基づいて設定される。ただし、目標温度設定部32では、目標温度に代えて目標昇温量を設定してもよい。昇温量とは、基準温度に対する相対温度を意味する。 The rolling setting device 15 communicates with the host computer 30. The host computer 30 includes a target plate thickness setting unit 31 for setting a target plate thickness of the steel plate 6 and a target temperature setting unit 32 for setting a target temperature of the steel plate. The target plate thickness and target temperature are set based on the product specifications and required quality. However, the target temperature setting unit 32 may set a target temperature rise amount instead of the target temperature. The amount of temperature rise means the temperature relative to the reference temperature.

圧延設定装置15の板厚設定計算部17は、目標板厚設定部31から目標板厚を受信し、受信した目標板厚に基づいて板厚設定値を計算する。走間板厚変更を行う際には、板厚設定計算部17は、板厚変更後の目標板厚を目標板厚設定部31から受信し、走間板厚変更計算部16において、走間板厚変更における各スタンドでの板厚変更量を計算する。そして、各スタンドでの板厚変更量から圧延パススケジュールを作成し、圧延機制御装置21に圧延パススケジュールを送信する。圧延機制御装置21は圧延パススケジュールに従って粗圧延機4及び仕上げ圧延機9の各スタンドの動作を制御する。 The plate thickness setting calculation unit 17 of the rolling setting device 15 receives the target plate thickness from the target plate thickness setting unit 31, and calculates the plate thickness setting value based on the received target plate thickness. When changing the running plate thickness, the plate thickness setting calculation unit 17 receives the target plate thickness after the plate thickness change from the target plate thickness setting unit 31, and the inter-run plate thickness change calculation unit 16 receives the target plate thickness between runs. Calculate the amount of plate thickness change at each stand when changing plate thickness. Then, a rolling path schedule is created from the amount of change in plate thickness at each stand, and the rolling path schedule is transmitted to the rolling mill control device 21. The rolling mill control device 21 controls the operation of each stand of the rough rolling mill 4 and the finish rolling mill 9 according to the rolling path schedule.

また、板厚設定計算部17は、誘導加熱装置出力計算部19に対して板厚設定値を送信する。走間板厚変更を行う際には、走間板厚変更計算部16は、走間板厚変更によって生じる鋼板6のテーパ部6aの板厚を計算するテーパ部板厚計算処理を行い、テーパ部6aの板厚に関する板厚情報を誘導加熱装置出力計算部19に対して送信する。走間板厚変更計算部16から送信されるテーパ部6aの板厚情報には、例えば、テーパ部6aの開始点の位置と板厚、テーパ部6aの終了点の位置と板厚が含まれる。 Further, the plate thickness setting calculation unit 17 transmits the plate thickness setting value to the induction heating device output calculation unit 19. When changing the running plate thickness, the running plate thickness change calculation unit 16 performs a taper portion plate thickness calculation process for calculating the plate thickness of the tapered portion 6a of the steel plate 6 caused by the change in the running plate thickness, and tapers. The plate thickness information regarding the plate thickness of the unit 6a is transmitted to the induction heating device output calculation unit 19. The plate thickness information of the tapered portion 6a transmitted from the inter-running plate thickness change calculation unit 16 includes, for example, the position and thickness of the start point of the tapered portion 6a and the position and plate thickness of the end point of the tapered portion 6a. ..

誘導加熱装置出力計算部19は、目標温度設定部32から目標温度又は目標昇温量を受信するとともに、板厚設定計算部17から目標板厚を受信する。走間板厚変更を行う際には、走間板厚変更計算部16からテーパ部6aの板厚情報を受信する。誘導加熱装置出力計算部19は、目標温度又は目標昇温量を達成するための鋼板6の板厚と誘導加熱装置7の出力との関係を規定したマップ又は関数を用いて、誘導加熱装置7の出力(電力)を計算する。走間板厚変更を行う際には、走間板厚変更計算部16から受信したテーパ部6aの板厚情報に基づき、テーパ部6aが誘導加熱装置7を通過する際の誘導加熱装置7の出力を計算する。誘導加熱装置出力計算部19は、計算した誘導加熱装置7の出力を誘導加熱装置制御装置22に対して設定する。 The induction heating device output calculation unit 19 receives the target temperature or the target temperature rise amount from the target temperature setting unit 32, and also receives the target plate thickness from the plate thickness setting calculation unit 17. When changing the running plate thickness, the plate thickness information of the tapered portion 6a is received from the running plate thickness change calculation unit 16. The induction heating device output calculation unit 19 uses a map or a function that defines the relationship between the thickness of the steel plate 6 and the output of the induction heating device 7 for achieving the target temperature or the target temperature rise amount, and the induction heating device 7 Calculate the output (power) of. When changing the running plate thickness, the induction heating device 7 when the tapered portion 6a passes through the induction heating device 7 based on the plate thickness information of the taper portion 6a received from the running plate thickness change calculation unit 16. Calculate the output. The induction heating device output calculation unit 19 sets the calculated output of the induction heating device 7 with respect to the induction heating device control device 22.

