JPH032931B2 - - Google Patents

Info

Publication number
JPH032931B2
JPH032931B2 JP9919982A JP9919982A JPH032931B2 JP H032931 B2 JPH032931 B2 JP H032931B2 JP 9919982 A JP9919982 A JP 9919982A JP 9919982 A JP9919982 A JP 9919982A JP H032931 B2 JPH032931 B2 JP H032931B2
Authority
JP
Japan
Prior art keywords
furnace
zone
temperature
charge
heating
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.)
Expired
Application number
JP9919982A
Other languages
Japanese (ja)
Other versions
JPS58217631A (en
Inventor
Kenji Doi
Koji Katsura
Haruyoshi Kumayama
Shinya Tanifuji
Shinji Hori
Shoji Nishichi
Juichi Tokunaga
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Kobe Steel Ltd
Original Assignee
Hitachi Ltd
Kobe Steel Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd, Kobe Steel Ltd filed Critical Hitachi Ltd
Priority to JP9919982A priority Critical patent/JPS58217631A/en
Publication of JPS58217631A publication Critical patent/JPS58217631A/en
Publication of JPH032931B2 publication Critical patent/JPH032931B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D11/00Process control or regulation for heat treatments

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Control Of Combustion (AREA)
  • Control Of Heat Treatment Processes (AREA)
  • Regulation And Control Of Combustion (AREA)

Description

【発明の詳細な説明】 本発明は加熱炉の制御方法に関する。[Detailed description of the invention] The present invention relates to a method for controlling a heating furnace.

半バツチ式多帯式加熱炉は連続鋳造機の下流の
設備として配置され、連続鋳造機より製造された
鋼片の8本〜10本を1チヤージとして加熱炉へ装
入される。装入されたチヤージは各炉帯毎に、独
立に移動可能なウオーキングビームにより移動
し、各炉帯で加熱され抽出予定時刻までに焼上げ
られる。
The semi-batch type multi-zone heating furnace is arranged as equipment downstream of the continuous casting machine, and 8 to 10 pieces of steel produced by the continuous casting machine are charged into the heating furnace as one charge. The charged charge is moved to each furnace zone by an independently movable walking beam, heated in each furnace zone, and baked by the scheduled extraction time.

第1図に半バツチ式多帯式加熱炉の構造を示
す。炉帯は全部で10帯で装入帯、第1加熱帯、第
2加熱帯、第3加熱帯、均熱帯の各上下帯であ
る。一般の連続式加熱炉と異なる点は、装入され
たチヤージを下流帯のチヤージの存在しない炉帯
まで移動させ、その時点から鋼片の加熱が始まる
ことである。これは連続鋳造機から送られるチヤ
ージが連続鋳造機の生産能力や製造鋼種により連
続式加熱炉のように投入ピツチが連続とならない
ためである。操業状況は特開昭56−96031に詳し
い。
Figure 1 shows the structure of a semi-batch type multi-zone heating furnace. There are 10 furnace zones in total: charging zone, first heating zone, second heating zone, third heating zone, and upper and lower zones of soaking zone. The difference from a general continuous heating furnace is that the charged charge is moved to a furnace zone in the downstream zone where no charge exists, and heating of the steel billet begins from that point. This is because the charge sent from the continuous casting machine is not continuous as in a continuous heating furnace, depending on the production capacity of the continuous casting machine and the type of steel manufactured. The operational status is detailed in JP-A-56-96031.

