JPH01198431A - Furnace temperature setter for continuous heating furnace - Google Patents

Furnace temperature setter for continuous heating furnace

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Publication number
JPH01198431A
JPH01198431A JP2298788A JP2298788A JPH01198431A JP H01198431 A JPH01198431 A JP H01198431A JP 2298788 A JP2298788 A JP 2298788A JP 2298788 A JP2298788 A JP 2298788A JP H01198431 A JPH01198431 A JP H01198431A
Authority
JP
Japan
Prior art keywords
temperature
furnace
heated
furnace temperature
temp
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
JP2298788A
Other languages
Japanese (ja)
Inventor
Tadashi Kondo
正 近藤
Masakatsu Saito
斉藤 正勝
Hiroshi Ueda
浩 上田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Toa Steel Co Ltd
Original Assignee
Toshiba Corp
Toa Steel Co 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 Toshiba Corp, Toa Steel Co Ltd filed Critical Toshiba Corp
Priority to JP2298788A priority Critical patent/JPH01198431A/en
Publication of JPH01198431A publication Critical patent/JPH01198431A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide the title furnace temp. setter which is capable of controlling temp. with high accuracy without overheating and insufficient heating even if ingots of different burned states coexist in a control zone by constituting the setter in such a manner as to select an optimum computation method according to the distribution state of the target temp. of the ingots and to compute a furnace set temp. CONSTITUTION:The ingots inserted into the continuous heating furnace 1 are heated respectively in different forms in a preheating zone, heating zone and holding zone and are then successively ejected 2. The furnace temps. in the upper and lower parts of the holding zone are detected 3 at this time and the furnace temps. are independently controlled 4 when the furnace temp. setter 10 sets the optimum furnace temp. in accordance with the detected values. The material data such as the size and material quality of the ingots and the process data such as ejection temp. are inputted by an input means 11 and are stored 12 for the purpose of said furnace temp. setting. An ejection signal is applied to an ejection pitch computing means 13 and a temp. computing means 15 at every ejection of the ingots from the furnace 1. The means 13 of the above-mentioned means computes the intended ejection pitch till the specified time by the stored 12 process data.

Description

【発明の詳細な説明】 〔発明の構成〕 (産業上の利用分野) この発明は、スラブまたはビレット等の被加熱材料(以
下、鋼片と言う)を加熱する連続加熱炉に係り、特に、
発熱量を制御するときに制御帯の炉温検出値と突合わせ
る炉温設定値を演算する炉温設定装置に関するものであ
る。
[Detailed Description of the Invention] [Structure of the Invention] (Field of Industrial Application) The present invention relates to a continuous heating furnace for heating a material to be heated (hereinafter referred to as a steel billet) such as a slab or billet, and in particular,
The present invention relates to a furnace temperature setting device that calculates a furnace temperature setting value to be matched with a furnace temperature detection value in a control zone when controlling the calorific value.

(従来の技術) この杜の従来の連続加熱炉として、予熱帯、加熱帯およ
び均熱帯の3つの制御帯を有する後帯式連続加熱炉があ
る。
(Prior Art) KonoMori's conventional continuous heating furnace is a rear zone type continuous heating furnace that has three control zones: a preheating zone, a heating zone, and a soaking zone.

この後帯式連続加熱炉は、制御帯毎に燃料を噴射して燃
焼させるバーナーと、炉温を検出する炉温センサと、こ
の炉温センサによる炉温検出値および炉温設定器等で与
えられる炉温設定値(θ 、  )の偏差を零に近付け
るように制御g   set する制御装置とを有し、各制御帯で独立に温度制御でき
る構成になっている。
This rear zone continuous heating furnace has a burner that injects and burns fuel in each control zone, a furnace temperature sensor that detects the furnace temperature, and a furnace temperature value detected by this furnace temperature sensor and a furnace temperature setting device. It has a control device that controls g set so that the deviation of the furnace temperature set value (θ, ) approached zero, and is configured to be able to independently control the temperature in each control band.

そして、鋼片は予熱帯、加熱帯および均熱帯を順次移動
する間に昇熱され、抽出口において抽出目標温度に到達
するように焼き上げられる。ところでこれらの制御帯に
は複数の鋼片が存在するのが普通であり、さらに、寸法
、材質、抽出目標温度および表面温度制限値等の同じ鋼
片が存在する場合と、異なる鋼片が存在する場合とがあ
る。
Then, the steel slab is heated while sequentially moving through a pre-heating zone, a heating zone, and a soaking zone, and is baked at the extraction port so as to reach the extraction target temperature. By the way, there are usually multiple pieces of steel in these control zones, and there are cases where there are pieces of steel with the same dimensions, material, extraction target temperature, surface temperature limit value, etc., and there are cases where there are pieces of steel with different values. There are cases where it is done.

このうち、寸法、材質、抽出目標温度および表面温度制
限値等の同じ鋼片が存在する場合には、炉温設定値に制
御されるまでの時間遅れを考慮しないと鋼片を抽出目標
温度に焼き上げることができないことがある。
Among these, if there are steel slabs with the same dimensions, material, extraction target temperature, surface temperature limit value, etc., the time delay until the furnace temperature is controlled to the set value is not taken into consideration to bring the steel slabs to the extraction target temperature. Sometimes it is not possible to bake.