以下に挙げた各実施の形態では、誘導加熱装置出力計算部19で行われる誘導加熱装置出力計算処理の詳細について説明する。 In each of the following embodiments, the details of the induction heating device output calculation process performed by the induction heating device output calculation unit 19 will be described.

3.実施の形態1の誘導加熱装置出力計算処理
図4は、本発明の実施の形態1の誘導加熱装置出力計算処理について説明する図である。図4の上段のグラフには、誘導加熱装置7が鋼板6のテーパ部6aが通過する際の誘導加熱装置7内の所定位置での板厚hの時間による変化が描かれ、下段のグラフには、誘導加熱装置7の出力pの時間による変化が描かれている。
3. 3. Induction heating device output calculation process of the first embodiment FIG. 4 is a diagram illustrating the induction heating device output calculation process of the first embodiment of the present invention. In the upper graph of FIG. 4, when the induction heating device 7 passes through the tapered portion 6a of the steel plate 6, the change in the plate thickness h at a predetermined position in the induction heating device 7 with time is drawn, and the lower graph shows the change. Is drawn a change in the output p of the induction heating device 7 with time.

図4に示す例では、誘導加熱装置7内の所定位置での板厚hは、hからhに変化している。目標温度或いは目標昇温量を達成することができる誘導加熱装置7の出力pは、板厚hが薄いほど小さくなる。図4に示す例では、走間板厚変更の前の板厚hには出力pが対応し、走間板厚変更の後の板厚hには出力pが対応する。板厚hが変化し始める時刻tに対応する部位がテーパ部6aの開始点であり、板厚hが変化し終わる時刻tに対応する部位がテーパ部6aの終了点である。テーパ部6aの板厚hは、hからhに連続的に変化する。 In the example shown in FIG. 4, the plate thickness h at a predetermined position in the induction heating device 7 changes from h 0 to h 1. The output p of the induction heating device 7 capable of achieving the target temperature or the target temperature rise amount becomes smaller as the plate thickness h becomes thinner. In the example shown in FIG. 4, the output p 0 corresponds to the plate thickness h 0 before the change in the inter-run plate thickness, and the output p 1 corresponds to the plate thickness h 1 after the change in the inter-run plate thickness. The portion corresponding to the time t 0 when the plate thickness h starts to change is the start point of the tapered portion 6a, and the portion corresponding to the time t 1 when the plate thickness h starts to change is the end point of the tapered portion 6a. The plate thickness h of the tapered portion 6a continuously changes from h 0 to h 1.

本実施の形態の誘導加熱装置出力計算処理では、テーパ部6aの開始点の板厚hとテーパ部6aの終了点の板厚hとに基づき、テーパ部6aが誘導加熱装置7を通過する際の誘導加熱装置7の出力pを計算する。具体的には、テーパ部6aの開始点の板厚hに応じた出力pから、テーパ部6aの終了点の板厚hに応じた出力pへ、誘導加熱装置7の出力pを一定速度で連続的に変化させる。なお、誘導加熱装置7の出力を変化させてから鋼板6の温度が変化するまでの間には応答遅れが存在する。誘導加熱装置7の出力を変化させる開始時刻は、ライン上でのテーパ部6aの走行位置と応答遅れとに基づいて決定される。 In the induction heating device output calculation process of the present embodiment, the tapered portion 6a passes through the induction heating device 7 based on the plate thickness h 0 at the start point of the tapered portion 6a and the plate thickness h 1 at the ending point of the tapered portion 6a. The output p of the induction heating device 7 is calculated. Specifically, the output p of the induction heating device 7 is changed from the output p 0 corresponding to the plate thickness h 0 at the start point of the tapered portion 6a to the output p 1 corresponding to the plate thickness h 1 at the end point of the tapered portion 6a. Is continuously changed at a constant speed. There is a response delay between the time when the output of the induction heating device 7 is changed and the time when the temperature of the steel sheet 6 changes. The start time for changing the output of the induction heating device 7 is determined based on the traveling position of the tapered portion 6a on the line and the response delay.

