JPS584412A - Controlling method of continuous heating furnace - Google Patents
Controlling method of continuous heating furnaceInfo
- Publication number
- JPS584412A JPS584412A JP10275981A JP10275981A JPS584412A JP S584412 A JPS584412 A JP S584412A JP 10275981 A JP10275981 A JP 10275981A JP 10275981 A JP10275981 A JP 10275981A JP S584412 A JPS584412 A JP S584412A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- steel material
- temperature
- combustion zone
- value
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000010438 heat treatment Methods 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims description 13
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 138
- 239000010959 steel Substances 0.000 claims abstract description 138
- 238000000605 extraction Methods 0.000 claims abstract description 31
- 239000000463 material Substances 0.000 claims description 104
- 238000002485 combustion reaction Methods 0.000 claims description 69
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical group [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 8
- 229910052802 copper Inorganic materials 0.000 claims description 8
- 239000010949 copper Substances 0.000 claims description 8
- 230000014759 maintenance of location Effects 0.000 claims 2
- 230000002250 progressing effect Effects 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 4
- 238000012546 transfer Methods 0.000 description 12
- 238000004364 calculation method Methods 0.000 description 6
- 238000005096 rolling process Methods 0.000 description 6
- 238000001514 detection method Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000005056 compaction Methods 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000005098 hot rolling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D23/00—Control of temperature
- G05D23/19—Control of temperature characterised by the use of electric means
- G05D23/1927—Control of temperature characterised by the use of electric means using a plurality of sensors
- G05D23/193—Control of temperature characterised by the use of electric means using a plurality of sensors sensing the temperaure in different places in thermal relationship with one or more spaces
- G05D23/1932—Control of temperature characterised by the use of electric means using a plurality of sensors sensing the temperaure in different places in thermal relationship with one or more spaces to control the temperature of a plurality of spaces
- G05D23/1934—Control of temperature characterised by the use of electric means using a plurality of sensors sensing the temperaure in different places in thermal relationship with one or more spaces to control the temperature of a plurality of spaces each space being provided with one sensor acting on one or more control means
Landscapes
- Engineering & Computer Science (AREA)
- Remote Sensing (AREA)
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Automation & Control Theory (AREA)
- Heat Treatments In General, Especially Conveying And Cooling (AREA)
- Control Of Heat Treatment Processes (AREA)
- Control Of Temperature (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は連続加熱炉の制御方法に係9、特に被加熱鋼材
を熱間圧延に最も適した温度に加熱制御することのでき
る連続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 continuous heating furnace, and particularly to a method for controlling a continuous heating furnace that can control the heating of a steel material to be heated to a temperature most suitable for hot rolling.
一般に、多帯式連続加熱炉の操業における各燃焼帯の炉
温制御において最も注目すべき点は、在炉鋼材の寸法、
重量、移動速度(抽出ピッチ)が一定でなく、′シか4
装入銀度や目標とする加熱温度も同じとは限らないとい
う非定常性にある。したがって、省エネルギ上、また鋼
材の品質上最適な加熱条件を満足する操業を行うために
は、この非定常性を定量化し、かつその変動を常時認識
あるいは予測することが必要であシ、それによシ各燃焼
帯の炉温もしくは燃料投入量を制御する方法が望ましい
。In general, the most important points in controlling the furnace temperature of each combustion zone in the operation of a multi-zone continuous heating furnace are the dimensions of the steel in the furnace,
The weight and moving speed (extraction pitch) are not constant, and the
It is unsteady in that the charged silver degree and target heating temperature are not always the same. Therefore, in order to perform operations that satisfy optimal heating conditions in terms of energy conservation and steel quality, it is necessary to quantify this unsteadiness and constantly recognize or predict its fluctuations. It is preferable to use a method that controls the furnace temperature or fuel input amount for each combustion zone.
これに対し、従来性われている一般的方法は、炉内での
鋼材の伝熱計算をもとに伝熱計算モデル式を定め、在炉
する鋼材毎に、現時点における温度を計算し、これと夫
々の残シの在炉時間とから鋼材毎の目標とする抽出温度
なる最小熱量原単位Oヒートパターンを決定し、これに
合せて各燃焼帯の炉温もしくは燃料投入量を決定するも
のである。In contrast, the conventional and general method is to define a heat transfer calculation model formula based on heat transfer calculations of steel materials in the furnace, calculate the current temperature of each steel material in the furnace, and calculate the current temperature of each steel material in the furnace. The target extraction temperature and minimum heat unit O heat pattern for each steel material are determined from the furnace time of each residue, and the furnace temperature or fuel input amount for each combustion zone is determined accordingly. be.
ところが、斯かる方法では、前述の非定常性から、尚該
燃焼帯0加熱負荷の変動すなわち鋼材を所望通り加熱す
るに要する供給熱量の変動が的確に捉えられているtの
ではなく、またモデル式の伝熱係数精度、信頼性が充分
でないという指摘があることによシ、非定常状態に適合
した制御方法とはいえないものである。しかも、鋼材の
寸法、装入温度、目標抽出温度、在炉時間などが鋼材毎
に異なっていることを考慮すれば、通常、炉長方向に3
〜4の燃焼ゾーンしか持たない連続加熱炉Kj+−いて
は、鋼材一枚一枚を予定のスケジュール通シ全てIIA
奥に目標とする温度で抽出することは不可能である。However, due to the above-mentioned unsteadiness, such a method does not accurately capture fluctuations in the combustion zone 0 heating load, that is, fluctuations in the amount of heat supplied to heat the steel material as desired; It has been pointed out that the heat transfer coefficient accuracy and reliability of the equation are not sufficient, so it cannot be said that this is a control method suitable for unsteady conditions. Moreover, considering that the dimensions, charging temperature, target extraction temperature, furnace time, etc. of steel materials differ for each steel material, it is normal to
In a continuous heating furnace Kj+-, which has only ~4 combustion zones, each steel sheet is processed according to the planned schedule.