一方、鋼片の寸法、材質、抽出目標温度および表面温度
制限値等の値が異なる場合、鋼片を抽出する毎に炉温を
設定し直さななければならず、その設定が適切でないと
、在炉している鋼片を抽出目標温度に焼き上げることが
できなかったり、抽出時に焼は過ぎてしまったりするこ
とがある。
On the other hand, if the dimensions, material, extraction target temperature, surface temperature limit value, etc. of the steel slabs are different, the furnace temperature must be reset every time a steel slab is extracted, and if the settings are not appropriate, It may not be possible to heat the steel pieces in the furnace to the target extraction temperature, or the steel pieces may be overheated during extraction.

そこで、従来は次に示す2つの方法のいずれかで炉温を
設定していた。
Therefore, conventionally, the furnace temperature was set using one of the following two methods.

(a)制御帯に混在している鋼片の中で最も焼は不足の
鋼片に注目してこの鋼片が抽出される時に、抽出目標温
度に到達できるように炉温を設定する。
(a) Among the steel pieces mixed in the control zone, the furnace temperature is set so that the extraction target temperature can be reached when this steel piece is extracted, paying attention to the steel piece that is least fired.

(b)制御帯に混在している鋼片のそれぞれについて、
抽出予定時刻の抽出温度を推定し、この抽出温度推定値
と抽出目標温度との偏差の合計または温度偏差の自乗合
計を最小にするように、現在時刻から抽出されるまでの
各鋼片の炉温を設定する。
(b) For each piece of steel mixed in the control zone,
The extraction temperature at the scheduled extraction time is estimated, and each billet is heated in the furnace from the current time until it is extracted, so as to minimize the sum of the deviations between this estimated extraction temperature value and the extraction target temperature, or the sum of the squares of the temperature deviations. Set the temperature.

(発明が解決しようとする課8) 上述した2つの炉温設定方法のうち、(a)に示した方
法を採用すると、他と比べて極端に焼は不足の鋼片が存
在した場合、この鋼片に先行する鋼片および続行する鋼
片の多くが抽出目標温度よりもかなり高く焼き上げられ
てしまうという間龜点があった。
(Issue 8 to be solved by the invention) Of the two furnace temperature setting methods mentioned above, if method (a) is adopted, if there is a steel billet that is extremely under-hardened compared to the others, this There was a lag point where many of the billets preceding and following the billet were baked well above the extraction target temperature.

また、(b)に示した方法を採用すると、同じ制御帯に
存在している鋼片の全部に注目して平均的な炉温設定値
を算出することになり、最も焼は不足の鋼片に対しては
その抽出温度が抽出目標温度よりもかなり低くなること
がある。そして、この温度が、例えば、圧延可能許容抽
出温度よりも低くなった場合には、圧延可能許容抽出温
度に加熱されるまで抽出を延ばさなければならず、いわ
ゆる、加熱炉待ちが発生する。そして、この加熱炉待ち
が発生すると圧延スケジュールが大幅に変更になってし
まうという問題点もあった。
In addition, if the method shown in (b) is adopted, the average furnace temperature setting value will be calculated by paying attention to all the slabs existing in the same control zone, and the slab that is most under-hardened will be calculated. The extraction temperature may be considerably lower than the extraction target temperature. If this temperature becomes lower than the allowable extraction temperature for rolling, for example, the extraction must be delayed until the material is heated to the allowable extraction temperature for rolling, resulting in what is called a waiting period for the heating furnace. There was also the problem that the rolling schedule would be significantly changed if this waiting time for the heating furnace occurred.

この発明は上記の問題点を解決するためになされたもの
で、焼き上がり状態の異なる鋼片が制御帯に混在した場
合でも、焼は過ぎや焼は不足のない高精度の温度制御を
可能にする連続加熱炉の炉温設定装置を得ることを目的
とする。    −〔発明の構成〕 (課題を解決するための手段) この発明に係る連続加熱炉の炉温設定装置は、被加熱材
料の材料データおよび工程データを入力する入力手段と
、これらのデータを記憶させると共に、推定温度データ
を記憶させるメモリと、制御帯における被加熱材料の将
来位置を演算する位置演算手段と、被加熱材料毎々の現
在温度を演算してメモリの推定温度データを逐次更新す
る温度演算手段と、メモリの記憶内容および演算された
将来位置に対応する最適な目標温度を被加熱材料毎に索
引する目標温度曲線索引手段と、この目標温度、被加熱
材料の将来位置およびメモリに記憶されたデータに基づ
いて、重み付き平均化を含めた複数の炉温設定値の演算
方法から最適なものを選択する最適炉温設定値演算方法
選択手段と、最適な重み係数を選択する最適重み係数演
算手段と、選択された最適炉温設定値演算方法に従い、
必要に応じて最適重み係数を用いて制御帯の炉温設定値
を演算する最適炉温設定値演算手段とを備えたものであ
る。
This invention was made to solve the above-mentioned problems, and even when steel slabs with different fired states coexist in the control zone, it is possible to perform high-precision temperature control without overheating or underheating. The purpose of this invention is to obtain a furnace temperature setting device for a continuous heating furnace. - [Structure of the Invention] (Means for Solving the Problems) A furnace temperature setting device for a continuous heating furnace according to the present invention includes an input means for inputting material data and process data of a material to be heated, and a memory for storing these data. and a memory for storing estimated temperature data, a position calculation means for calculating the future position of the heated material in the control zone, and a temperature for calculating the current temperature of each heated material and sequentially updating the estimated temperature data in the memory. a calculation means, a target temperature curve indexing means for indexing the optimum target temperature corresponding to the stored content of the memory and the calculated future position for each material to be heated, and storing the target temperature, the future position of the material to be heated, and the memory in the memory. an optimal furnace temperature set value calculation method selection means for selecting the optimal one from a plurality of furnace temperature set value calculation methods including weighted averaging, based on the calculated data, and an optimal weight for selecting an optimal weighting coefficient. According to the coefficient calculation means and the selected optimum furnace temperature set value calculation method,
and an optimum furnace temperature setting value calculating means for calculating the furnace temperature setting value of the control zone using the optimum weighting coefficient as necessary.