第2図に均熱帯のチヤージが抽出完了後、第3
加熱帯のチヤージが移動開始し均熱帯へ進入中の
炉内実績温度と投入燃料流量の関係を示す。チヤ
ージが炉帯内で停止している間の加熱炉制御は一
般の連続式加熱炉と同様、一定時間周期で鋼片の
加熱パターンに従つてチヤージ内の各鋼片毎に一
定時間後の加熱予測を行ない、制御炉帯の現在炉
内雰囲気温度を基準に設定値を決定し制御系に対
して炉温設定値を出力する制御方式とする。しか
し第2図のようにチヤージが次帯へ進入中(炉帯
間の移動中)はチヤージの鋼片温度が進入炉帯の
雰囲気温度に比べかなり低いため炉温が急激に低
下し始める。従つて加熱パターンによる炉温設定
による制御では一定周期による炉温設定温である
ため、実績炉温を下げる方向への制御を行なつて
いる場合、次の設定値出力のタイミングまでの間
で設定値>実績炉温の関係が発生する。そこでそ
れまで燃料流量を下げていた制御系としては逆に
燃料流量を上げる方向に動作する。さらに次のタ
イミングで設定値を現在炉温より下げる方向へ出
力しても同様の現象が発生し制御はハンチング
し、黒煙発生の原因となる。そして、炉温がほぼ
一定値に落ちついたタイミングでは設定燃料はか
なり高い値で保持することになりチヤージが炉帯
間を移動し炉温が急激に下降している間の燃料が
無駄になるといつた問題点が発生する。
Figure 2 shows the third stage after the charging in the soaking zone has completed extraction.
The relationship between the actual temperature inside the furnace and the flow rate of the input fuel is shown when the charge in the heating zone begins to move and enters the soaking zone. The heating furnace control while the charge is stopped in the furnace zone is similar to a general continuous heating furnace, in which each billet in the charge is heated after a fixed period of time according to the heating pattern of the billet at a fixed time period. The control method is to make a prediction, determine the set value based on the current furnace atmosphere temperature of the controlled furnace zone, and output the furnace temperature set value to the control system. However, as shown in FIG. 2, while the charge is advancing to the next zone (while moving between furnace zones), the temperature of the steel billet in the charge is considerably lower than the ambient temperature of the furnace zone into which it enters, so the furnace temperature begins to drop rapidly. Therefore, in the control by setting the furnace temperature using a heating pattern, the furnace temperature is set at a fixed period, so when controlling to lower the actual furnace temperature, the setting is performed until the timing of the next set value output. A relationship of value > actual furnace temperature occurs. Therefore, the control system, which had previously been lowering the fuel flow rate, operates in the opposite direction to increase the fuel flow rate. Furthermore, even if the set value is output in a direction lower than the current furnace temperature at the next timing, a similar phenomenon will occur and the control will be hunting, causing black smoke to be generated. Then, when the furnace temperature has settled down to an almost constant value, the set fuel is held at a fairly high value. However, other problems may occur.

本発明の目的は炉帯間をチヤージが移動中に、
炉内温度の急激な下降現象に対して、炉温設定方
式による投入燃料の無駄を、燃料流量設定方式に
より、最適な加熱炉制御と成る加熱炉の制御方法
を提供することにある。
The object of the present invention is to
It is an object of the present invention to provide a method for controlling a heating furnace, which achieves optimum heating furnace control by using a fuel flow rate setting method, while eliminating waste of input fuel by using a furnace temperature setting method, in response to a phenomenon in which the temperature inside the furnace rapidly decreases.

即ち、本発明は鋼片を複数本のまとまつた単位
で各炉帯毎に加熱を行ない、加熱後チヤージ単位
に抽出し、当該抽出完了後、後続チヤージが次の
炉帯へ移動する半バツチ的多帯式加熱炉の温度、
燃料流量制御方法においてチヤージが炉帯内に停
止している間は各々の鋼片の加熱パターンに従つ
てチヤージ単位の温度予測により設定温度を決定
し炉内雰囲気温度を制御し、チヤージが次の炉帯
へ移動している間は各々の鋼片の加熱パターンと
は無関係にある一定時間毎、投入燃料を目標抽出
温度と抽出までの在炉時間より決定し各炉帯の燃
料流量を制御することを特徴とする半バツチ的多
帯式加熱炉の温度、燃料流量の制御方法に存す
る。
That is, the present invention heats a plurality of steel billets in each furnace zone, extracts them into charge units after heating, and after the completion of the extraction, the subsequent charge moves to the next furnace zone. Temperature of multi-zone heating furnace,
In the fuel flow control method, while the charge is stopped in the furnace zone, the set temperature is determined by temperature prediction for each charge according to the heating pattern of each billet, and the atmosphere temperature in the furnace is controlled. While moving to the furnace zone, the input fuel is determined at fixed time intervals, regardless of the heating pattern of each billet, based on the target extraction temperature and the time in the furnace until extraction, and the fuel flow rate in each furnace zone is controlled. A method for controlling the temperature and fuel flow rate of a semi-batch multi-zone heating furnace is provided.