It is impossible to extract at the target temperature deep inside.
これを実現させる方案としては、鋼材の抽出スケジュー
ルを炉の制御性に追従することができるまで充分低ピツ
チ抽出に落とすか、あるいは、炉を改造して燃焼ゾーン
を炉長方向に細分化し、きめ細く操業を行うことなどが
考えられる。To achieve this, the extraction schedule for steel material can be reduced to a sufficiently low pitch that it can follow the controllability of the furnace, or the furnace can be modified to subdivide the combustion zone along the length of the furnace, resulting in a fine-grained extraction schedule. Possible options include conducting narrower operations.
しかしながら、前者の場合は連続加熱炉の最大特性であ
る高生産性が失われ、圧延機能力との同期が果せず不適
となる欠点がある。また、後者の場合においても、設備
の大規模化に加えて操炉が複雑、困難になるため実現性
に乏しい。However, in the former case, high productivity, which is the greatest characteristic of a continuous heating furnace, is lost, and synchronization with the rolling function cannot be achieved, making it unsuitable. In addition, even in the latter case, it is difficult to implement because the equipment becomes large-scale and the reactor operation becomes complicated and difficult.
このように、従来、連続加熱炉の制御方法として多くの
提案がなされているが、未だ完全に確立された技術には
至っておらず、鋼材の抽出結果は目標に約しある程度の
ばらつきは避けられず、その結果、品質、歩留シの向上
、省エネルギ効果は期待できないものであった。したが
って、従来、鋼材抽出温度のばらつきをいかに小さくシ
、かつ省エネルギ、高生産性を保持するかが問題となっ
ている。この点について、各燃焼帯に位置する鋼材のう
ち、どの鋼材に着目するか−に深く関係するものである
が、近年種々提案されている連続加熱炉の制御方法では
、充分評価、検討されていないとζろである。In this way, many proposals have been made for control methods for continuous heating furnaces, but the technology has not yet been completely established, and it is difficult to achieve a certain degree of variation in the extraction results of steel materials. As a result, improvements in quality, yield, and energy savings could not be expected. Therefore, conventionally, the problem has been how to reduce variations in steel material extraction temperature while maintaining energy savings and high productivity. This point is deeply related to which steel material to focus on among the steel materials located in each combustion zone, but the control methods for continuous heating furnaces that have been proposed in recent years have not been sufficiently evaluated and studied. If you don't have it, you'll be disappointed.
本発明は上記問題点に着目し、連続加熱炉の有する非定
常性という観点から、制御対象とする燃焼帯の対象鋼材
(群)を明確にするとともに、その非定常性を定量化し
て尚該燃焼帯の炉温制御をなし、最適加熱条件を満足す
る操業を行うことを可能KL、もって省エネルギ上およ
び品質上最適な加熱条件に制御する連続加熱炉の制御方
法を提供することを目的とする。The present invention focuses on the above-mentioned problems, and from the viewpoint of the unsteady nature of continuous heating furnaces, it clarifies the target steel material(s) in the combustion zone to be controlled, quantifies the unsteady nature, and The purpose of the present invention is to provide a continuous heating furnace control method that controls the furnace temperature in the combustion zone and allows operation to satisfy optimal heating conditions. do.
上記目的を達成するために、本発明に係る連続加熱炉の
制御方法は、各燃焼帯毎にこの入口付近に位置する大単
位の鋼材群と、それらよシ鋼材進行方向前方にあって尚
該燃焼帯の最も熱的影響度の高い位置の小単位の鋼材群
とに着目し、前記大単位鋼材群についてその過去の抽出
実績および今後の抽出予−jから得られる炉内鋼材移動
速度から求められる鋼材負荷値と、嶺ム燃焼帯入ロ時に
おける鋼材平均温度の代表値として得られる熱履歴値と
、^該燃焼帯出口における鋼材目標温度の代表値として
得られる出側目挿値とから、それらの関数値として求め
られる要求炉温を算出し、前記小単位銅材群について現
在までの與績経適時間および実績炉温と、尚該燃焼帯出
口までの予lit残シ滞留時間と、その出口時の目標加
熱Ii度とから、鋼材毎の残りの滞留時必要炉温の代表
値としての要求炉温を算出し、これら大単位および小単
位鋼材群のF+]1g!求炉温の加重平均値を尚該燃焼
帯の炉温として設定制御するように構成り、、!ej鋏
燃焼帯にかかつている要求加熱レベルを的確に捉え、両
鋼材群が要求する炉温を複合制御するように、亀って目
標に対するばらつきを小さくシ、高品質、省エネルギ化
を園るようにした。In order to achieve the above object, the method for controlling a continuous heating furnace according to the present invention is aimed at controlling a large unit group of steel materials located near the inlet of each combustion zone, and a group of steel materials located ahead of the steel materials in the direction of progress of each combustion zone. Focusing on the small group of steel materials in the position of the highest thermal influence in the combustion zone, the steel material movement speed in the furnace is determined from the past extraction results and future extraction plans for the large group of steel materials. Thermal history value obtained as the representative value of the steel material average temperature at the time of entering the combustion zone, and the exit side interpolation value obtained as the representative value of the steel material target temperature at the exit of the combustion zone. , calculate the required furnace temperature obtained as a function value of these, and calculate the elapsed suitable time and actual furnace temperature for the small unit copper material group, and the preliminary lit residual residence time up to the exit of the combustion zone. , from the target heating Ii degree at the exit, calculate the required furnace temperature as a representative value of the required furnace temperature during remaining residence for each steel material, and calculate the F+]1g! of these large unit and small unit steel material groups. The weighted average value of the furnace temperature is set and controlled as the furnace temperature of the combustion zone. Accurately grasp the required heating level for the ej scissors combustion zone and jointly control the furnace temperature required by both steel groups, thereby reducing the variation in target, achieving high quality, and energy saving. I did it like that.