(作 用) 加熱炉の一つの制御帯に存在する鋼片Sが゛、第2図に
示すように、時刻t。にて位置X。に在炉し、時刻t1
にて位置X1に移動したとする。この鋼片Sは、抽出口
に向かう方向の各位置において材料平均温度の目標値を
持っており、この目標値を連ねたものが目標温度曲線A
になっている。
(Function) As shown in FIG. 2, the steel piece S existing in one control zone of the heating furnace is at time t. At position X. is in the furnace at time t1
Suppose that the user moves to position X1 at . This steel piece S has a target value of the material average temperature at each position in the direction toward the extraction port, and the series of these target values is the target temperature curve A.
It has become.

二二で、位置X。における目標温度をT。、位置X1に
おける目標温度をT1とすれば、鋼片Sが位置X。から
位置X1に移動する時間Δt(−1,−18)内で、現
在温度θ。から目標温度Tlまで昇熱させる必要がある
。この温度差Δθ(−T1−θ。)だけ昇熱させるに必
要な炉温θ は、材料の表面温度を用いることによって
次式で演算することができる。
Twenty-two, position X. The target temperature at T. , if the target temperature at position X1 is T1, then the steel piece S is at position X. The current temperature θ within the time Δt (−1, −18) to move from to position X1. It is necessary to raise the temperature from the target temperature Tl. The furnace temperature θ required to raise the temperature by this temperature difference Δθ (-T1-θ) can be calculated by the following equation using the surface temperature of the material.

−273・・曲(1) ただし、 C:比熱(Kcal/Kg ”C) ρ:密度(Kg/Td) b:鋼片の幅(m) σ:ステファンボルッマン定数 ΦCGu ’上部総括熱吸収率 Φ。。1 :下部総括熱吸収率 Δθ :温度偏差(−T1−θo)(”C)Δ :時間
間隔(−tl−to)(hr)θ :炉温(’C) θ :鋼片の上部表面温度(’C) θl :鋼片の下部表面温度(’C) である。
-273...Song (1) Where, C: Specific heat (Kcal/Kg ``C) ρ: Density (Kg/Td) b: Width of steel slab (m) σ: Stefan-Bormann constant ΦCGu ' Upper overall heat absorption Rate Φ..1: Lower overall heat absorption rate Δθ: Temperature deviation (-T1-θo) (''C) Δ: Time interval (-tl-to) (hr) θ: Furnace temperature ('C) θ: Steel slab Upper surface temperature ('C) θl : Lower surface temperature ('C) of the steel piece.

一方、加熱炉の一つの制御帯には、第3図に示すように
、n個の鋼片s1.s2.s3. ・。
On the other hand, in one control zone of the heating furnace, as shown in FIG. 3, n steel pieces s1. s2. s3.・.

S、−1,Snがそれぞれ抽出口から順に離れた位置X
、XX   ・・・、X   、X  に存在し、1 
  2’l      n−1n しかも、これ等の鋼片の抽出予定時刻が各々【1゜12
.13.・・・、1  .1.これ等の鋼片のn−1n 現在温度が各々θ1.θ2.θ3.・・・、θn−“1
゜θ 、これ等の鋼片の目標温度曲線がAであったとす
れば、上記(1)式を用いることによって、それぞれ抽
出目標温度に昇熱するに必要な炉温θ2、。
Positions X where S, -1, and Sn are respectively distant from the extraction port in order
, XX ..., X , X exists, 1
2'l n-1n Furthermore, the scheduled extraction times for these pieces of steel are [1°12
.. 13. ..., 1. 1. The n-1n current temperatures of these steel pieces are respectively θ1. θ2. θ3. ..., θn-“1
゜θ, If the target temperature curve of these steel slabs is A, then by using the above equation (1), the furnace temperature θ2 required to raise the temperature to the extraction target temperature, respectively.

θ  θ  ・・・、θ   θ を演算することがg
2’  g3’    gn−1’  gnできる。
θ θ ..., calculating θ θ is g
2'g3'gn-1' gn can be done.

これらの炉温θ8..θg2’  θ2゛3.・−・、
θ8□−1゜θ が第3図に示すように、抽出口に近い
ものがgn 最も高く、抽出口から遠くなるに従って順に低くなる場
合があったり、第4図に示すように、狭い範囲で僅かに
ばらついたり、あるいはまた、第5図に示すように、抽
出口から遠くなるにしたがって順に低くなるものの、鋼
片S の炉温θ のみgn が飛抜けて高くなったりすることがある。
These furnace temperatures θ8. .. θg2' θ2゛3.・-・、
As shown in Figure 3, θ8□-1゜θ is the highest gn near the extraction port, and it may decrease as the distance from the extraction port increases, or in a narrow range as shown in Figure 4. There may be slight variations, or, as shown in FIG. 5, the furnace temperature θ of the steel slab S may be significantly higher than gn, although it gradually decreases as the distance from the extraction port increases.