4.実施の形態2の誘導加熱装置出力計算処理
図5は、本発明の実施の形態2の誘導加熱装置出力計算処理について説明する図である。図5の上段のグラフには、誘導加熱装置7が鋼板6のテーパ部6aが通過する際の誘導加熱装置7内の所定位置での板厚hの時間による変化が描かれ、下段のグラフには、誘導加熱装置7の出力pの時間による変化が描かれている。
4. Induction heating device output calculation process of the second embodiment FIG. 5 is a diagram illustrating the induction heating device output calculation process of the second embodiment of the present invention. In the upper graph of FIG. 5, the change of the plate thickness h at a predetermined position in the induction heating device 7 when the tapered portion 6a of the steel plate 6 passes through the induction heating device 7 is drawn, and the lower graph shows the change with time. Is drawn a change in the output p of the induction heating device 7 with time.

図5に示す例では、図4に示す例と同様に、誘導加熱装置7内の所定位置での板厚hは、hからhに連続的に変化している。本実施の形態の誘導加熱装置出力計算処理では、テーパ部6aの開始点の板厚hとテーパ部6aの終了点の板厚hとに加えて、テーパ部6aの圧延方向に設定された複数の中間目標点における板厚にも基づき、テーパ部6aが誘導加熱装置7を通過する際の誘導加熱装置7の出力pを計算する。 In the example shown in FIG. 5, the plate thickness h at a predetermined position in the induction heating device 7 continuously changes from h 0 to h 1 as in the example shown in FIG. In the induction heating device output calculation process of the present embodiment, in addition to the plate thickness h 0 at the start point of the tapered portion 6a and the plate thickness h 1 at the end point of the tapered portion 6a, the thickness is set in the rolling direction of the tapered portion 6a. The output p of the induction heating device 7 when the tapered portion 6a passes through the induction heating device 7 is calculated based on the plate thickness at the plurality of intermediate target points.

中間目標点は、テーパ部6aの開始時刻tから終了時刻tまでの間の任意の複数の時刻tc0,tc1に対応する部位である。各中間目標点の時刻tc0,tc1における板厚hc0,hc1を計算し、前述のマップ又は関数を用いて、目標温度或いは目標昇温量を達成することができる誘導加熱装置7の出力pc0,pc1を計算する。テーパ部6aの開始点と中間目標点との間、中間目標点の間、中間目標点とテーパ部6aの終了点との間の誘導加熱装置の出力pは線形近似により計算される。 The intermediate target point is a portion of the tapered portion 6a corresponding to a plurality of arbitrary times t c0 and t c1 between the start time t 0 and the end time t 1. The induction heating device 7 capable of calculating the plate thicknesses h c0 and h c1 at the times t c0 and t c1 of each intermediate target point and achieving the target temperature or the target temperature rise amount by using the above-mentioned map or function. Calculate the outputs p c0 and p c1. The output p of the induction heating device between the start point and the intermediate target point of the tapered portion 6a, between the intermediate target points, and between the intermediate target point and the end point of the tapered portion 6a is calculated by linear approximation.

5.実施の形態3の誘導加熱装置出力計算処理
図6及び図7は、本発明の実施の形態3の誘導加熱装置出力計算処理について説明する図である。図6及び図7の上段のグラフには、誘導加熱装置7が鋼板6のテーパ部6aが通過する際の誘導加熱装置7内の所定位置での板厚hの時間による変化が描かれ、下段のグラフには、誘導加熱装置7の出力pの時間による変化が描かれている。
5. Induction heating device output calculation process of the third embodiment FIGS. 6 and 7 are diagrams for explaining the induction heating device output calculation process of the third embodiment of the present invention. In the upper graphs of FIGS. 6 and 7, when the induction heating device 7 passes through the tapered portion 6a of the steel plate 6, the change in the plate thickness h at a predetermined position in the induction heating device 7 with time is drawn, and the lower graph shows. In the graph of, the change of the output p of the induction heating device 7 with time is drawn.

図6及び図7に示す例では、図4に示す例と同様に、誘導加熱装置7内の所定位置での板厚hは、hからhに連続的に変化している。本実施の形態の誘導加熱装置出力計算処理では、テーパ部6aの開始点の板厚hに応じた誘導加熱装置7の出力pから、テーパ部6aの終了点の板厚hに応じた誘導加熱装置7の出力pへ、誘導加熱装置7の出力pを段階的に変化させる。 In the examples shown in FIGS. 6 and 7, the plate thickness h at a predetermined position in the induction heating device 7 continuously changes from h 0 to h 1 as in the example shown in FIG. In the induction heating device output calculation process of the present embodiment, the output p 0 of the induction heating device 7 corresponding to the plate thickness h 0 of the start point of the tapered portion 6a corresponds to the plate thickness h 1 of the end point of the tapered portion 6a. The output p of the induction heating device 7 is changed stepwise to the output p 1 of the induction heating device 7.