以下に本発明の実施例を6帯式連続加熱炉を例として詳
細に説明する。Embodiments of the present invention will be described in detail below using a six-zone continuous heating furnace as an example.
第1図に示されるように、6帯式加熱炉lは装入口2か
ら抽出口3に至る炉長方向に沿って、上下予熱帯4.5
と、上下加熱帯6.7および上下均熱帯8.9を備えて
いる。被加熱対象である両割10a、装入口2から順次
装入され、抽出口3の方向へ加熱されながら移動し、抽
出口3にて後の熱間圧嬌に最適なa度まで昇温させられ
て取り出されるものである。仁の際、抽出口3における
最終的な出側目標値に合致させるべく、鋼材10に対す
る加熱条件を各燃焼帯4〜9で制御する必要がある。As shown in FIG. 1, the six-zone heating furnace l has upper and lower preheating zones 4.5
It is equipped with 6.7 upper and lower heating zones and 8.9 upper and lower soaking zones. The Ryowari 10a, which is the object to be heated, is charged sequentially from the charging port 2, moves toward the extraction port 3 while being heated, and is heated at the extraction port 3 to a degree a that is optimal for later hot compaction. It is something that is taken out. During combustion, it is necessary to control the heating conditions for the steel material 10 in each combustion zone 4 to 9 in order to match the final outlet target value at the extraction port 3.
今、制御対象とする燃焼帯として上部加熱帯6を考え、
以下ζ0燃焼帯の炉温を制御する方法を例にとって第2
−に基づき説明する。Now, considering the upper heating zone 6 as the combustion zone to be controlled,
The following is a second example of a method for controlling the furnace temperature in the ζ0 combustion zone.
-Explanation based on.
この上部加熱帯(以下燃焼帯とい5)6の炉温を制御す
るに際して考慮しなければならないの祉、現在この燃焼
帯6に在炉している鋼材10に対する加熱条件と、将来
投入される鋼材lOに対して必要な加熱条件である。こ
れは当該燃焼帯6における現在の要求加熱レベルと、将
来の要求加熱レベルとを適格に捉えておかなければ、最
適な加熱条件に制御できないからである。When controlling the furnace temperature of this upper heating zone (hereinafter referred to as combustion zone 5) 6, there are certain considerations that must be taken into account, such as the heating conditions for the steel materials 10 currently in the furnace and the steel materials that will be introduced in the future. These are the necessary heating conditions for lO. This is because unless the current required heating level and future required heating level in the combustion zone 6 are properly understood, it is not possible to control the heating conditions to the optimum.
そζで、仁の燃焼帯6に!!−求される加熱レベルを捉
えて炉温制御するIIcM!Aシ、当該燃焼帯6のバー
ナ11により形成される火炎位置あるいは炉温検出端1
2の位置に対応する比較的小単位の鋼材群14と、壱該
燃焼帯6の入口付近に位置す石比教的大単位の鋼材群1
3とに着目するものである。Then, we reach Jin's combustion zone 6! ! - IIcM that controls the furnace temperature by capturing the required heating level! A, the flame position or furnace temperature detection end 1 formed by the burner 11 of the combustion zone 6
A relatively small group of steel materials 14 corresponding to the position 2, and a large group of steel materials 1 located near the entrance of the combustion zone 6.
We will focus on 3.
すなわち、前述の如く、連続加熱炉1の非定常性および
燃焼制御ゾーンが炉長方向に3〜4ゾーンしかないこと
からすれば、ある燃焼帯の炉温を制御しようとするとき
、制御対象とする鋼材は、そのゾーン内に位置するうち
の最4加熱条件の厳しいもの一枚と考えることもできる
し、ある程度枚数を集めた鋼材群として捉えること4可
能である。That is, as mentioned above, considering the unsteadiness of the continuous heating furnace 1 and the fact that there are only 3 to 4 combustion control zones in the furnace length direction, when trying to control the furnace temperature in a certain combustion zone, it is difficult to control the The steel material to be heated can be considered to be one of the steel materials located within the zone that is subjected to the most severe heating conditions, or it can be considered as a group of steel materials that have been collected to a certain number.
ま九、制御il]灼象たる燃焼帯の将来の加熱条件が賓
動する要因は、当該燃焼帯の入口付近に゛位置する鋼材
に存する。このようなことから、本爽施例では、第2図
に示すように、当該燃焼帯6に位置する鋼材10のうち
、燃焼帯入口付近にある比較的大単位の鋼材群13(こ
れをA鋼材群と称する)と、炉温検出端12あるい祉バ
ーナIIC)位置を考慮し、最も操炉影蕃すなわち熱的
影畳度の大きい位置にある比較的小単位の鋼材群14(
これをB鋼材群と称する)とに着目するものとした。こ
れは、要求加熱レベルの変動を燃焼帯の炉温に反映させ
るためA鋼材については大単位でよく、他方、焼上げ程
度の最終チェックをなすためKはB鋼材を小単位とする
必要があるからである。特に本爽施例では人鋼材群を3
枚、B鋼材群を1枚としているが、両鋼材群の大きさ、
炉内位置については各燃焼帯毎に異なってよく、実炉に
て実験的に充分検証した上で最適なものとすることが望
ましい。9. Control] The factor that changes the future heating conditions of the burning zone lies in the steel material located near the entrance of the burning zone. For this reason, in this example, as shown in FIG. 2, among the steel materials 10 located in the combustion zone 6, a relatively large group of steel materials 13 (this Considering the position of the furnace temperature detection end 12 or the welfare burner IIC), a relatively small unit steel group 14 (referred to as a steel group) located at a position where the furnace operation influence, that is, the degree of thermal influence is the largest, is determined.
This will be referred to as the B steel material group). This can be done in large units for steel A in order to reflect fluctuations in the required heating level on the furnace temperature in the combustion zone, while for steel K it is necessary to do it in small units for steel B in order to perform a final check on the degree of baking. It is from. In particular, in this example, the number of human steel materials was 3.