本発明は被加熱材料の目標温度と現在温度とを比較して
炉温設定値θ 、  の演算方法を、例g   set えば、次の3つのうちから選択するものである。
The present invention compares the target temperature of the material to be heated with the current temperature and selects a method for calculating the furnace temperature set value θ, for example, from among the following three methods.

(1)炉温θ  θ  θ  ・・・、θ   θ が
gl’  g2’  g3’    gn−1’  g
n第3図に示すように、抽出口に近いものが最も高く、
抽出口から遠くなるに従って順に低くなると予測された
場合には、抽出口側の鋼片S1に注目して、鋼片S1か
ら求めた炉温θ2□を炉温設定値θg’setとする。
(1) Furnace temperature θ θ θ ..., θ θ is gl'g2'g3'gn-1' g
As shown in Figure 3, the one closest to the extraction port has the highest
If it is predicted that the temperature will decrease as the distance from the extraction port increases, focus on the steel slab S1 on the extraction port side, and set the furnace temperature θ2□ obtained from the steel slab S1 as the furnace temperature set value θg'set.

(2)炉温θ8..θg2’  0g3’ ・・・、0
gn−1’  θgnが第4図に示すように、狭い範囲
で僅かにばらついている場合には、全ての鋼片Sl、S
2.S3゜・・・、S   S に注口して、炉温θg
t’  θ8□。
(2) Furnace temperature θ8. .. θg2'0g3' ..., 0
gn-1' If θgn varies slightly in a narrow range as shown in Fig. 4, all steel pieces Sl, S
2. S3゜..., pour into S S and set the furnace temperature θg
t' θ8□.

n−1’n θ  ・・・、θ   θ を重み付き平均化して平g
3’    gn−1’  gn 均炉温1 を求め、この平均炉温1 を炉温設定g 値θ 、  とする。なお、重み付き平均化方法g  
 set の−例としては次の方法があり、これらのいずれかを選
択する。
n-1'n θ ..., θ θ is weighted averaged and the average g
3'gn-1'gn Equal furnace temperature 1 is determined, and this average furnace temperature 1 is set as the furnace temperature setting g value θ. Note that the weighted averaging method g
Examples of set include the following methods, and select one of these methods.

(a) n個の鋼片に対して全て同じ重みをつける。(a) Give the same weight to all n pieces of steel.

(b)抽出口側の鋼片により大きな重みをつける。(b) Add greater weight to the steel piece on the extraction port side.

(c) n個の鋼片の中で、焼は不足の鋼片(材料湿度
が目標温度曲線より低いもの)に対してより大きな重み
をつける。
(c) Among the n pieces of steel, a larger weight is given to the pieces with insufficient tempering (those whose material humidity is lower than the target temperature curve).

(3)炉温θ  θ  θ  ・・・、θ   θ が
gl’  g2° g3’    ・gn−1’  g
n第5図に示すように、抽出口から遠くなるにしたがっ
て順に低くなるものの、鋼片S の炉温θgnのみが飛
抜けて高くなっている場合には、最も焼は不足の鋼片S
 に着目して、炉温θ を炉温段n         
        gn定値θ 、  とする。
(3) Furnace temperature θ θ θ ..., θ θ is gl' g2° g3'・gn-1' g
As shown in Fig. 5, the furnace temperature θgn of the steel slab S is extremely high, although it gradually decreases as the distance from the extraction port increases.
Focusing on the furnace temperature θ, the furnace temperature stage n
Let gn constant value θ, be.

  set このために、先ず、入力手段を介して人力される材料デ
ータおよび工程データをメモリに記憶させる一方、位置
演算手段により鋼片St 、 S2 。
To do this, first, the material data and process data entered manually through the input means are stored in the memory, while the steel pieces St, S2 are set by the position calculation means.

S  ・・・ S  、S のそれぞれの抽出時刻に3
”  n−1n おける制御帯の将来位置を演算する。そして、温度演算
手段により鋼片S1.S2.S3.・・・。
S ... 3 at each extraction time of S and S
The future position of the control zone at ``n-1n'' is calculated.Then, the temperature calculation means is used to calculate the future position of the control band at point S1, S2, S3, etc.

S  、S の各々の現在温度を推定してメモリn−1
n に記憶させる。
The current temperature of each of S and S is estimated and stored in memory n-1.
Store it in n.

次に、目標温度曲線索引手段が鋼片S1.S2゜S  
・・・ S   S の将来位置と、材料デー3”  
n−1’  n りおよび工程データとに基づいて、鋼片の目標温度を索
引すると、最適炉温設定値演算方法選択手段が、目標温
度と現在温度との関係から、重み付き平均化を含めた複
数の炉温設定値の演算方法から最適な方法を選択する。
Next, the target temperature curve indexing means selects the steel piece S1. S2゜S
... Future position of S S and material data 3"
When the target temperature of the steel billet is indexed based on n-1' n and process data, the optimal furnace temperature set value calculation method selection means selects the method including weighted averaging based on the relationship between the target temperature and the current temperature. The optimal method is selected from among multiple methods for calculating the furnace temperature set value.