図6に示す例では、テーパ部6aの開始時刻tにおいて、誘導加熱装置7の出力pを板厚hに応じた出力pから変化させる。その後も、誘導加熱装置7の出力pを段階的に変化させていき、テーパ部6aの終了時刻tにおいて、板厚hに応じた出力pに変化させる。図7に示す例では、テーパ部6aの開始時刻tよりも後の時刻まで、テーパ部6aの開始点の板厚hに応じた出力pを維持する。その後、誘導加熱装置7の出力pを段階的に変化させていき、テーパ部6aの終了時刻tよりも前の時刻で、テーパ部6aの終了点の板厚hに応じた出力pに変化させる。なお、誘導加熱装置7の出力pを段階的に変化させる際の段階数には限定はない。ただし、段階数が少ないほどテーパ部6aの温度分布に斑ができやすくなるので、段階数は多いほうが好ましい。 In the example shown in FIG. 6, at the start time t 0 of the tapered portion 6a, the output p of the induction heating device 7 is changed from the output p 0 according to the plate thickness h 0. After that, go gradually changing the output p of the induction heating device 7, at the end time t 1 of the tapered portion 6a, it is changed to output p 1 corresponding to the thickness h 1. In the example shown in FIG. 7, the output p 0 corresponding to the plate thickness h 0 at the start point of the tapered portion 6a is maintained until a time after the start time t 0 of the tapered portion 6a. After that, the output p of the induction heating device 7 is changed stepwise, and the output p 1 corresponding to the plate thickness h 1 of the end point of the tapered portion 6a at a time before the end time t 1 of the tapered portion 6a. Change to. The number of steps when the output p of the induction heating device 7 is changed stepwise is not limited. However, the smaller the number of steps, the more likely it is that the temperature distribution of the tapered portion 6a will be uneven. Therefore, it is preferable that the number of steps is large.

6.実施の形態4の誘導加熱装置出力計算処理
図8は、本発明の実施の形態3の誘導加熱装置出力計算処理について説明する図である。実施の形態1において誘導加熱装置7の出力の計算に用いているマップ又は関数は、誘導加熱装置7に入る際の鋼板6の計画温度(これを入側計画温度と称する)を前提として作成されている。しかし、機器の個体差や経時変化、操業状態のばらつき、環境条件のばらつき等の要因により、誘導加熱装置7に入る際の鋼板6の実績温度(これを入側実績温度と称する)は必ずしも入側計画温度と一致しない。
6. Induction heating device output calculation process of the fourth embodiment FIG. 8 is a diagram illustrating the induction heating device output calculation process of the third embodiment of the present invention. The map or function used in the calculation of the output of the induction heating device 7 in the first embodiment is created on the premise of the planned temperature of the steel plate 6 when entering the induction heating device 7 (this is referred to as an entry side planned temperature). ing. However, due to factors such as individual differences in equipment, changes over time, variations in operating conditions, and variations in environmental conditions, the actual temperature of the steel sheet 6 when entering the induction heating device 7 (this is called the actual temperature on the entry side) is not always entered. It does not match the side planned temperature.

本実施の形態の誘導加熱装置出力計算処理では、オンライン操業中の入側実績温度を利用して誘導加熱装置7の出力を制御する。詳しくは、誘導加熱装置7の上流側に設置された粗出側温度計5から鋼板6の入側実績温度TAFが収集され、入側実績温度TAFと入側計画温度TCALとが比較される。そして、入側実績温度TAFと入側計画温度TCALとの偏差に基づいて、誘導加熱装置7の補正出力ΔpFFが計算される。補正出力ΔpFFは、入側実績温度TAFが入側計画温度TCALよりも高い場合には負の値とされ、入側実績温度TAFが入側計画温度TCALよりも低い場合には正の値とされる。補正出力ΔpFFが、設定計算における誘導加熱装置7の出力pに加算されることにより、最終的な出力が得られる。 In the induction heating device output calculation process of the present embodiment, the output of the induction heating device 7 is controlled by using the actual temperature on the entry side during online operation. Specifically, induction entry side actual temperature T AF from the heating device 7 crude exit side thermometer 5 which is installed upstream of the steel sheet 6 is collected, and the entry side actual temperature T AF and entry side plan temperature T CAL comparison Will be done. Then, the correction output Δp FF of the induction heating device 7 is calculated based on the deviation between the actual entry-side temperature T AF and the planned entry-side temperature T CAL. The correction output Δp FF is set to a negative value when the incoming side actual temperature T AF is higher than the incoming side planned temperature T CAL , and is set to a negative value when the incoming side actual temperature T AF is lower than the incoming side planned temperature T CAL. It is considered to be a positive value. The final output is obtained by adding the correction output Δp FF to the output p of the induction heating device 7 in the setting calculation.