Although the steel group B is made into one sheet, the size of both steel groups,
The position in the furnace may be different for each combustion zone, and it is desirable to determine the optimum position after thorough experimental verification in an actual furnace.
このように選定され九着目鋼材群では、それぞれ要求さ
れる条件が異なるため、必要な設定炉温も異なる。そζ
で、まず、A鋼材群に着目し、この人鋼材群に対する設
定条件を求める。設定条件は、当該燃焼帯6に投入され
る鋼材群の大きさや抽出ピッチあるいは目標温度などに
よシ変動する非定常性であることから、これを定量化す
る手段として、「鋼材負荷値」、r声履歴値」、「出側
目標値」の要因に分別して求め木ものである。The ninth group of steel materials selected in this way has different required conditions, and therefore requires different set furnace temperatures. Soζ
First, focusing on steel group A, setting conditions for this steel group are determined. Since the setting conditions are unsteady and vary depending on the size of the steel group introduced into the combustion zone 6, extraction pitch, target temperature, etc., as a means to quantify this, "steel material load value", This is a tree that separates the factors into ``voice history value'' and ``output target value.''
まず、人鋼材群の銅材負荷値MAは、鋼材の寸法、重量
および移動速度に関するものであり、次式にて表現でき
る。First, the copper material load value MA of the steel material group relates to the dimensions, weight, and moving speed of the steel material, and can be expressed by the following equation.
MA=υ、XΣWム/ΣpL、、、、、、、、、、、、
、、、、、、、、、、、、、、、、、、 (1)L
L
ここでM^は人鋼材群の鋼材負荷値(tm/H,)、ν
tは現在時刻lにおけるA鋼材群の移動速度(II /
Hr )、WitfA鋼材群中の鋼材A f)単重(
t@、PbはA鋼材群中の鋼材にの輻(−) (鋼材
間にクリアランスのある場合はこれを含める)である。MA=υ,XΣWmu/ΣpL, ,,,,,,,,,
, , , , , , , , , , , , (1) L
L Here, M^ is the steel load value (tm/H,) of the human steel group, ν
t is the moving speed (II /
Hr), WittA steel material A f) unit weight (
t@, Pb is the convergence (-) of the steel materials in the A steel material group (if there is a clearance between the steel materials, this is included).
このA11lj材群についての単重W↓や幅PLKつい
ては、トラッキング情報によシ容易に知ることができる
。The unit weight W↓ and width PLK of this A11lj material group can be easily known from tracking information.
とζろで、移動速度9t は、現在時刻1における平
均速度であり、現時点を中心に時間間隔4tを考え、現
在よシ少し前までの鋼材抽出実績と将来の鋼材抽出予測
を含めて求めたA鋼材群の移動距離から算出される。す
なわち、下式から求められる。In ζro, the moving speed 9t is the average speed at the current time 1, which was calculated by considering a time interval of 4t around the current time and including the steel material extraction results up until a little earlier than the present time and the future steel material extraction predictions. Calculated from the moving distance of A steel group. That is, it is obtained from the following formula.
シー = X/ Δ・之 (ガ’/Hr) ・
・・・・・・・・・・・・・・・・・・・・ (2
)こζで、XはΔχ内KA鋼材群の移動する距離(m)
、Δlは現在時刻lを中心とする時間間隔である。C = X/ Δ・之 (Ga'/Hr) ・
・・・・・・・・・・・・・・・・・・・・・ (2
) where ζ, X is the distance (m) that the KA steel group moves within Δχ
, Δl is a time interval centered on the current time l.
上記(2)式において、Xを算出するためには、現時刻
Aを中心とじ九過去側時刻(λ−Δl/2)から将来時
刻(i+)−t/2)間の鋼材の抽出時刻O実績と予測
が必要である。予測に関しては圧延機能力と加熱炉10
能力の大小関係によシ、前者が後者を上まわっている場
合には、加熱炉内の在炉鋼材の種別にて予め定められた
抽出ピッチで抽出されるので、今後抽出される鋼材の抽
出時刻予測が可能となる。逆に、後者が前者を上まわっ
ている場合には、鋼材の種別、寸法と圧砥サイズ、圧気
スケジュールなどによシ圧延所要時間が定まり、同様に
抽出時刻を予測する仁とが可能である。In equation (2) above, in order to calculate Actual results and predictions are necessary. Regarding prediction, rolling capability and heating furnace 10
Depending on the size of the capacity, if the former exceeds the latter, the steel will be extracted at a predetermined extraction pitch depending on the type of steel in the heating furnace. Time prediction becomes possible. On the other hand, if the latter exceeds the former, the required rolling time is determined by the type of steel material, dimensions, rolling size, pressure schedule, etc., and it is possible to predict the extraction time in the same way. .
なお、予め知られている休止については、その所要時間
を加え修正すればよい。Note that for a pause that is known in advance, the required time may be added and modified.
また、時間間隔ノlは抽出ピッチとの兼ね合いで定まシ
、鋼材負荷値MAO変やをダイ少々ツクに適確に表現し
、かつその絶対値す充分議論できるような値として実験
的に求められ、一般的には平均抽出ピッチのトI倍程度
にするとよいことが判明した。In addition, the time interval No. 1 is determined in consideration of the extraction pitch, and is determined experimentally as a value that accurately expresses the change in the steel load value MAO and allows for a thorough discussion of its absolute value. It has been found that it is generally best to set the pitch to about I times the average extraction pitch.
斯かる鋼材負荀値M^は、現在よシ過去側の移動実績の
みならず、今後の移動予想も含め九リアルタイムかつダ
イナミックな意味をもつむととなる。Such steel material negative value M^ has a real-time and dynamic meaning, including not only the current and past movement results but also future movement predictions.
