JPH0379727A - Method for controlling steel temperature in continuous annealing - Google Patents

Method for controlling steel temperature in continuous annealing

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Publication number
JPH0379727A
JPH0379727A JP21658089A JP21658089A JPH0379727A JP H0379727 A JPH0379727 A JP H0379727A JP 21658089 A JP21658089 A JP 21658089A JP 21658089 A JP21658089 A JP 21658089A JP H0379727 A JPH0379727 A JP H0379727A
Authority
JP
Japan
Prior art keywords
temperature
cooling
steel material
steel
transformation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP21658089A
Other languages
Japanese (ja)
Inventor
Kazuhiro Yahiro
和広 八尋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP21658089A priority Critical patent/JPH0379727A/en
Publication of JPH0379727A publication Critical patent/JPH0379727A/en
Pending legal-status Critical Current

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  • Control Of Heat Treatment Processes (AREA)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Abstract

PURPOSE:To reduce errors in the estimated steel temp., to accurately regulate the cooling amt. or the like and to obtain a steel of stabilized material with good productivity by controlling the manipulated variable according to the steel temp. estimated by considering the state of progress in the transformation of the steel to be subjected to cooling or the like. CONSTITUTION:In continuous annealing, the amt. of cooling or heating is controlled according to the conditions in cooling or heating of a steel. Then, the steel temp. in a prescribed position on the line or a prescribed time is controlled to a prescribed objective one. At this time, the temp. of the above steel is estimated by a temp. estimated model in consideration of the state of progress in the transformation of the above steel. According to the accumulated steel temp., the above cooling amt. and heating amt. are determined.

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野] 本発明は、連続焼鈍炉の冷却帯又は加熱帯において鋼材
の温度(板温)を高精度に制御する方法に関する。
[Industrial Application Field] The present invention relates to a method of controlling the temperature of a steel material (plate temperature) with high precision in a cooling zone or a heating zone of a continuous annealing furnace.

【従来の技術】[Conventional technology]