そして、この最適炉温設定値演算方法選択手段が重み付
き平均化を選択したとき、最適重み係数演算手段が上述
した方法から最適な重み係数を選択する。そこで、最適
炉温設定値演算手段が選択された最適炉温設定値演算方
法に従って、場合によっては最適重み係数をも用いて鋼
片が制御帯から抽出される時の温度を目標温度に一致さ
せる炉温設定値を演算する。
When the optimum furnace temperature setting value calculation method selection means selects weighted averaging, the optimum weighting coefficient calculation means selects the optimum weighting coefficient from the above-mentioned methods. Therefore, the optimum furnace temperature set value calculation means adjusts the temperature at which the billet is extracted from the control zone to the target temperature according to the selected optimum furnace temperature set value calculation method, and in some cases also uses the optimal weighting coefficient. Calculate the furnace temperature set value.

この結果、焼き上がり状態の異なる鋼片が制御帯に混在
した場合でも、焼は過ぎや焼は不足のない高精度の温度
制御が可能になる。
As a result, even if steel slabs with different fired states coexist in the control zone, highly accurate temperature control is possible without over-heating or under-heating.

(実施例) 第1図はこの発明の一実施例の構成を、連続加熱炉の制
御系と併せて示したブロック図である。
(Embodiment) FIG. 1 is a block diagram showing the configuration of an embodiment of the present invention together with a control system for a continuous heating furnace.

同図において、予熱帯、加熱帯および均熱帯の各制御帯
にバーナを備える連続加熱炉1は圧延スケジュールに従
って抽出口より鋼片を抽出する鋼片抽出手段2を備えて
いる。また、各制御帯に対応して、炉温を検出する炉温
センサ3と、バーナの燃料噴射量を調節して炉温を制御
する炉温制御手段4とを備える他に、炉温センサ3の出
力信号および連続加熱炉1の鋼片抽出信号を入力して、
炉温設定値を演算し、鋼片抽出手段2に鋼片補出指令を
、炉温制御手段4に炉温設定信号を与える炉温設定装置
10を備えている。
In the figure, a continuous heating furnace 1 equipped with burners in each control zone of a pre-heating zone, a heating zone, and a soaking zone is equipped with a steel billet extraction means 2 for extracting steel billets from an extraction port according to a rolling schedule. Further, in addition to providing a furnace temperature sensor 3 for detecting the furnace temperature and a furnace temperature control means 4 for controlling the furnace temperature by adjusting the fuel injection amount of the burner, the furnace temperature sensor 3 corresponds to each control zone. Input the output signal of the continuous heating furnace 1 and the billet extraction signal of the continuous heating furnace 1,
A furnace temperature setting device 10 is provided which calculates a furnace temperature set value and gives a steel billet extraction command to the steel billet extraction means 2 and a furnace temperature setting signal to the furnace temperature control means 4.

ここで、炉温設定装置10は鋼片抽出口を有する均熱帯
を制御対象としたもので、鋼片の寸法、材質、表面温度
制限値等の材料データ、および、工程の種類、抽出目標
温度、所要時間等の工程データを入力する入力手段11
と、この入力手段11の入力データを記憶させる他、現
在温度を推定した現在温度データを記憶させるメモリ1
2と、鋼片が連続加熱炉1の均熱帯から抽出されるまで
の抽出予定ピッチを演算する抽出ピッチ演算手段13と
、この抽出予定ピッチを用いて鋼片の将来位置を演算す
る位置演算手段14と、鋼片の現在温度を演算してメモ
リ12の推定温度データを逐次更新する温度演算子段1
5と、鋼片の材質等に対応する目標温度曲線を用いて制
御帯における鋼片の目標温度を索引する目標温度曲線索
引手段16と、鋼片の目標温度の分布状態に応じて最適
な炉温設定値の演算方法を選択する最適炉温設定値演算
方法選択手段17と、最適炉温設定値の演算に用いる最
適重み係数を選択する最適重み係数選択手段18と、選
択された演算方法に従い、制御帯の最適炉温設定値を演
算する最適炉温設定値演算手段19とで構成されている
。
Here, the furnace temperature setting device 10 is intended to control a soaking zone having a steel billet extraction port, and includes material data such as dimensions, material, and surface temperature limit value of the steel billet, type of process, and extraction target temperature. , input means 11 for inputting process data such as required time, etc.
In addition to storing input data of this input means 11, a memory 1 stores current temperature data obtained by estimating the current temperature.
2, an extraction pitch calculation means 13 for calculating the scheduled extraction pitch until the steel billet is extracted from the soaking zone of the continuous heating furnace 1, and a position calculation means for calculating the future position of the steel billet using this scheduled extraction pitch. 14, and a temperature operator stage 1 that calculates the current temperature of the steel billet and sequentially updates the estimated temperature data in the memory 12.
5, a target temperature curve indexing means 16 for indexing the target temperature of the steel slab in the control zone using a target temperature curve corresponding to the material of the steel slab, and an optimum furnace according to the distribution state of the target temperature of the steel slab. The optimum furnace temperature set value calculation method selection means 17 selects the calculation method of the temperature set value, the optimum weight coefficient selection means 18 selects the optimum weighting coefficient to be used for calculating the optimum furnace temperature set value, and selects the optimum furnace temperature set value calculation method according to the selected calculation method. , and an optimum furnace temperature setting value calculation means 19 for calculating the optimum furnace temperature setting value for the control zone.