次に、人鋼材群の熱履歴値HIAを求める。ム鋼材群が
蟲該燃焼帯6の入口位置に到達している場合において、
これらA鋼材群の加熱炉lへの鋏人から現在に至るまで
の移動実績は在炉鋼材のトラッキング情報によシ知るこ
とができる。また、仁の間の実績として炉内雰囲気i1
度およびA鋼材群の装入温度は判明しているので、予め
理論的もしくは実験的に求められている伝熱係数を用い
、公知の加熱炉内鋼材の伝熱計算法によシ、人鋼材群の
鋼材毎に尚赦燃焼帯6の入口時における鋼材↓の平均温
度(0区)↓が計算される。人鋼材群の各々について、
この鋼材平均温度(θI)Aを求め、その代表値をもっ
て熱履歴11[[HIムとするものである。この代表値
は通常平均値としてよく、あるいは加熱不足などを生じ
る可能性がある場合など状況に応じて最小値を採用する
。Next, the thermal history value HIA of the steel material group is determined. When the steel group has reached the inlet position of the combustion zone 6,
The movement history of these steel materials group A from the time they were transferred to the heating furnace 1 to the present can be known from the tracking information of the steel materials in the furnace. In addition, as a result of Jin-no-ma, the furnace atmosphere i1
Since the temperature and the charging temperature of the steel material group A are known, the heat transfer coefficient determined theoretically or experimentally in advance is used to calculate the heat transfer of the steel material in the heating furnace using the known heat transfer calculation method for the steel material in the heating furnace. For each steel material in the group, the average temperature (0 zone) ↓ of the steel material ↓ at the entrance of the gentle combustion zone 6 is calculated. For each group of human steel materials,
This steel material average temperature (θI)A is determined and its representative value is taken as the thermal history 11 [[HIM]. This representative value may normally be an average value, or a minimum value may be adopted depending on the situation, such as when there is a possibility of insufficient heating.
更に、A鋼材群の出側目標値HO^は灰のようにして求
められる。飾述の如く、在炉鋼材の抽出ピッチから抽出
時刻の予測が可能であシ、シ九がって、人鋼材群につき
各鋼材毎の燃焼帯6の出口位置から抽出口31での滞留
時間の予測ができる。Furthermore, the output side target value HO^ of the A steel material group is determined in a gray manner. As mentioned above, it is possible to predict the extraction time from the extraction pitch of steel materials in the furnace, and the residence time at the extraction port 31 from the exit position of the combustion zone 6 for each steel material group for each steel material group. can be predicted.
したがって、この滞留時間の予測値と、各鋼材毎に定め
られている目標抽出温度、および轟賦燃焼帯6の出口か
ら抽出口3まで通過する際の炉内雰囲気温度O予測値を
用い、予め理論的あるいは実験的に求められた伝熱係数
を採用し、公知の加熱炉内鋼材の伝熱計算法によシ、轟
骸燃焼帯6の出口時におけるA鋼材群についての各鋼材
毎の平均温度の目標値(#、)門を算出することができ
る。Therefore, using the predicted value of this residence time, the target extraction temperature determined for each steel material, and the predicted value of the furnace atmosphere temperature O when passing from the outlet of the roaring combustion zone 6 to the extraction port 3, Using the heat transfer coefficient determined theoretically or experimentally, and using the known heat transfer calculation method for steel materials in the heating furnace, the average for each steel material for steel material group A at the exit of the roaring shell combustion zone 6 is calculated. The target temperature value (#,) can be calculated.
A鋼材群の各鋼材ふについて求められ良鋼材平均目標温
度(−・)Aから出側目標値HOAを定めるものである
が、この出側目標値HOAは、尚該鋼材平均目標温f(
#e)iの代表値をもって定める。The outlet target value HOA is determined from the good steel average target temperature (-・) A obtained for each steel material in the A steel group.
#e) Determine using the representative value of i.
仁の代表値祉通常平均値でよく、状況によっては最大値
を採る。最大値とするのは燃焼帯6において加熱不足が
生じないようにするためである。Typical value of ren The average value is usually sufficient, but depending on the situation, the maximum value may be taken. The reason for setting it to the maximum value is to prevent insufficient heating from occurring in the combustion zone 6.
このようにして求められた鋼材負荷値Mム、熱履歴値H
I^、出側目標値HO^からなる3つの要因は、嶋該燃
焼帯6の加熱負荷すなわちム鋼材群が要求している炉温
レベルを定量的に表示し、しかも加熱負荷の変動はこれ
ら3要因の変動として表われる。したがって、i該燃焼
帝6の設定条件であるA鋼材群の要求炉温θ^は、上記
3111因の関数値として次式の如く表わされる。Steel load value M and thermal history value H obtained in this way
The three factors consisting of I^ and outlet target value HO^ quantitatively represent the heating load of the combustion zone 6, that is, the furnace temperature level required by the steel material group, and the fluctuations in the heating load are caused by these factors. It appears as fluctuations in three factors. Therefore, the required furnace temperature θ^ of steel material group A, which is the setting condition for the combustion temperature 6, is expressed as a function value of the above 3111 factors as shown in the following equation.
θA冨F(Mム、HI^、HOA) ・・・・・・・
・・・・・ (3)ここで関数形Fは、6鋏燃焼帯6の
伝熱特性に依存するものであシ、炉の操業が非定常であ
ることからすれば理論的に求めることは困難である丸め
、これを基礎として実験的に充分検証され九関数形とす
ることが望ましい。通常この関数形は一次結合の形で表
わす仁とができる。θA wealth (Mmu, HI^, HOA) ・・・・・・・・・
(3) Here, the functional form F depends on the heat transfer characteristics of the six-scissor combustion zone 6, and given that the operation of the furnace is unsteady, it cannot be determined theoretically. Since rounding is difficult, it is desirable to have a nine-function form that has been thoroughly verified experimentally based on this rounding. Normally, this functional form can be expressed as a linear combination.
なお、上記値を求める上で必要な在炉鋼材の抽出ピッチ
予測や各ゾーン滞留時間予測値は、各鋼材の圧延時間予
測値を圧嬌機のパススケジスールモデル等により計算す
る手段が有効となっている丸め、容易かつ精度よく求め
ることができる。In addition, to calculate the extraction pitch prediction of in-furnace steel material and the predicted value of residence time in each zone, which are necessary to obtain the above values, it is effective to calculate the predicted rolling time value of each steel material using a pass schedule model of the compaction machine, etc. You can easily and accurately determine the rounding value.