なお、本実施の形態では粗出側温度計5から入側実績温度を収集しているが、鋼板の温度制御が目標昇温量を用いて行われるのであれば、入側実績温度に代えて入側実績昇温量を収集すればよい。この場合、入側計画昇温量と入側実績昇温量とを比較し、その偏差に応じて誘導加熱装置7の補正出力を計算すればよい。 In this embodiment, the actual temperature on the entry side is collected from the rough outlet side thermometer 5, but if the temperature control of the steel sheet is performed using the target temperature rise amount, the actual temperature on the entry side is replaced with the actual temperature on the entry side. It suffices to collect the actual temperature rise amount on the entrance side. In this case, the planned temperature rise amount on the entry side and the actual temperature rise amount on the entry side may be compared, and the correction output of the induction heating device 7 may be calculated according to the deviation.

7.実施の形態5の誘導加熱装置出力計算処理
図9は、本発明の実施の形態5の誘導加熱装置出力計算処理について説明する図である。実施の形態1において誘導加熱装置7の出力の計算に用いているマップ又は関数は、誘導加熱装置7を通過後の鋼板6の温度が目標温度になるように作成されている。しかし、機器の個体差や経時変化、操業状態のばらつき、環境条件のばらつき等の要因により、誘導加熱装置7を通過後の鋼板6の実績温度(これを出側実績温度と称する)は必ずしも目標温度と一致しない。
7. Induction heating device output calculation process of the fifth embodiment FIG. 9 is a diagram illustrating the induction heating device output calculation process of the fifth embodiment of the present invention. The map or function used in the calculation of the output of the induction heating device 7 in the first embodiment is created so that the temperature of the steel plate 6 after passing through the induction heating device 7 becomes the target temperature. However, the actual temperature of the steel sheet 6 after passing through the induction heating device 7 (this is called the actual temperature at the exit side) is not always the target due to factors such as individual differences in equipment, changes over time, variations in operating conditions, and variations in environmental conditions. Does not match the temperature.

本実施の形態の誘導加熱装置出力計算処理では、オンライン操業中の出側実績温度を利用して誘導加熱装置7の出力を制御する。詳しくは、誘導加熱装置7の下流側に設置された仕上げ入側温度計8から鋼板6の出側実績温度TACTが収集され、目標温度TTGTと出側実績温度TACTとが比較される。そして、目標温度TTGTと出側実績温度TACTとの偏差に基づいて、誘導加熱装置7の補正出力ΔpFBが計算される。補正出力ΔpFBは、出側実績温度TACTが目標温度TTGTよりも高い場合には負の値とされ、出側実績温度TACTが目標温度TTGTよりも低い場合には正の値とされる。補正出力ΔpFBが、設定計算における誘導加熱装置7の出力pに加算されることにより、最終的な出力が得られる。 In the induction heating device output calculation process of the present embodiment, the output of the induction heating device 7 is controlled by using the actual temperature on the exit side during online operation. Specifically, the actual outlet temperature T ACT of the steel plate 6 is collected from the finish inlet thermometer 8 installed on the downstream side of the induction heating device 7, and the target temperature T TGT and the actual outlet temperature T ACT are compared. .. Then, the correction output Δp FB of the induction heating device 7 is calculated based on the deviation between the target temperature T TGT and the actual output side temperature T ACT. Corrected output Delta] p FB, when delivery side actual temperature T ACT is higher than the target temperature T TGT is a negative value, if the exit side actual temperature T ACT is lower than the target temperature T TGT and positive values Will be done. The final output is obtained by adding the corrected output Δp FB to the output p of the induction heating device 7 in the setting calculation.

なお、本実施の形態では仕上げ入側温度計8から出側実績温度を収集しているが、鋼板の温度制御が目標昇温量を用いて行われるのであれば、出側実績温度に代えて出側実績昇温量を収集すればよい。この場合、入側実績昇温量と目標昇温量とを比較し、その偏差に応じて誘導加熱装置7の補正出力を計算すればよい。 In the present embodiment, the actual temperature on the exit side is collected from the finish inlet thermometer 8, but if the temperature control of the steel sheet is performed using the target temperature rise amount, the actual temperature on the outlet side is used instead. It suffices to collect the actual temperature rise amount on the outgoing side. In this case, the actual temperature rise amount on the entry side and the target temperature rise amount may be compared, and the correction output of the induction heating device 7 may be calculated according to the deviation.

8.その他
実施の形態4の誘導加熱装置出力計算処理は、実施の形態1乃至3のどの誘導加熱装置出力計算処理と組み合わせてもよい。また、実施の形態5の誘導加熱装置出力計算処理は、実施の形態1乃至4のどの誘導加熱装置出力計算処理と組み合わせてもよい。
8. Other The induction heating device output calculation process of the fourth embodiment may be combined with any of the induction heating device output calculation processes of the first to third embodiments. Further, the induction heating device output calculation process of the fifth embodiment may be combined with any of the induction heating device output calculation processes of the first to fourth embodiments.