上記のように構成された本実施例の動作について説明す
る。
The operation of this embodiment configured as described above will be explained.

連続加熱炉1は挿入口から挿入された鋼片を複数の制御
帯、すなわち、予熱帯、加熱帯および均熱帯でそれぞれ
異なる態様で加熱し、加熱し終わった鋼片を鋼片抽出手
段2によって抽出口から順次抽出する。この時、均熱帯
の上部および下部の炉温は炉温センサ3によって検出さ
れ、その検出値に基づいて炉温設定装置10が最適炉温
を設定すると、炉温制御手段4がその炉温設定値に従っ
て炉温を独立に制御する。
The continuous heating furnace 1 heats the steel billets inserted through the insertion port in different ways in a plurality of control zones, that is, a preheating zone, a heating zone, and a soaking zone, and then extracts the heated billets by the billet extraction means 2. Extract sequentially from the extraction port. At this time, the furnace temperature in the upper and lower parts of the soaking zone is detected by the furnace temperature sensor 3, and when the furnace temperature setting device 10 sets the optimum furnace temperature based on the detected value, the furnace temperature control means 4 sets the furnace temperature. Control the furnace temperature independently according to the value.

ここで、炉温設定するために、入力手段11により、鋼
片の寸法、材質、表面温度制限値等の材料データと、工
程の種類、抽出目標温度、所要時間等の工程データを入
力すると、これらのデータがメモリ12に記憶される。
Here, in order to set the furnace temperature, material data such as the dimensions, material, and surface temperature limit value of the steel billet, and process data such as the type of process, extraction target temperature, and required time are inputted using the input means 11. These data are stored in memory 12.

また、連続加熱炉1から鋼片が抽出される毎に、抽出ピ
ッチ演算手段13および温度演算手段15に抽出信号が
加えられるようになっており、このうち、抽出ピッチ演
算手段13はこの抽出信号と、メモリ12に記憶された
工程データとに基づいて、一定時間後までの抽出予定ピ
ッチを演算する。また、位置演算手段14はこの抽出予
定ピッチから求められる抽出予定時刻における鋼片の均
熱帯の将来位置を演算する。
Moreover, every time a steel billet is extracted from the continuous heating furnace 1, an extraction signal is applied to the extraction pitch calculation means 13 and the temperature calculation means 15. Based on this and the process data stored in the memory 12, the pitch to be extracted until after a certain period of time is calculated. Further, the position calculating means 14 calculates the future position of the soaking zone of the steel billet at the scheduled extraction time determined from this scheduled extraction pitch.

一方、温度゛演算手段15においては、連続加熱炉1か
ら得られる抽出信号を受けて、炉温センサ3の炉温検出
値と、過去にこの温度演算手段15で演算してメモリ1
2に記憶させである鋼片の平均温度演算値とから、鋼片
の平均温度を演算、推定し、その結果を再び、メモリ1
2に記憶させる。
On the other hand, the temperature calculating means 15 receives the extracted signal obtained from the continuous heating furnace 1, and stores the detected value of the furnace temperature of the furnace temperature sensor 3 and the memory of the temperature calculated by the temperature calculating means 15 in the past.
The average temperature of the steel slab is calculated and estimated from the average temperature calculation value of the steel slab stored in memory 1.
2.

さらに、目標温度曲線索引手段16においては、位置演
算手段14から得られる鋼片の均熱帯内位置と、メモリ
12から得られる鋼片の材料データから、鋼片の目標温
度を索引する。最適炉温設定値演算方法選択手段17で
は、位置演算手段14から得られる鋼片の均熱帯内位置
と、メモリ12から得られる鋼片の材料データと、目標
温度曲線索引手段16から得られる均熱帯内の目標温度
とから、加熱炉を制御するための炉温設定値の演算方法
を選択する。
Furthermore, the target temperature curve indexing means 16 indexes the target temperature of the steel billet from the position of the steel billet within the soaking zone obtained from the position calculation means 14 and the material data of the steel billet obtained from the memory 12. The optimal furnace temperature setting value calculation method selection means 17 selects the position of the steel billet within the soaking zone obtained from the position calculation means 14, the material data of the steel billet obtained from the memory 12, and the uniformity obtained from the target temperature curve indexing means 16. From the target temperature in the tropics, select a calculation method for the furnace temperature set value for controlling the heating furnace.

また、最適重み係数選択手段18では、炉温設定値の演
算方法として重み付き平均化が選択されたとき、位置演
算手段14から得られる鋼片の加熱炉内の位置と、メモ
リ12から得られる鋼片の材料データとに基づいて、上
述した重み係数を選択する。
Furthermore, when weighted averaging is selected as the calculation method for the furnace temperature set value, the optimal weighting coefficient selection means 18 determines the position of the steel billet in the heating furnace obtained from the position calculation means 14 and the position obtained from the memory 12. The weighting factors described above are selected based on the material data of the steel billet.