一方、尚該燃焼帯6内の最も熱的影脅を受ける位置に在
炉するB鋼材群についての設定条件は次のように求めら
れる。すなわち、このB鋼材群について、前述の公知の
伝熱計算法を用いて、尚該燃焼帯60人口における奥績
平均温f(’t)ふと、同出口における目標平均温f:
(#。)ルとを求める仁とが可能である。また、これら
の値と、当該燃焼帯6におけゐ予測滞留時間およびm誼
燃焼帯6の予め理論的あるい拡夷験的に求められ良伝熱
係数を用い、前述の公知の伝熱計算法によシ、邑該燃焼
帯60通過時Kl−けるB鋼材群に与えられるべき目標
炉温($r)Aを予め算出することができる。On the other hand, the setting conditions for the B steel material group placed in the furnace at the position most exposed to thermal influence within the combustion zone 6 are determined as follows. That is, for this B steel material group, using the above-mentioned well-known heat transfer calculation method, we can calculate that the average temperature f('t) in the combustion zone 60 population and the target average temperature f at the exit of the same combustion zone are:
(#.) Le and seeking jin and is possible. In addition, using these values, the predicted residence time in the combustion zone 6, and the good heat transfer coefficient obtained theoretically or empirically in advance for the combustion zone 6, the above-mentioned known heat transfer calculation is performed. According to the law, it is possible to calculate in advance the target furnace temperature ($r) A that should be given to the steel group B when passing through the combustion zone 60.
し九がって、今対象としているB鋼材群は、当該燃焼帯
6の出口に近いので、燃焼帯60入口から現在の位置に
至るまでの炉温および経過時間は実績値として判明して
いるの士、との実績炉温および実績経過時間と、現在位
置から尚該燃焼帯60出口に至るまでO予測残シ滞留時
間が明らかになれば、嶋1*B鋼材群について燃焼帯出
口時の目標温ttで加熱すべき残シの滞留時間に必要と
される要求炉温(θflI)bが定まる。この場合、予
測滞留時間は前述した如く、圧延機バススケジューに′
などから容易に求められる。しかして、B鋼材群各々に
ついての設定条件は、現在位置までの実績炉温、実績経
過時間、予III残haw時間、および出口目標@度か
ら定められる燃焼帯通過時の目標炉温(#:)Aに基づ
いて算出される要求炉ll1(ネ
#rm)↓ として与えられる。ただし、仁の要求炉*
温←すl)A は、当該燃焼帯通過時の@標炉温(θ
1)↓を下限として中−プすることが望ましい。Therefore, since the steel group B that is currently being targeted is close to the exit of the combustion zone 6, the furnace temperature and elapsed time from the entrance of the combustion zone 60 to the current position are known as actual values. Once the actual furnace temperature and actual elapsed time of the furnace and the predicted O residual residence time from the current position to the exit of the combustion zone 60 are known, it is possible to calculate The required furnace temperature (θflI)b required for the residence time of the residue to be heated at the target temperature tt is determined. In this case, the predicted residence time depends on the rolling mill bus schedule as described above.
It can be easily determined from Therefore, the setting conditions for each steel group B are the actual furnace temperature up to the current position, the actual elapsed time, the preliminary III remaining haw time, and the target furnace temperature at the time of passing through the combustion zone (#: ) The required reactor calculated based on A is given as ll1(ne#rm)↓. However, the required furnace temperature* Temperature←Sl)A is @standard furnace temperature (θ
1) It is desirable to use ↓ as the lower limit.
このようにして算出されるB鋼材群の各々につい傘
て求められる要求炉温(’y+a)io代表値をもって
B鋼材群の要求炉温θlとし、代表値は通常平均慎でよ
く、状況によって最大値とする。なお、実施例では一枚
の鋼材を対象にしている丸め一義的に決定される。The required furnace temperature ('y+a)io representative value of each B steel material group calculated in this way is taken as the required furnace temperature θl of the B steel material group, and the representative value may normally be an average value, but depending on the situation, the maximum value. In addition, in the embodiment, rounding is uniquely determined for one piece of steel material.
次に1上述のようにして、人鋼材群についての要求炉温
θ^と、B鋼材群についての要求炉温θ農とが求められ
ると、制御対象としている燃焼帯6の設定炉温θは、両
者の加重平均をもって定められる。すなわち、7式によ
抄淡定されるものであ但し g、hは重み係数である。Next, when the required furnace temperature θ^ for the steel material group B and the required furnace temperature θ^ for the B steel material group are determined as described above in 1, the set furnace temperature θ of the combustion zone 6 to be controlled is determined. , is determined by the weighted average of both. That is, it is determined by formula 7, where g and h are weighting coefficients.
上記(4)式の重み係数a、jは、実炉の状況、操炉目
標に応じて任意に決定される。すなわち、非常に加熱温
度要求の厳しい材料O鳩合紘、θ、とem (DI&大
値(&a ≧810と@ g −1、h −0。The weighting coefficients a and j in the above equation (4) are arbitrarily determined depending on the actual furnace situation and the furnace operation target. That is, for materials with very strict heating temperature requirements, θ, and em (DI & large value (&a ≧810 and @ g −1, h −0.
θムくθ=0と龜g m Q 、 邊−1)とし、回榔
加熱温j[に対する少々の早熟が許容される場合には省
エネルギ指向の操炉を行うようにg)!なる重み係数を
採用すればよく、これらは実験的に見出すものである。θ = 0 and g m Q , -1), and if a little early ripening is allowed for the regeneration heating temperature j[g)! It is sufficient to adopt weighting coefficients which are determined experimentally.