1 連続鋳造機
2 スラブ加熱炉
3 エッジャ
4 粗圧延機
5 粗出側温度計
6 鋼板
7 誘導加熱装置
8 仕上げ入側温度計
9 仕上げ圧延機
10 仕上げ出側温度計
11 冷却テーブル
12 コイラ前シャー
13 コイラ
15 鋼板温度制御装置としての圧延設定装置
16 走間板厚変更計算部
17 板厚設定計算部
19 誘導加熱装置出力計算部
21 圧延機制御装置
22 誘導加熱装置制御装置
30 上位計算機
31 目標板厚設定部
32 目標温度設定部
1 Continuous casting machine 2 Slab heating furnace 3 Edger 4 Rough rolling mill 5 Roughing side thermometer 6 Steel plate 7 Induction heating device 8 Finishing inlet side thermometer 9 Finishing rolling mill 10 Finishing exit side thermometer 11 Cooling table 12 Roller front shear 13 Roller 15 Rolling setting device as steel plate temperature control device 16 Running plate thickness change calculation unit 17 Plate thickness setting calculation unit 19 Induction heating device output calculation unit 21 Rolling machine control device 22 Induction heating device control device 30 Upper computer 31 Target plate thickness Setting unit 32 Target temperature setting unit

Claims (6)