次に、最適炉温設定値演算手段19では、メモリ12か
ら得られる材料データおよび現在の推定温度データと、
目標温度曲線索引手段16から得られる鋼片の目標温度
と、最適重み係数選択手段18から得られる重み係数と
、位置演算手段14から得られる鋼片の加熱炉内の位置
とから、上記(1)式を用いて制御帯に存在する鋼片の
焼き上がり状態に最も適した炉温設定値を演算する。
Next, the optimum furnace temperature set value calculation means 19 uses the material data and the current estimated temperature data obtained from the memory 12,
From the target temperature of the steel billet obtained from the target temperature curve indexing means 16, the weighting coefficient obtained from the optimum weighting coefficient selection means 18, and the position of the steel billet in the heating furnace obtained from the position calculation means 14, the above (1) ) is used to calculate the furnace temperature setting most suitable for the fired state of the steel slabs present in the control zone.

このようにして演算された炉温設定値に基りいて炉温制
御手段4が、連続加熱炉1の均熱帯の上部および下部の
炉温を制御する。
Based on the furnace temperature setting value calculated in this manner, the furnace temperature control means 4 controls the furnace temperature of the upper and lower portions of the soaking zone of the continuous heating furnace 1.

かくして、この実施例によれば、均熱帯に混在している
。鋼片の焼き上がり状態等が変化しても、きめの細かい
制御が可能になり、各々の鋼片が抽出されるときに、そ
の鋼片の抽出温度と抽出目標温度との偏差を最小に保つ
ように制御帯の温度を精度よく設定することができる。
Thus, according to this embodiment, they are mixed in the soaking zone. Even if the firing state of the steel billet changes, fine-grained control is possible, and when each billet is extracted, the deviation between the extraction temperature of that steel billet and the extraction target temperature is kept to a minimum. The temperature of the control zone can be set with high precision.

なお、上記実施例では、均熱帯の炉温を制御するための
炉温設定装置10について説明したが、予熱帯から加熱
帯への鋼片の移動、加熱帯から均熱帯への鋼片の移動を
それぞれ予熱帯、加熱帯からの鋼片の抽出と見做すなら
ば予熱帯および加熱帯の温度制御にも適用することがで
きる。
In addition, in the above embodiment, the furnace temperature setting device 10 for controlling the furnace temperature in the soaking zone was explained, but the movement of the steel billet from the preheating zone to the heating zone, and the movement of the steel billet from the heating zone to the soaking zone. If these are regarded as extraction of steel pieces from the preheating zone and heating zone, respectively, it can also be applied to temperature control of the preheating zone and heating zone.

〔発明の効果〕〔Effect of the invention〕

以上の説明によって明らかなように、この発明によれば
、鋼片の目標温度の分布状態に応じて、最適な演算方法
を選択して炉温設定値を演算しているので、焼き上がり
状態の異なる鋼片が制御帯に混在した場合でも、焼は過
ぎや焼は不足のない高精度な温度制御が可能になるとい
う効果がある。
As is clear from the above explanation, according to the present invention, the furnace temperature setting value is calculated by selecting the optimal calculation method according to the distribution state of the target temperature of the steel billet, so that Even if different pieces of steel coexist in the control zone, there is an effect that highly accurate temperature control is possible with no shortage of overheating or hardening.

【図面の簡単な説明】 第1図はこの発明の一実施例の構成を示すブロック図、
第2図乃至第5図は同実施例の原理を説明するために、
鋼片の位置と温度との関係を示す線図である。 10・・・炉温設定装置、11・・・入力手段、12・
・・メモリ、13・・・抽出ピッチ演算手段、14・・
・位置演算手段、15・・・温度演算手段、16・・・
目標温度曲線索引手段、17・・・最適炉温設定値演算
方法選択手段、18・・・最適重み係数選択手段、19
・・・最適炉温設定値演算手段。 出願人代理人  佐  藤  −雄 0:目標温度 X:翁杓温度 第2図 第3図 第4図 第5図
[BRIEF DESCRIPTION OF THE DRAWINGS] FIG. 1 is a block diagram showing the configuration of an embodiment of the present invention.
Figures 2 to 5 are for explaining the principle of the embodiment.
It is a diagram showing the relationship between the position of a steel piece and temperature. 10...furnace temperature setting device, 11...input means, 12.
...Memory, 13...Extraction pitch calculation means, 14...
・Position calculation means, 15...Temperature calculation means, 16...
Target temperature curve indexing means, 17...Optimum furnace temperature setting value calculation method selection means, 18...Optimum weighting coefficient selection means, 19
...optimum furnace temperature set value calculation means. Applicant's representative: Sato -Yu 0: Target temperature

Claims (1)