連続焼鈍における鋼材の板温の制御については、例えば
、特公昭63−14051に、次のような技術が開示さ
れている。それは、連続焼鈍設備内に設置され、内部に
冷媒を貫流させた1本乃至複数本の冷却用ロールに銅帯
を巻付け、該巻付は長さを変更させる機構を有する銅帯
の冷却装置を制御するに際し、#4−IFの搬送順序、
寸法、物性値を記した作業予定表を記憶し、予め得られ
る関係式から巻付角を計算し、巻付角を変更させる機構
を制御する制御装置を設け、該冷却用ロールの入側に銅
帯温度計、#I4帯の溶接線検出器を設け、該冷却装置
内に鋼帯の張力計、冷媒温度計、銅帯搬送速度計を設け
、溶接線通過本数と作業予定表から認識する通過中の銅
帯の寸法、物性値と冷却用ロール入011s帯温度、銅
帯張力、冷媒温度、銅帯搬送速度とを前記関係式に代入
して鋼帯の冷却用ロールに対する巻付角を定期的に計算
し、その値に基づいて巻付角を変更すると共に、銅帯の
溶接線が冷却用ロールを通過中に巻付角を制御するとい
うものである。この公報には合わせて次のような技術も
開示されている。それは、前記制御装置内の関係式に新
たに該冷却用ロール山開の制御鋼帯目標温度を修正する
式を付加し、最終冷却用ロール出側に銅帯温度計を設け
、該冷却用ロール出側鋼帯温度計からの入力により定期
的に山開の制御#j4帯目標温度を修正し巻付角を再計
算し、銅帯の冷却用ロールに対する巻付角を修正すると
いうものである。 一方、特公昭63−34210には次のような技術が開
示されている。それは、板厚、板幅あるいは加熱炉出口
温度基準の異なるストリップを加熱炉に連続的に通板し
て連続焼鈍を行う連続焼鈍炉における板温制御方法にお
いて、板厚、板幅、あるいは加熱炉出ロストリップ温度
基準(板温基′?$)の変更(セット替)に伴い操作量
としての加熱炉の燃料流量あるいはそれとストリップの
炉内通板速度とを変更して制御量たる加熱炉出ロストリ
ップ温度(板温)を制御するに当たり、初めに炉出口板
温と燃料流量、炉温、板厚、板幅及びストリップの炉内
通板速度との関係を動的に表現する可変未知パラメータ
を含む板温制御モデルを設定し、来たるべき板厚、板幅
あるいは炉出口板温基準の変更(セット替)に対して所
定の評価間数の最小値を与える板温の推移軌道と、スト
リップの炉内通板速度の変更を伴う場合にはその速度変
更量並びに変更開始時期とを上記板温制御モデルに用い
て予め求め、ストリップのセット替位置を絶えずトラッ
キングしながら上記で求めた速度変更開始時期に通板速
度を変更すると共に、板温が推移軌道に向かって推移す
るように燃料流量を所定のサンプリング周期で時々刻々
算出し制御するというものである。ここで、燃料流量の
設定値を求める際には、その設定値は所定の評価関数の
最小値を与える値として、板温制御モデルを用いて算出
されるのがよく、可変未知パラメータは、これを推定し
てもよいと言及されている。 前記特公昭63−14051に開示された技術は、温度
モデル式にて操作量設定し、その誤差をフィードバック
制御で解消するというものである。 一方、前記特公昭63−34210に開示された技術は
、温度モデル式にて操作量を設定し、発生する誤差をパ
ラメータ推定又は学習によって吸収し、モデル精度を高
めるというものである。
Regarding the control of the plate temperature of steel materials during continuous annealing, the following technique is disclosed, for example, in Japanese Patent Publication No. 14051/1983. It is a copper strip cooling device that is installed in a continuous annealing facility, and has a mechanism in which a copper strip is wound around one or more cooling rolls through which a refrigerant flows, and the length of the wrapping is changed. When controlling #4-IF transport order,
A control device is installed on the entry side of the cooling roll, which stores a work schedule that describes dimensions and physical property values, calculates the wrapping angle from a relational expression obtained in advance, and controls a mechanism that changes the wrapping angle. A copper strip thermometer and #I4 zone weld line detector are installed, and a steel strip tension meter, refrigerant thermometer, and copper strip conveyance speed meter are installed in the cooling device, and recognition is made from the number of weld lines passing and the work schedule. By substituting the dimensions and physical property values of the copper strip during passing, the temperature of the 011s zone in the cooling roll, the tension of the copper strip, the refrigerant temperature, and the conveyance speed of the copper strip into the above relational expression, the wrapping angle of the steel strip with respect to the cooling roll can be calculated. The winding angle is calculated periodically and the winding angle is changed based on the calculated value, and the winding angle is controlled while the weld line of the copper strip passes through the cooling roll. This publication also discloses the following technology. It adds a new formula to the relational formula in the control device to correct the target temperature of the control steel strip for the opening of the cooling roll, installs a copper strip thermometer on the exit side of the final cooling roll, and Based on the input from the steel strip thermometer on the exit side, the target temperature of #j4 zone of opening control is periodically corrected, the wrapping angle is recalculated, and the wrapping angle of the copper strip with respect to the cooling roll is corrected. . On the other hand, Japanese Patent Publication No. 63-34210 discloses the following technology. It is a strip temperature control method in a continuous annealing furnace in which strips with different thicknesses, widths, or heating furnace exit temperatures are continuously passed through the heating furnace for continuous annealing. Due to the change (set change) of the output loss strip temperature standard (plate temperature base'? $), the fuel flow rate of the heating furnace as a manipulated variable or the rate of strip passing through the furnace is changed to increase the heating furnace output as a controlled variable. In controlling the loss strip temperature (strip temperature), first variable unknown parameters dynamically express the relationship between the furnace exit strip temperature, fuel flow rate, furnace temperature, strip thickness, strip width, and strip passing speed in the furnace. Set a plate temperature control model including a plate temperature transition trajectory that provides the minimum value of a predetermined number of evaluation intervals for upcoming changes in plate thickness, plate width, or furnace exit plate temperature standards (set change); If the speed at which the strip passes through the furnace is changed, the amount of speed change and the start time of the change are determined in advance using the above plate temperature control model, and the speed determined above is determined while constantly tracking the strip setting position. The sheet passing speed is changed at the change start time, and the fuel flow rate is calculated and controlled from time to time at a predetermined sampling period so that the sheet temperature moves toward a transition trajectory. When determining the set value of the fuel flow rate, the set value is preferably calculated using a plate temperature control model as the value that gives the minimum value of a predetermined evaluation function, and the variable unknown parameter is calculated using this value. It is mentioned that it may be estimated. The technique disclosed in the above-mentioned Japanese Patent Publication No. 14051/1983 sets the manipulated variable using a temperature model formula and eliminates the error using feedback control. On the other hand, the technique disclosed in the above-mentioned Japanese Patent Publication No. 63-34210 sets the manipulated variable using a temperature model formula, absorbs errors that occur through parameter estimation or learning, and improves model accuracy.