本発明はチヤージが炉帯間を移動中に発生する
炉温の急激な下降量と一定値に落つくまでに要す
る進入開始からの時間を把握することによりチヤ
ージが移動開始したタイミングより炉温が一定値
に落つくまでをチヤージの移動中と判断しその間
は鋼片の加熱パターンとは無関係に制御系に対し
て燃料流量による設定方式にて制御するものであ
る。この関係を第3図に示す。一定周期でのタイ
ミングで抽出目標温度と現在の鋼片温度との差
θr、残在炉時間Trより決定される燃料流量設定値
Vsを計算し制御系に出力する。この制御を炉温
が落つくまで繰返す。但し燃料流量設定値Vs
炉帯により決めた下限値Vnio以下となる場合は下
限値で保持する。
The present invention enables the furnace temperature to be lowered from the timing when the charge starts moving by understanding the amount of sudden decrease in furnace temperature that occurs while the charge is moving between furnace zones and the time required from the start of approach until it reaches a constant value. It is determined that the charge is moving until it reaches a certain value, and during that time, the control system is controlled by setting the fuel flow rate regardless of the heating pattern of the steel billet. This relationship is shown in FIG. The fuel flow rate set value is determined from the difference θ r between the extraction target temperature and the current billet temperature at a certain periodic timing, and the remaining furnace time T r
Calculate V s and output to the control system. This control is repeated until the furnace temperature drops. However, if the fuel flow rate set value V s is less than the lower limit value V nio determined by the furnace zone, it is held at the lower limit value.

第4図に本発明による具体例を示す。 FIG. 4 shows a specific example according to the present invention.

101はウオーキングビームによる移動信号
で、104は移動状況判定装置である。ウオーキ
ングビーム移動信号は1ピツチ移動タイミング毎
に移動状況判定装置104へ入力され各帯の先頭
に在荷する鋼片の鋼片番号と炉内位置の変化を監
視しチヤージが移動中は停止中かを判断しその結
果を移動状況記憶装置105へ記憶する。107
は設定値計算装置で一定周期でタイマー106に
より動作し、移動状況判定SW(スイツチ)10
8は移動状況記憶装置105の状態により切換え
られる。移動状況判定SW108が停止中の場合
は炉温設定値計算装置109が動作し加熱パター
ンに従つた加熱予測により設定炉温TSを制御系
へ出力する。
101 is a movement signal from a walking beam, and 104 is a movement status determining device. The walking beam movement signal is input to the movement status determination device 104 at each pitch movement timing, and changes in the billet number and the position in the furnace of the steel billet at the beginning of each band are monitored, and it is checked whether the charge is stopped while the charge is moving or not. is determined and the result is stored in the movement status storage device 105. 107
is a set value calculation device that is operated by a timer 106 at regular intervals, and is operated by a movement status judgment SW (switch) 10.
8 is switched depending on the state of the movement status storage device 105. When the movement status determination SW 108 is stopped, the furnace temperature set value calculation device 109 operates and outputs the set furnace temperature TS to the control system by heating prediction according to the heating pattern.

ここで TS=Tp+ΔTs …(1) ΔTs:加熱パターンによる現在炉温からの炉温
変動巾 Tp:現在実績炉温(炉温検出器3より入力) 移動状況判定SW108が移動中の場合は燃料
流量設定値計算装置110が動作し抽出目標温度
と現在鋼片温度の差θrと、残在炉時間Tr、炉帯に
より決まる定数Aにより燃料流量設定値Vsを計
算し制御系へ出力する。
Here, TS=T p +ΔT s …(1) ΔT s : Range of furnace temperature fluctuation from the current furnace temperature due to heating pattern T p : Current actual furnace temperature (input from furnace temperature detector 3) Movement status judgment SW 108 is moving In this case, the fuel flow rate set value calculation device 110 operates and calculates the fuel flow rate set value V s based on the difference θ r between the extraction target temperature and the current billet temperature, the remaining furnace time T r , and a constant A determined by the furnace zone. Output to control system.

ここで VS=A・θr/Tr …(2) 但し VS<Vnio …(3) の場合は VS=Vnio …(4) を燃料流量設定値とすることによりチヤージが炉
帯間を移動中の最適な加熱炉制御を可能とする。
Here, VS=A・θ r /T r …(2) However, if VS<V nio …(3), by setting VS=V nio …(4) as the fuel flow rate setting value, the charge can be adjusted between the furnace zones. Enables optimal heating furnace control while moving.