【特許請求の範囲】 独立して温度制御することができ、且、複数の被加熱材
料を存在させると共に、抽出口方向に順次移動させるこ
とのできる制御帯を有し、この制御帯の炉温の検出値と
設定値との偏差が零になるように発熱量を制御する連続
加熱炉において、次のa項乃至i項の各手段を備えたこ
とを特徴とする連続加熱炉の炉温設定装置。 a、前記被加熱材料の寸法、材質、表面温度制限値等の
材料データ、および、工程の種類、抽出目標温度、所要
時間等の工程データを入力する入力手段。 b、前記被加熱材料の各々の推定温度データを記憶させ
ると共に、前記入力手段によって入力された材料データ
および工程データを記憶させるメモリ。 c、前記メモリに記憶された工程データに基づいて前記
被加熱材料が前記制御帯から抽出されるまでの抽出予定
ピッチを演算する抽出ピッチ演算手段。 d、前記抽出ピッチ演算手段によって演算された抽出予
定ピッチより抽出予定時刻を求め、この抽出予定時刻に
おける前記被加熱材料の前記制御帯内の将来位置を演算
する位置演算手段。 e、前記制御帯の炉温の検出値と、前記メモリに記憶さ
れている推定温度データとに基づいて前記被加熱材料の
各々の現在温度を推定し、前記メモリの推定温度データ
を順次更新する温度演算手段。 f、前記被加熱材料の目標温度曲線を記憶し、前記位置
演算手段によって演算された前記被加熱材料の将来位置
と、前記メモリに記憶された材料データおよび工程デー
タとに基づいて、前記被加熱材料の目標温度を索引する
目標温度曲線索引手段。 g、前記位置演算手段によって演算された前記被加熱材
料の将来位置と、前記メモリに記憶された材料データお
よび推定温度データと、前記目標温度曲線索引手段によ
って索引された目標温度とに基づいて、重み付き平均化
を含めた複数の炉温設定値の演算方法から最適な演算方
法を選択する最適炉温設定値演算方法選択手段。 h、前記最適炉温設定値演算方法選択手段が重み付き平
均化を選択したとき、前記位置演算手段によって演算さ
れた前記被加熱材料の将来位置と、前記メモリに記憶さ
れた材料データとに基づいて、最適な重み係数を選択す
る最適重み係数選択手段。 i、前記位置演算手段によって演算された前記被加熱材
料の加熱炉内の将来位置と、前記メモリに記憶された材
料データと、前記目標温度曲線索引手段によって索引し
た目標温度と、前記最適重み係数選択手段によって選択
された最適重み係数とに基づき、前記最適炉温設定値演
算方法選択手段によって選択された最適炉温設定値演算
方法に従って、前記被加熱材料が前記制御帯から抽出さ
れる時の前記被加熱材料の温度が目標温度に一致するよ
うな前記制御帯の炉温設定値を演算する最適炉温設定値
演算手段。
[Claims] It has a control zone that can independently control the temperature, has a plurality of materials to be heated, and can be moved sequentially toward the extraction port, and has a control zone that can control the temperature of the furnace in this control zone. Furnace temperature setting for a continuous heating furnace in which the calorific value is controlled so that the deviation between the detected value and the set value becomes zero, characterized in that the continuous heating furnace is equipped with each of the means set forth in the following items a to i. Device. a. Input means for inputting material data such as the dimensions, material, and surface temperature limit value of the material to be heated, and process data such as the type of process, extraction target temperature, and required time. b. A memory that stores estimated temperature data for each of the materials to be heated, and also stores material data and process data input by the input means. c. Extraction pitch calculation means for calculating a scheduled extraction pitch until the material to be heated is extracted from the control zone based on the process data stored in the memory. d. Position calculating means for determining a scheduled extraction time from the scheduled extraction pitch calculated by the extraction pitch calculating means and calculating the future position of the material to be heated within the control zone at this scheduled extraction time. e. Estimating the current temperature of each of the materials to be heated based on the detected value of the furnace temperature in the control zone and the estimated temperature data stored in the memory, and sequentially updating the estimated temperature data in the memory. Temperature calculation means. f. storing a target temperature curve of the material to be heated, and based on the future position of the material to be heated calculated by the position calculating means and the material data and process data stored in the memory; Target temperature curve indexing means for indexing the target temperature of the material. g. Based on the future position of the heated material calculated by the position calculation means, the material data and estimated temperature data stored in the memory, and the target temperature indexed by the target temperature curve index means, Optimal furnace temperature set value calculation method selection means for selecting an optimal calculation method from a plurality of furnace temperature set value calculation methods including weighted averaging. h. When the optimal furnace temperature setting value calculation method selection means selects weighted averaging, based on the future position of the material to be heated calculated by the position calculation means and the material data stored in the memory. optimum weighting coefficient selection means for selecting an optimum weighting coefficient; i, the future position of the material to be heated in the heating furnace calculated by the position calculating means, the material data stored in the memory, the target temperature indexed by the target temperature curve indexing means, and the optimum weighting coefficient; When the material to be heated is extracted from the control zone according to the optimal furnace temperature set value calculation method selected by the optimal furnace temperature set value calculation method selection means based on the optimal weighting coefficient selected by the selection means. Optimal furnace temperature set value calculating means for calculating a furnace temperature set value for the control zone such that the temperature of the heated material matches a target temperature.
JP2298788A 1988-02-03 1988-02-03 Furnace temperature setter for continuous heating furnace Pending JPH01198431A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2298788A JPH01198431A (en) 1988-02-03 1988-02-03 Furnace temperature setter for continuous heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2298788A JPH01198431A (en) 1988-02-03 1988-02-03 Furnace temperature setter for continuous heating furnace

Publications (1)

Publication Number Publication Date
JPH01198431A true JPH01198431A (en) 1989-08-10

Family

ID=12097894

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2298788A Pending JPH01198431A (en) 1988-02-03 1988-02-03 Furnace temperature setter for continuous heating furnace

Country Status (1)

Country Link
JP (1) JPH01198431A (en)

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