【発明が解決しようとする課題】[Problem to be solved by the invention]

しかしながら、鋼材が冷却又は加熱される際、例えば冷
却される場合、第1図に示されるように、鋼材はγ鉄か
らα鉄(例えばオーステナイトからフェライト〉へと変
態し、この時に発熱現象が発生する。この変態による温
度変化は温度モデルの誤差となるが、前述したような従
来の技術では、発生する誤差のフィードバック制御又は
発生した誤差をパラメータ推定又は学習により吸収する
という方法で対応していた。 しかしながら、このような方法では、変態による温度変
化を充分に考慮して温度制御ができず、板温制御精度も
低いものであった。 なお、本出願人は先に特開昭59−110737にて、
連続焼鈍においてこのα/γの相分率を磁気的にモニタ
して熱処理制御を行う技術を提案したが、相変態に伴う
吸/発熟量を考慮した温度制御にまでは至っていなかっ
た。 本発明はこのような従来の問題に鑑みてなされたもので
あって、鋼材の変態状態まで的確に温度推定モデルに反
映させ、以ってより正確な温度制御を行うことのできる
連続焼鈍における鋼材の温度制御方法を提供することを
目的とする。
However, when the steel material is cooled or heated, for example, when it is cooled, the steel material transforms from γ iron to α iron (for example, from austenite to ferrite), and at this time, an exothermic phenomenon occurs. Temperature changes due to this transformation cause errors in the temperature model, but in the conventional technology described above, this was dealt with by feedback control of the generated errors or by absorbing the generated errors through parameter estimation or learning. However, in such a method, the temperature cannot be controlled in sufficient consideration of the temperature change due to transformation, and the plate temperature control accuracy is also low. At,
Although a technology has been proposed in which heat treatment is controlled by magnetically monitoring the α/γ phase fraction during continuous annealing, temperature control that takes into account the amount of absorption/development accompanying phase transformation has not yet been achieved. The present invention has been made in view of such conventional problems, and it provides a steel material for continuous annealing that allows even the transformation state of the steel material to be accurately reflected in the temperature estimation model, thereby enabling more accurate temperature control. The purpose of this invention is to provide a temperature control method.

【課題を解決するための手段] 本発明は、連続焼鈍における鋼材の冷却条件又は加熱条件に応じて冷却量又は加熱量を制御することにより、ライン上の所定位置あるいは所定時間における鋼材の温度を所定の目標温度に制御するようにした連続焼鈍における鋼材の温度制御方法において、冷却又は加熱する鋼材の変態の進行状況を考慮して、冷却又は加熱される鋼材の温度を温度推定モデルによって推定し、推定された鋼材温度に基づき、前記冷却量又は加熱量を決定することにより上記目的を達成したものである。 又、本発明は、前記鋼材の変態の進行状況を考慮するために、該鋼材の変態率の時間変化に応じた変態発熱量の変化を考慮することにより、容易且つ正確に変態の進行状況を考慮できるようにしたものである。 又、本発明は、連続焼鈍ライン内に鋼材の変態率又はオーステナイト量のうち少なくとも一方を検出するセンサを設け、前記温度推定モデルのパラメータを学習補正することにより、−層正確な温度制御ができるようにしたものである。 【作用】[Means to solve the problem] The present invention is capable of controlling the temperature of the steel material at a predetermined position on the line or at a predetermined time to a predetermined target temperature by controlling the amount of cooling or heating according to the cooling conditions or heating conditions of the steel material during continuous annealing. In the temperature control method of steel material during continuous annealing, the temperature of the steel material to be cooled or heated is estimated by a temperature estimation model, taking into account the progress of transformation of the steel material to be cooled or heated, and based on the estimated steel material temperature, The above object is achieved by determining the amount of cooling or heating. Further, in order to consider the progress of transformation of the steel material, the present invention easily and accurately determines the progress of transformation by considering changes in the heat value of transformation according to time changes in the transformation rate of the steel material. This is something that can be taken into consideration. Further, the present invention provides a sensor for detecting at least one of the transformation rate and the amount of austenite of the steel material in the continuous annealing line, and learns and corrects the parameters of the temperature estimation model, thereby enabling accurate temperature control. This is how it was done. [Effect]