具体的に、厚板加熱炉では、加熱帯において紘、lθム
ーθml≦1lQcOと龜−−1、遥=1、lθム−θ
■、1 > g o cのと自最大値を選択して設定し
、均熱帯ではθムとθ、0最大値を選択して設定した。Specifically, in the thick plate heating furnace, in the heating zone, Hiro, lθmu θml≦1lQcO and 龜−1, Haruka=1, lθmu−θ
■, 1 > g o c and its own maximum value were selected and set, and in the soaking zone, θ um and θ, 0 maximum value were selected and set.
第3図には、本夾施例による各燃焼帯の炉温を設定する
場合の70−チャートを示す。この−に示されるように
、各燃焼帯毎に、それぞれ、ム鋼材群とB鋼材群のサー
チをなし、人鋼材群について鋼材負荷値Mム、熱履歴値
HIA、出側目標値HOムを算出し、要求炉温θムを演
算するとともに、BIRt群について通過目標炉温(#
t)↓、入口よ〕現位置までの実績炉温と実績時間、残
シの滞留時間を算出し、要求炉温θ腸を演算する。次い
で、求められた両者の要求炉温θム、θlに基づき、適
宜重み係数を設定することKよプ最適炉温θを式(4)
から算出し、幽咳炉温θに当該燃焼帯を制御するもので
ある。FIG. 3 shows a 70-chart for setting the furnace temperature of each combustion zone according to the present embodiment. As shown in this figure, for each combustion zone, the M steel group and the B steel group are searched, and the steel load value M, thermal history value HIA, and output side target value HO are determined for the human steel group. In addition to calculating the required furnace temperature θm, the passing target furnace temperature (#
t) ↓, entrance] Calculate the actual furnace temperature, actual time, and residence time of the remaining waste up to the current position, and calculate the required furnace temperature θ. Next, based on the obtained required furnace temperatures θ and θl, weighting coefficients are set appropriately.
The combustion zone is controlled to the combustion furnace temperature θ.
このような実施例によシ行つ九制御例の結果を第4図に
示す。この図の上段は、目標加熱条件の厳しい場合に対
応してθム、θ箇の最大値を選択して行つ九制御結果で
あシ、抽出順序に従って取シ出され丸缶鋼材について抽
出温度を測定したものである。なお鎖線は目標抽出温度
である。i九同−下段は過常圧嬌機に対する制御結果で
あp1重み係歇を6mg、Awlとして行つえものであ
る。FIG. 4 shows the results of nine control examples carried out in accordance with such an embodiment. The upper part of this figure shows the results of the control performed by selecting the maximum values of θ and θ in response to severe target heating conditions. was measured. Note that the chain line is the target extraction temperature. The lower part of i9 shows the control results for the overpressure machine, which was carried out with the p1 weight intermittent set to 6 mg and Awl.
このように、本実施例によれば、制御対象とする燃焼帯
の入口付近および最も操炉影畳変の大自い位置の両鋼材
群に常時着目することによル、蟲該燃焼帯に要求される
要求レベルを的確に捉えることができる。を九、人鋼材
群から要求加熱レベルの変動を前もって把握し、かつB
銅材群から焼上げ1度をチェックで自ることによシ、こ
れら両者の要求炉温を複合して高度な制御を行う仁とが
可能となる。更に、鋼材の目標加熱温度に対する実績値
のばらつきを着しく軽減することも可能である。特に、
連続加熱炉の有する非定常性を充分反映し九制御が可能
である丸め、目標温度に対するばらつ龜が半減するとと
もに燃料原単位な略3〜4X低減することができ、省エ
ネルギ効果が大きく、シかも板厚精度向上によ〉歩留〉
がO,OS%内向上、品質や歩留)向上効果が大書いと
いう好tしい結果を得る仁とかで11え。As described above, according to this embodiment, by always focusing on the steel groups near the entrance of the combustion zone to be controlled and at the position where the furnace operation shadow is most likely to change, it is possible to control the combustion zone. It is possible to accurately grasp the required level of demand. 9. Understand the fluctuations in the required heating level from the steel material group in advance, and
By checking the firing temperature from a group of copper materials, it becomes possible to perform advanced control by combining the required furnace temperatures of both of them. Furthermore, it is also possible to significantly reduce the variation in the actual value with respect to the target heating temperature of the steel material. especially,
It fully reflects the unsteadiness of continuous heating furnaces and allows nine-way control.The variation in temperature relative to the target temperature is halved, and the fuel consumption rate can be reduced by approximately 3 to 4 times, resulting in a large energy-saving effect. By improving plate thickness accuracy〉Yield〉
However, it is possible to obtain favorable results such as an improvement in O, OS%, quality and yield), and a large improvement effect.
1お、本実施例は、炉層、バーナ配列、銅材種類が異な
る他の炉に対して4適用でき、汎用性がある。その他、
複数の燃焼ゾーンを有する熱処理炉、鉤威炉にも適用で
きることはもちろんである。1. This embodiment can be applied to other furnaces with different furnace layers, burner arrangements, and types of copper materials, and is therefore versatile. others,
It goes without saying that the present invention can also be applied to heat treatment furnaces and heat treatment furnaces having multiple combustion zones.
以上説明したように、本発明によれば、省エネルギ上、
品質上最適な加熱条件を的確に与えることができ、被加
熱鋼材をばらつきが少なく目II温度で抽出できる効果
を奏する。As explained above, according to the present invention, in terms of energy saving,
It is possible to accurately provide the optimum heating conditions in terms of quality, and there is an effect that the steel to be heated can be extracted at the second temperature with little variation.