粗圧延機、誘導加熱装置、仕上げ圧延機の順に鋼板が流れる熱間エンドレス圧延ラインにおいて、前記仕上げ圧延機に入る前記鋼板の温度を前記誘導加熱装置の出力によって制御する鋼板温度制御装置であって、
前記鋼板の板厚を走間で変更する走間板厚変更を行う場合、
前記粗圧延機の板厚変更動作によって生じる前記鋼板のテーパ部の板厚を計算するテーパ部板厚計算処理と、
目標温度又は目標昇温量を達成するための前記鋼板の板厚と前記誘導加熱装置の出力との関係を規定したマップ又は関数を用いて、前記テーパ部板厚計算処理で計算された前記テーパ部の板厚に基づき、前記テーパ部が前記誘導加熱装置を通過する際の前記誘導加熱装置の出力を計算する誘導加熱装置出力計算処理と、を実行し、
前記誘導加熱装置出力計算処理では、前記テーパ部の開始点の板厚と前記テーパ部の終了点の板厚とに基づき、前記テーパ部が前記誘導加熱装置を通過する際の前記誘導加熱装置の出力を計算する
ことを特徴とする熱間エンドレス圧延ラインの鋼板温度制御装置。
A steel plate temperature control device that controls the temperature of the steel sheet entering the finish rolling machine by the output of the induction heating device in a hot endless rolling line in which steel sheets flow in the order of a rough rolling mill, an induction heating device, and a finish rolling mill. ,
When changing the inter-run plate thickness to change the plate thickness of the steel plate between runs
Tapered portion plate thickness calculation processing for calculating the plate thickness of the tapered portion of the steel plate caused by the plate thickness changing operation of the rough rolling mill, and
The taper calculated by the taper plate thickness calculation process using a map or function that defines the relationship between the plate thickness of the steel plate and the output of the induction heating device for achieving the target temperature or the target temperature rise amount. Based on the plate thickness of the portion, the induction heating device output calculation process for calculating the output of the induction heating device when the tapered portion passes through the induction heating device is executed .
In the induction heating device output calculation process, the induction heating device when the tapered portion passes through the induction heating device is based on the plate thickness at the start point of the tapered portion and the plate thickness at the end point of the tapered portion. A steel plate temperature control device for hot endless rolling lines, characterized in that the output is calculated.
前記誘導加熱装置出力計算処理では、前記テーパ部の圧延方向に設定された複数の中間目標点における板厚にも基づき、前記テーパ部が前記誘導加熱装置を通過する際の前記誘導加熱装置の出力を計算する
ことを特徴とする請求項1に記載の熱間エンドレス圧延ラインの鋼板温度制御装置。
In the induction heating device output calculation process, the output of the induction heating device when the tapered portion passes through the induction heating device is also based on the plate thickness at a plurality of intermediate target points set in the rolling direction of the tapered portion. The steel plate temperature control device for a hot endless rolling line according to claim 1 , wherein the method is calculated.
粗圧延機、誘導加熱装置、仕上げ圧延機の順に鋼板が流れる熱間エンドレス圧延ラインにおいて、前記仕上げ圧延機に入る前記鋼板の温度を前記誘導加熱装置の出力によって制御する鋼板温度制御装置であって、
前記鋼板の板厚を走間で変更する走間板厚変更を行う場合、
前記粗圧延機の板厚変更動作によって生じる前記鋼板のテーパ部の板厚を計算するテーパ部板厚計算処理と、
目標温度又は目標昇温量を達成するための前記鋼板の板厚と前記誘導加熱装置の出力との関係を規定したマップ又は関数を用いて、前記テーパ部板厚計算処理で計算された前記テーパ部の板厚に基づき、前記テーパ部が前記誘導加熱装置を通過する際の前記誘導加熱装置の出力を計算する誘導加熱装置出力計算処理と、を実行し、
前記誘導加熱装置出力計算処理では、前記テーパ部の開始点の板厚に応じた前記誘導加熱装置の出力から、前記テーパ部の終了点の板厚に応じた前記誘導加熱装置の出力へ、前記誘導加熱装置の出力を連続的に変化させる
ことを特徴とする熱間エンドレス圧延ラインの鋼板温度制御装置。
A steel plate temperature control device that controls the temperature of a steel sheet entering the finish rolling mill by the output of the induction heating device in a hot endless rolling line in which steel sheets flow in the order of a rough rolling mill, an induction heating device, and a finish rolling mill. ,
When changing the inter-run plate thickness to change the plate thickness of the steel plate between runs
Tapered portion plate thickness calculation processing for calculating the plate thickness of the tapered portion of the steel plate caused by the plate thickness changing operation of the rough rolling mill, and
The taper calculated by the taper plate thickness calculation process using a map or function that defines the relationship between the plate thickness of the steel plate and the output of the induction heating device for achieving the target temperature or the target temperature rise amount. Based on the plate thickness of the portion, the induction heating device output calculation process for calculating the output of the induction heating device when the tapered portion passes through the induction heating device is executed .
In the induction heating device output calculation process, the output of the induction heating device according to the plate thickness at the start point of the tapered portion is changed to the output of the induction heating device according to the plate thickness at the end point of the tapered portion. A steel plate temperature control device for a hot endless rolling line, which is characterized by continuously changing the output of an induction heating device.
粗圧延機、誘導加熱装置、仕上げ圧延機の順に鋼板が流れる熱間エンドレス圧延ラインにおいて、前記仕上げ圧延機に入る前記鋼板の温度を前記誘導加熱装置の出力によって制御する鋼板温度制御装置であって、
前記鋼板の板厚を走間で変更する走間板厚変更を行う場合、
前記粗圧延機の板厚変更動作によって生じる前記鋼板のテーパ部の板厚を計算するテーパ部板厚計算処理と、
目標温度又は目標昇温量を達成するための前記鋼板の板厚と前記誘導加熱装置の出力との関係を規定したマップ又は関数を用いて、前記テーパ部板厚計算処理で計算された前記テーパ部の板厚に基づき、前記テーパ部が前記誘導加熱装置を通過する際の前記誘導加熱装置の出力を計算する誘導加熱装置出力計算処理と、を実行し、
前記誘導加熱装置出力計算処理では、前記テーパ部の開始点の板厚に応じた前記誘導加熱装置の出力から、前記テーパ部の終了点の板厚に応じた前記誘導加熱装置の出力へ、前記誘導加熱装置の出力を段階的に変化させる
ことを特徴とする熱間エンドレス圧延ラインの鋼板温度制御装置。
A steel plate temperature control device that controls the temperature of a steel sheet entering the finish rolling mill by the output of the induction heating device in a hot endless rolling line in which steel sheets flow in the order of a rough rolling mill, an induction heating device, and a finish rolling mill. ,
When changing the inter-run plate thickness to change the plate thickness of the steel plate between runs
Tapered portion plate thickness calculation processing for calculating the plate thickness of the tapered portion of the steel plate caused by the plate thickness changing operation of the rough rolling mill, and