本発明においては、連続焼鈍における鋼材の板温を制御
するに当たって、温度制御(冷却又は加熱)さ扛る鋼材
の変態の進行状況を考慮して該鋼材の温度を推定し、推
定温度に基づき操作量を制御する。 従って、鋼材が温度制御される過程における該鋼材の変
態の進行状況を考慮して該鋼材の温度を推定できるため
、冷却・加熱中における実際の鋼材温度に対する推定さ
れる鋼材温度の誤差を大幅に減少し、精度よく冷却量や
加熱量を制御して所望の温度変化量が得られる温度制御
を実行することができる。よって、より安定した材質の
鋼材を高い生産性の下に製造できる。 なお、前記鋼材の変態の進行状況を考慮するのを、該鋼
材の変態率の時間変化に応じた変態発熱量の変化を考慮
することとすれば、変態の進行状況を変態発熱量という
客観的な数量で把握できるため、鋼材温度の推定が容易
となる。 更に、ライン中に鋼材の変態量又はオーステナイト量を
検出するセンサを設け、その実測値と、推定値とを比較
して、変態の進行モデル中の可変パラメータを学習する
ようにすると、変態の進行状況の推定精度を大幅に向上
させることが可能になる。
In the present invention, when controlling the plate temperature of the steel material during continuous annealing, the temperature of the steel material is estimated taking into account the progress of transformation of the steel material that is undergoing temperature control (cooling or heating), and operations are performed based on the estimated temperature. Control quantity. Therefore, the temperature of the steel material can be estimated by taking into account the progress of transformation of the steel material during the process of temperature control, which greatly reduces the error in the estimated steel material temperature from the actual steel material temperature during cooling and heating. It is possible to perform temperature control in which a desired amount of temperature change is obtained by accurately controlling the amount of cooling and heating. Therefore, more stable steel materials can be manufactured with high productivity. In addition, if the progress of transformation of the steel material is considered by considering the change in the transformation calorific value according to the time change of the transformation rate of the steel material, the progress of the transformation can be objectively referred to as the transformation calorific value. It is easy to estimate the temperature of the steel material because it can be determined with a quantitative quantity. Furthermore, if a sensor is installed in the line to detect the amount of transformation or austenite in the steel material, and the actual measured value is compared with the estimated value to learn the variable parameters in the transformation progress model, the progress of transformation can be improved. It becomes possible to significantly improve the accuracy of estimating the situation.