【図面の簡単な説明】
第1−は6帝弐連続加熱炉の断面劇、第2−は制御対象
燃焼帯の断面−1第3園は制御方法を示すフローチャー
ト−1第4−は実施例を適用して抽出した鋼材の抽出温
度を示す図である。
1・一連続加熱炉、10・・・鋼材、11・・・バーナ
、1jl−F温検出端、13・・・A銅材群、14・・
・B鋼材群。
代理人 鵜 沼 辰 之
(ほか2名)[Brief explanation of the drawings] Part 1- is a cross-sectional view of the 6-temperature continuous heating furnace, Part 2- is a cross-section of the combustion zone to be controlled, Part 3 is a flowchart showing the control method -1, Part 4 is an example It is a figure which shows the extraction temperature of the steel material extracted by applying. 1. Continuous heating furnace, 10... Steel material, 11... Burner, 1jl-F temperature detection end, 13... A copper material group, 14...
・B steel group. Agent Tatsuyuki Unuma (and 2 others)
Claims (1)
帯の入口付近に位置する大単位の銅材群と、それらよシ
鋼材進行方向前方にあって尚鋏燃焼帯の最も熱的影響度
O高い位置の小単位鋼材群に着目し、前記大単位鋼材群
についてその過去の抽出実績および今後の抽出予測から
得られる炉内鋼材移動速度から求められる鋼材負荷値と
、尚鋏燃焼帯入口時における鋼材平均温度の代表値とし
て得られる熱履歴値と、嶋該燃焼帯出口における鋼材目
標温度の代表値として得られる出側目標値とから、それ
らの関数値として求められる要求炉温を算出し、酌記小
単位鋼材詳について現在までの実績経過時間および実績
炉温と、尚尊燃焼帯出口までの予測残シ滞蕾時間と、そ
の燃焼−出口の目標加熱温度とから鋼材毎の残シの滞留
時必要炉温の代表値としての要求炉温を算出し、これら
大単位および小単位鋼材群の両要求炉温の加重平均値を
轟該燃焼帯の炉温として設定することを%像とする連続
加熱炉の制御方法。(1) For each combustion zone of a multi-zone continuous heating furnace, there is one group of large units of copper material located near the entrance of the combustion zone, and a group of large units of copper material located near the entrance of the combustion zone, and a large group of copper materials located in the forward direction of the steel material progressing direction and at the farthest point of the scissors combustion zone. Focusing on the small unit steel material group at a position with a high degree of thermal influence O, the steel material load value obtained from the steel material movement speed in the furnace obtained from the past extraction results and future extraction predictions for the large unit steel material group, and the steel material load value From the thermal history value obtained as a representative value of the steel material average temperature at the entrance of the combustion zone and the exit side target value obtained as the representative value of the steel material target temperature at the combustion zone exit, the demand furnace is determined as a function value of these values. The temperature is calculated, and the steel material is calculated based on the actual elapsed time and actual furnace temperature for the small unit steel material details, the predicted residual bud retention time up to the exit of the Shoson combustion zone, and the target heating temperature at the combustion exit. Calculate the required furnace temperature as a representative value of the required furnace temperature during retention of each residue, and set the weighted average value of both the required furnace temperatures of the large unit and small unit steel material groups as the furnace temperature of the combustion zone. A continuous heating furnace control method that takes this into account.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10275981A JPS584412A (en) | 1981-07-01 | 1981-07-01 | Controlling method of continuous heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10275981A JPS584412A (en) | 1981-07-01 | 1981-07-01 | Controlling method of continuous heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS584412A true JPS584412A (en) | 1983-01-11 |
| JPH0160528B2 JPH0160528B2 (en) | 1989-12-22 |
Family
ID=14336120
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10275981A Granted JPS584412A (en) | 1981-07-01 | 1981-07-01 | Controlling method of continuous heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS584412A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03200499A (en) * | 1989-12-27 | 1991-09-02 | Toyota Motor Corp | Small vessel building method |
-
1981
- 1981-07-01 JP JP10275981A patent/JPS584412A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03200499A (en) * | 1989-12-27 | 1991-09-02 | Toyota Motor Corp | Small vessel building method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0160528B2 (en) | 1989-12-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103225017B (en) | Rod and wire billet heating furnace model control method and apparatus | |
| CN109248928A (en) | Dynamic furnace temperature control method for hot rolling heating furnace | |
| RU2008121977A (en) | METHOD AND LINE OF CLEAR ROLLING FOR HOT ROLLING OF SOURCE MATERIAL | |
| CN113652533B (en) | Slab heating control method and device | |
| JPS584412A (en) | Controlling method of continuous heating furnace | |
| JP4469143B2 (en) | Manufacturing method of hot-rolled steel sheet | |
| JPS6051535B2 (en) | Optimal control device for billet heating furnace | |
| JPH08246058A (en) | Automatic combustion control method in continuous heating furnace | |
| JP3982042B2 (en) | Combustion control method for continuous heating furnace | |
| JP3297741B2 (en) | Furnace temperature control method for continuous heating furnace | |
| JP5919734B2 (en) | Method for setting furnace temperature and furnace temperature control system for continuous heating furnace, continuous heating furnace, and method for producing metal material | |
| KR101286558B1 (en) | Method for Determining Set-point Temperature of Each Zone of Reheating Furnace | |
| KR20100047006A (en) | A method and a skid apparatus for reducing temperature difference in a heating furnace | |
| CN106370020B (en) | Recuperative heater blank head and tail temperature difference control method | |
| CN117660748A (en) | Control method for step-by-step operation of billet in step-type heating furnace | |
| US20050252587A1 (en) | Process for producing steel product and production facility therefor | |
| JPS6411686B2 (en) | ||
| JPH05279754A (en) | Furnace temperature control method for continuous heating furnace | |
| JPH076001B2 (en) | Furnace temperature setting device for continuous heating furnace | |
| JP3174148B2 (en) | Furnace equipment for heating and soaking high-temperature slabs | |
| JPS5812325B2 (en) | Control method for continuous heating furnace | |
| JP2792445B2 (en) | Hot rolling method for preventing steel sheet from rolling around four edges | |
| JP4686987B2 (en) | Heating furnace combustion control method in hot rolling | |
| JPS6055569B2 (en) | Heating temperature control method for seamless steel pipes | |
| JPS62164824A (en) | Method for controlling heat pattern of continuous heating furnace |