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

第1図は半バツチ的多帯式加熱炉の構造とチヤ
ージの在荷例を示す図、第2図は炉温設定値方式
によるチヤージが炉帯間を移動中の燃料流量と炉
温との関係図、第3図は燃料流量設定方式による
炉温と燃料流量の関係図、第4図はチヤージが移
動中の燃料流量設定方式と炉温設定方式による具
体例のブロツク図を示す。 1…装入帯ウオーキングビーム、2…第1加熱
帯ウオーキングビーム、3…第2加熱帯ウオーキ
ングビーム、4…第3加熱帯ウオーキングビー
ム、5…均熱帯ウオーキングビーム、6…鋼片、
7…装入機、8…抽出機、9…第1加熱帯バーナ
ー、10…第2加熱帯バーナー、11…第3加熱
帯バーナー、12…均熱帯バーナー、102…燃
料流量検出器、103…炉温検出器。
Figure 1 shows the structure of a semi-batch multi-zone heating furnace and an example of charge inventory, and Figure 2 shows the relationship between the fuel flow rate and furnace temperature when the charge is moving between furnace zones using the furnace temperature setpoint method. FIG. 3 is a diagram showing the relationship between the furnace temperature and fuel flow rate according to the fuel flow rate setting method, and FIG. 4 is a block diagram of a concrete example of the fuel flow rate setting method and the furnace temperature setting method when the charge is moving. 1... Charging zone walking beam, 2... First heating zone walking beam, 3... Second heating zone walking beam, 4... Third heating zone walking beam, 5... Soaking zone walking beam, 6... Steel billet,
7... Charging machine, 8... Extraction machine, 9... First heating zone burner, 10... Second heating zone burner, 11... Third heating zone burner, 12... Soaking zone burner, 102... Fuel flow rate detector, 103... Furnace temperature detector.

Claims (1)

【特許請求の範囲】[Claims] 1 鋼片を複数本のまとまつたチヤージ単位で各
炉帯毎に加熱を行ない、加熱後に前記チヤージ単
位に抽出して次の炉帯へ移動させるようにした半
バツチ式多帯式加熱炉の制御方法において、前記
チヤージ単位が炉帯内に停止している間は各々の
鋼片の加熱パターンに従つて前記チヤージ単位の
温度予測により設定温度を決定し炉内雰囲気温度
を制御し、前記チヤージ単位が次の炉帯へ移動し
ている間は、一定時間毎に当該チヤージの次の炉
帯からの抽出目標温度と現在の鋼片温度の温度差
および当該チヤージの次の炉帯での在炉時間に基
づき前記次の炉帯の投入燃料を求め、前記次の炉
帯の投入燃料を制御するようにしたことを特徴と
する加熱炉制御方法。
1. Control of a semi-batch type multi-zone heating furnace in which steel slabs are heated in each furnace zone in a plurality of charge units, and after heating, they are extracted into the charge units and transferred to the next furnace zone. In the method, while the charge unit is stopped in the furnace zone, a set temperature is determined by predicting the temperature of the charge unit according to the heating pattern of each billet, and the atmosphere temperature in the furnace is controlled; While the charge is moving to the next furnace zone, the temperature difference between the extraction target temperature from the next furnace zone of the charge and the current billet temperature and the temperature difference of the current billet temperature in the next furnace zone of the charge are calculated at regular intervals. A heating furnace control method, characterized in that the fuel input to the next furnace zone is determined based on time, and the fuel input to the next furnace zone is controlled.
JP9919982A 1982-06-11 1982-06-11 Control of heating furnace Granted JPS58217631A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9919982A JPS58217631A (en) 1982-06-11 1982-06-11 Control of heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9919982A JPS58217631A (en) 1982-06-11 1982-06-11 Control of heating furnace

Publications (2)

Publication Number Publication Date
JPS58217631A JPS58217631A (en) 1983-12-17
JPH032931B2 true JPH032931B2 (en) 1991-01-17

Family

ID=14240974

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9919982A Granted JPS58217631A (en) 1982-06-11 1982-06-11 Control of heating furnace

Country Status (1)

Country Link
JP (1) JPS58217631A (en)

Also Published As

Publication number Publication date
JPS58217631A (en) 1983-12-17

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