【実施例】【Example】

以下、本発明の実施例を第2図を用いて詳細に説明する
。 この実施例では、ガスジェット冷却帯10とロール冷却
帯12を有した冷却設備を備え、溶接点検出器14等に
より鋼帯1の位置を板温制御装置20の鋼帯トラッキン
グ部22でトラッキングし、鋼帯1に与えられる冷却条
件Coを銅帯位置に従って冷却量決定部24に入力する
ようにしている。 冷却量決定部24では、入力される冷却条件CO(板厚
、板幅、目標板温etc、  )と、板温センサ71〜
73により検出される現在温度の情報から、各冷却帯1
0.12で冷却すべき冷却量を求める。求めた冷却量よ
り、予め与えられる冷却量と操作量との関係に従って、
ガスジェット制御装置30におけるガスジェット冷却帯
10の操作量、対向ガスジェット制御装置40における
対向ガスジェット41.42の操作量、ロール冷却制御
装置50におけるロール冷却帯12の操作量を求める。 この実施例では、冷却量を求める際に、変態発熱量を考
慮するようにしている。又、冷却量を求める際には、制
御モデル中の可変パラメータを、学習制御部26より得
られるようにしている。 学習制御部26では、変態率センサ61.62・・・の
実測値と変態進行モデルの推定値の比較により、変態進
行モデル中の可変パラメータのオンライン推定を行う、
又、この学習制御部26は、温度予測値と板温センサ7
1.72・・・による実測温度の比較により、温度モデ
ル中の可変パラメータをオンライン推定する。 この構成によれば、変!B発熱による外乱を除いて温度
モデル中の可変パラメータを学習できるので、高精度な
温度モデル学習を実施することが可能である。 ガスジェット制御装置30、対向ガスジェット制御装置
40、ロール冷却装置50では、冷却量決定部24で決
定した操作量に応じ、それぞれガスジェット圧力、ダン
パー開度、ロール押込量を制御する。 以下、実施例の作用を説明する。 この実施例においては、冷却設備の冷却量を決定する際
に、鋼帯1の冷却時間及び冷却設備の冷却能力から、所
定時間経過した鋼帯1の温度変化を推定すると同時に、
該鋼帯1の冷却による変態の進行状況から、例えばR帯
1の変態発熱量を算出し、推定される鋼帯1の温度変化
の誤差を、算出された変態発熱量で補正し、補正された
温度変化量が得られるように冷却を制御する。 まず、前記鋼帯1の変態の進行状況の求め方を説明する
。 冷却中の鋼帯1の変態率Wは、冷却時間tの関数として
次式(1)から算出できる。 W=、1− eXi)[A・ (t/B)  ]−(1
)ここで、A、B、Cは鋼帯1の成分、温度、板厚、冷
却速度等によって決定されるパラメータである。 この(1)式で時間に対する鋼帯1中の変態の進行状渇
を知ることができる。ここで、前記所定数の冷却ゾーン
を有する冷却設備において、その入側から第1番目の冷
却ゾーンまでの冷却時間をtiとすれば、該第1番目の
冷却ゾーン内における冷却時間ΔT i (”j i、
  i i−+)と(1)式の関係から、第1番目の冷
却ゾーン内の変態率変化量ΔWi  (=Wi−Wi−
1)を算出できる。 この変態率変化量ΔWiが与えられたときの、第iゾー
ンにおける銅帯の変態発熱量Qyiは、次式(2)によ
って算出できる。 Qyi=HネΔWi         ・・・(2)但
し、Hは鋼帯1の変態潜熱(鋼帯1の成分、鋼種、温度
毎に決定できる物理量)である。 従って、まず、この(2)式によって、鋼帯1を入側温
度から目標温度まで冷却する際の、各冷却ゾーン内にお
ける変態発熱量QTを演算により求め、次いで求められ
た変態発熱量Qviで鋼帯1の冷却時間を及び冷却設備
の能力から推定される鋼帯1の温度変化を補正すれば、
鋼帯1の各冷却ゾーンにおける正確な温度変化を推定す
ることができる。 よって、このようにして推定された温度変化を各冷却ゾ
ーンで実現するように、次式(3)に示す第1番目の冷
却ゾーンにおけるガスジェット冷却時の温度変化量ΔT
 i o、同じく(4)式に示すロール冷却時の温度変
化量ΔT i Rの温度モデル式を用いて各冷却ゾーン
内の必要冷却量を決定する。 これにより、変態発熱量Qyi、ひいては変態の進行状
況を考慮して鋼帯1に所望の温度変化を与えるように冷
却を制御することができる。冷却ゾーンの出側温度θD
は次のようになる。 θ0=θtr++(θE−θtrt )x exp[(
−2XαoXJ2o) /<Cp*ρ*i *v ) ] (2G=3.×Δpa!X2”(3) θ0 :冷却ゾーン出側温度 θtry :変態発熱影響温度 (” Q T i X p X h / a ()+θ
0)θE :冷却ゾーン入側温度 αG =ガスジェット冷却能 J2()  ニガスジエツト冷却長 CP :比熱 ρ  :比重 h  :板厚 ■   ニラインスピード θ0 ニガスジエツト冷媒温度 al、al:係数 ΔP ニガスジエツト圧力と炉圧との差圧 θO=θtr2+(θE−θtr2 )xexp[(K
R−J2*) /(Cp  ・ρ ・h−v)] θtr2=QviXρXh/KR+θR・・・(4) J2R:ロール接触長 KR:ロール冷媒〜ストリップ熱通過 率 θtr2:変態発熱影響温度 θR:ロール冷媒温度 なお、加熱の場合は、式(1)を(5)式に、(2)式
を(6)式に、(3)式を(7)式にそれぞれ変更すれ
ばよい。 w= exp[A’  −(t /B  )  ] =
 (5)A′、B′、C′は銅帯の成分、温度、板厚、
加熱速度の間数として与えられるパラメータである。 Q丁H=−)(*ΔWi         ・・・(6
)θ0=θtr3 +(θE−θtr3)XeXp[−
(2本αi*J!i) / (Cp *ρ*hmV )1・・・(7)θt「3
:変B発熱影響温度 (=QvtXρxh/α I+θI 〉θN :炉温 αi :炉温〜ストリソ1間熱伝達係数ぶI :加熱ゾ
ーン長 (7〉式は(3)式を炉温と銅帯の関係に置き替えてい
る。
Hereinafter, embodiments of the present invention will be described in detail using FIG. 2. In this embodiment, the cooling equipment includes a gas jet cooling zone 10 and a roll cooling zone 12, and the position of the steel strip 1 is tracked by the steel strip tracking unit 22 of the plate temperature control device 20 using a welding point detector 14 or the like. , the cooling condition Co given to the steel strip 1 is inputted to the cooling amount determination unit 24 according to the copper strip position. In the cooling amount determination unit 24, input cooling conditions CO (plate thickness, plate width, target plate temperature, etc.) and plate temperature sensors 71 to