The taper calculated by the taper plate thickness calculation process using a map or function that defines the relationship between the plate thickness of the steel plate and the output of the induction heating device for achieving the target temperature or the target temperature rise amount. Based on the plate thickness of the portion, the induction heating device output calculation process for calculating the output of the induction heating device when the tapered portion passes through the induction heating device is executed .
In the induction heating device output calculation process, the output of the induction heating device according to the plate thickness at the start point of the tapered portion is changed to the output of the induction heating device according to the plate thickness at the end point of the tapered portion. A steel plate temperature control device for a hot endless rolling line, characterized in that the output of an induction heating device is changed stepwise.
粗圧延機、誘導加熱装置、仕上げ圧延機の順に鋼板が流れる熱間エンドレス圧延ラインにおいて、前記仕上げ圧延機に入る前記鋼板の温度を前記誘導加熱装置の出力によって制御する鋼板温度制御装置であって、
前記鋼板の板厚を走間で変更する走間板厚変更を行う場合、
前記粗圧延機の板厚変更動作によって生じる前記鋼板のテーパ部の板厚を計算するテーパ部板厚計算処理と、
目標温度又は目標昇温量を達成するための前記鋼板の板厚と前記誘導加熱装置の出力との関係を規定したマップ又は関数を用いて、前記テーパ部板厚計算処理で計算された前記テーパ部の板厚に基づき、前記テーパ部が前記誘導加熱装置を通過する際の前記誘導加熱装置の出力を計算する誘導加熱装置出力計算処理と、を実行し、
前記誘導加熱装置出力計算処理では、前記誘導加熱装置の上流側に設置した温度計から前記鋼板の入側実績温度又は入側実績昇温量を収集し、前記マップ又は前記関数の前提となる前記鋼板の入側計画温度又は入側計画昇温量と前記入側実績温度又は前記入側実績昇温量との偏差に応じて前記誘導加熱装置の出力を補正する
ことを特徴とする熱間エンドレス圧延ラインの鋼板温度制御装置。
A steel plate temperature control device that controls the temperature of a steel sheet entering the finish rolling mill by the output of the induction heating device in a hot endless rolling line in which steel sheets flow in the order of a rough rolling mill, an induction heating device, and a finish rolling mill. ,
When changing the inter-run plate thickness to change the plate thickness of the steel plate between runs
Tapered portion plate thickness calculation processing for calculating the plate thickness of the tapered portion of the steel plate caused by the plate thickness changing operation of the rough rolling mill, and
The taper calculated by the taper plate thickness calculation process using a map or function that defines the relationship between the plate thickness of the steel plate and the output of the induction heating device for achieving the target temperature or the target temperature rise amount. Based on the plate thickness of the portion, the induction heating device output calculation process for calculating the output of the induction heating device when the tapered portion passes through the induction heating device is executed .
In the induction heating device output calculation process, the incoming side actual temperature or the incoming side actual temperature rise amount of the steel sheet is collected from the thermometer installed on the upstream side of the induction heating device, and the map or the function as a premise of the above. The feature is that the output of the induction heating device is corrected according to the deviation between the planned entry-side temperature or the planned entry-side temperature rise of the steel sheet and the actual entry-side temperature or the actual entry-side temperature rise. Steel plate temperature control device for hot endless rolling lines.
粗圧延機、誘導加熱装置、仕上げ圧延機の順に鋼板が流れる熱間エンドレス圧延ラインにおいて、前記仕上げ圧延機に入る前記鋼板の温度を前記誘導加熱装置の出力によって制御する鋼板温度制御装置であって、
前記鋼板の板厚を走間で変更する走間板厚変更を行う場合、
前記粗圧延機の板厚変更動作によって生じる前記鋼板のテーパ部の板厚を計算するテーパ部板厚計算処理と、
目標温度又は目標昇温量を達成するための前記鋼板の板厚と前記誘導加熱装置の出力との関係を規定したマップ又は関数を用いて、前記テーパ部板厚計算処理で計算された前記テーパ部の板厚に基づき、前記テーパ部が前記誘導加熱装置を通過する際の前記誘導加熱装置の出力を計算する誘導加熱装置出力計算処理と、を実行し、
前記誘導加熱装置出力計算処理では、前記誘導加熱装置の下流側に設置した温度計から前記鋼板の出側実績温度又は出側実績昇温量を収集し、前記目標温度又は前記目標昇温量と前記出側実績温度又は前記出側実績昇温量との偏差に応じて前記誘導加熱装置の出力を補正する
ことを特徴とする熱間エンドレス圧延ラインの鋼板温度制御装置。
A steel plate temperature control device that controls the temperature of a steel sheet entering the finish rolling mill by the output of the induction heating device in a hot endless rolling line in which steel sheets flow in the order of a rough rolling mill, an induction heating device, and a finish rolling mill. ,
When changing the inter-run plate thickness to change the plate thickness of the steel plate between runs
Tapered portion plate thickness calculation processing for calculating the plate thickness of the tapered portion of the steel plate caused by the plate thickness changing operation of the rough rolling mill, and
The taper calculated by the taper plate thickness calculation process using a map or function that defines the relationship between the plate thickness of the steel plate and the output of the induction heating device for achieving the target temperature or the target temperature rise amount. Based on the plate thickness of the portion, the induction heating device output calculation process for calculating the output of the induction heating device when the tapered portion passes through the induction heating device is executed .
In the induction heating device output calculation process, the actual temperature on the exit side or the actual temperature rise on the exit side of the steel plate is collected from a thermometer installed on the downstream side of the induction heating device, and is combined with the target temperature or the target temperature rise amount. A steel plate temperature control device for a hot endless rolling line, characterized in that the output of the induction heating device is corrected according to a deviation from the actual output side temperature or the actual temperature rise on the output side.
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