From the current temperature information detected by 73, each cooling zone 1
Calculate the amount of cooling to be performed using 0.12. From the obtained cooling amount, according to the relationship between the cooling amount and the manipulated variable given in advance,
The operation amount of the gas jet cooling zone 10 in the gas jet control device 30, the operation amount of the opposing gas jets 41 and 42 in the opposing gas jet control device 40, and the operation amount of the roll cooling zone 12 in the roll cooling control device 50 are determined. In this embodiment, the amount of heat generated by transformation is taken into consideration when determining the amount of cooling. Further, when determining the cooling amount, variable parameters in the control model are obtained from the learning control section 26. The learning control unit 26 performs online estimation of the variable parameters in the metamorphosis progress model by comparing the actual measured values of the metamorphosis rate sensors 61, 62, and the estimated values of the metamorphosis progress model.
Further, this learning control unit 26 uses the predicted temperature value and the plate temperature sensor 7.
1.72... The variable parameters in the temperature model are estimated online by comparing the measured temperatures. According to this configuration, strange! Since variable parameters in the temperature model can be learned excluding disturbances caused by B heat generation, highly accurate temperature model learning can be performed. The gas jet control device 30, the opposing gas jet control device 40, and the roll cooling device 50 each control the gas jet pressure, the damper opening degree, and the roll pushing amount according to the operation amount determined by the cooling amount determination unit 24. The effects of the embodiment will be explained below. In this embodiment, when determining the cooling amount of the cooling equipment, the temperature change of the steel strip 1 after a predetermined period of time is estimated from the cooling time of the steel strip 1 and the cooling capacity of the cooling equipment, and at the same time,
For example, the transformation calorific value of the R band 1 is calculated from the progress of transformation due to cooling of the steel strip 1, and the error in the estimated temperature change of the steel strip 1 is corrected by the calculated transformation calorific value. Cooling is controlled to obtain the desired temperature change amount. First, a method of determining the progress of transformation of the steel strip 1 will be explained. The transformation rate W of the steel strip 1 during cooling can be calculated from the following equation (1) as a function of the cooling time t. W=,1-eXi)[A・(t/B)]-(1
) Here, A, B, and C are parameters determined by the composition, temperature, plate thickness, cooling rate, etc. of the steel strip 1. From this equation (1), it is possible to know the progress of transformation in the steel strip 1 with respect to time. Here, in the cooling equipment having the predetermined number of cooling zones, if the cooling time from the entrance side to the first cooling zone is ti, then the cooling time in the first cooling zone ΔT i ('' j i,
From the relationship between i i−+) and equation (1), the transformation rate change amount ΔWi (=Wi−Wi−
1) can be calculated. When this transformation rate change amount ΔWi is given, the transformation calorific value Qyi of the copper strip in the i-th zone can be calculated by the following equation (2). Qyi=HneΔWi (2) where H is the latent heat of transformation of the steel strip 1 (a physical quantity that can be determined for each component, steel type, and temperature of the steel strip 1). Therefore, first, the transformation calorific value QT in each cooling zone when cooling the steel strip 1 from the entrance temperature to the target temperature is calculated using equation (2), and then the transformation calorific value Qvi is calculated. If the temperature change of the steel strip 1 estimated from the cooling time of the steel strip 1 and the capacity of the cooling equipment is corrected,
Accurate temperature changes in each cooling zone of the steel strip 1 can be estimated. Therefore, in order to realize the temperature change estimated in this way in each cooling zone, the amount of temperature change ΔT during gas jet cooling in the first cooling zone shown in the following equation (3) is
io, the required cooling amount in each cooling zone is determined using the temperature model equation of the temperature change amount ΔT i R during roll cooling, which is also shown in equation (4). Thereby, cooling can be controlled so as to give a desired temperature change to the steel strip 1 in consideration of the transformation calorific value Qyi and the progress of the transformation. Cooling zone outlet temperature θD
becomes as follows. θ0=θtr++(θE−θtrt)xexp[(
-2XαoXJ2o) /<Cp*ρ*i *v) ] (2G=3.×Δpa! a()+θ
0) θE: Cooling zone entrance temperature αG = Gas jet cooling capacity J2 () Ni-gas jet cooling length CP: Specific heat ρ: Specific gravity h: Plate thickness ■ Ni-line speed θ0 Ni-gas jet refrigerant temperature al, al: Coefficient ΔP Ni-gas jet pressure and furnace pressure Differential pressure θO=θtr2+(θE−θtr2)xexp[(K
R-J2*) /(Cp ・ρ ・h-v)] θtr2=QviXρXh/KR+θR...(4) J2R: Roll contact length KR: Roll refrigerant to strip heat transfer rate θtr2: Transformation heat effect temperature θR: Roll Refrigerant temperature In the case of heating, equation (1) may be changed to equation (5), equation (2) may be changed to equation (6), and equation (3) may be changed to equation (7). w=exp[A'-(t/B)]=
(5) A', B', and C' are the composition, temperature, and thickness of the copper strip;
This is a parameter given as a number between heating rates. Q Ding H=-)(*ΔWi...(6
) θ0=θtr3 + (θE−θtr3)XeXp[−
(2 αi*J!i) / (Cp *ρ*hmV)1...(7) θt"3
: Variable B exothermic influence temperature (=Qvt Replaced by relationship.

【発明の効果】【Effect of the invention】

以上説明した通り、本発明によれば、連続焼鈍炉におけ
る鋼材を冷却又は加熱する際に、該鋼材の変態進行を考
慮して鋼材の温度を正確に推定し、この推定温度に基づ
き鋼材の冷却量あるいは加熱量を決定しているため、実
際の鋼材温度に対する推定温度誤差を大幅に減少させる
ことができ、高精度な鋼材温度制御を実現することがで
きる。従って、安定した材質の鋼材を高い生産性の下で
製造できる等の優れた効果が得られる。
As explained above, according to the present invention, when cooling or heating a steel material in a continuous annealing furnace, the temperature of the steel material is accurately estimated in consideration of the progress of transformation of the steel material, and the steel material is cooled based on this estimated temperature. Since the amount or heating amount is determined, it is possible to significantly reduce the estimated temperature error with respect to the actual steel material temperature, and it is possible to realize highly accurate steel material temperature control. Therefore, excellent effects such as being able to manufacture stable steel materials with high productivity can be obtained.

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

第1図は、本発明の基本原理を説明するための変態現象
による温度変化の様子を示す線図、第2図は、本発明の
実施例に係る鋼連続焼鈍における板温制御システム(冷
却制御システム)を示す概略ブロック図である。 1・・・鋼帯、 10・・・ガスジェット冷却帯、 12・・・ロール冷却帯、 0・・・板温制御装置、 2・・・銅帯トラッキング部、 4・・・冷却量決定部、 6・・・学習制御部、 O・・・ガスジェット制御装置、 0・・・対向ガスジェット制御装置、 O・・・ロール冷却制御装置、 1.62・・・変態率センサ、 1.72・・・板温センサ。
FIG. 1 is a diagram showing the state of temperature change due to the transformation phenomenon to explain the basic principle of the present invention, and FIG. 2 is a diagram showing the plate temperature control system (cooling control FIG. 2 is a schematic block diagram showing the system. DESCRIPTION OF SYMBOLS 1... Steel strip, 10... Gas jet cooling zone, 12... Roll cooling zone, 0... Plate temperature control device, 2... Copper strip tracking part, 4... Cooling amount determination part , 6...Learning control unit, O...Gas jet control device, 0...Opposed gas jet control device, O...Roll cooling control device, 1.62...Transformation rate sensor, 1.72 ...Plate temperature sensor.

Claims (3)

【特許請求の範囲】[Claims] (1)連続焼鈍における鋼材の冷却条件又は加熱条件に
応じて冷却量又は加熱量を制御することにより、ライン
上の所定位置あるいは所定時間における鋼材の温度を所
定の目標温度に制御するようにした連続焼鈍における鋼
材の温度制御方法において、 冷却又は加熱する鋼材の変態の進行状況を考慮して、冷
却又は加熱される鋼材の温度を温度推定モデルによつて
推定し、 推定された鋼材温度に基づき、前記冷却量又は加熱量を
決定することを特徴とする連続焼鈍における鋼材の温度
制御方法。
(1) By controlling the cooling amount or heating amount according to the cooling or heating conditions of the steel material during continuous annealing, the temperature of the steel material at a predetermined position on the line or for a predetermined time is controlled to a predetermined target temperature. In the temperature control method for steel materials during continuous annealing, the temperature of the steel material to be cooled or heated is estimated by a temperature estimation model, taking into account the progress of transformation of the steel material to be cooled or heated, and the temperature of the steel material is estimated based on the estimated steel material temperature. , a method for controlling the temperature of a steel material during continuous annealing, the method comprising determining the amount of cooling or the amount of heating.
(2)前記鋼材の変態の進行状況を考慮するために、該
鋼材の変態率の時間変化に応じた変態発熱量の変化を考
慮することとした請求項1に記載の連続焼鈍における鋼
材の温度制御方法。
(2) The temperature of the steel material during continuous annealing according to claim 1, wherein in order to consider the progress of transformation of the steel material, a change in the transformation calorific value according to a time change in the transformation rate of the steel material is taken into consideration. Control method.
(3)連続焼鈍ライン内に、鋼材の変態率又はオーステ
ナイト量のうち少なくとも一方を検出するセンサを設け
、前記温度推定モデルのパラメータを学習補正すること
とした請求項1又は2のいずれかに記載の連続焼鈍にお
ける鋼材の温度制御方法。
(3) A sensor for detecting at least one of the transformation rate and the amount of austenite of the steel material is provided in the continuous annealing line, and the parameters of the temperature estimation model are learned and corrected. Temperature control method for steel materials during continuous annealing.
JP21658089A 1989-08-23 1989-08-23 Method for controlling steel temperature in continuous annealing Pending JPH0379727A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21658089A JPH0379727A (en) 1989-08-23 1989-08-23 Method for controlling steel temperature in continuous annealing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21658089A JPH0379727A (en) 1989-08-23 1989-08-23 Method for controlling steel temperature in continuous annealing

Publications (1)

Publication Number Publication Date
JPH0379727A true JPH0379727A (en) 1991-04-04

Family

ID=16690644

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21658089A Pending JPH0379727A (en) 1989-08-23 1989-08-23 Method for controlling steel temperature in continuous annealing

Country Status (1)

Country Link
JP (1) JPH0379727A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022055557A (en) * 2020-09-29 2022-04-08 Jfeスチール株式会社 Continuous annealing method for cold-rolled steel sheet

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2022055557A (en) * 2020-09-29 2022-04-08 Jfeスチール株式会社 Continuous annealing method for cold-rolled steel sheet

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