JPH02225626A - Method for controlling transfer speed of continuous annealing furnace - Google Patents
Method for controlling transfer speed of continuous annealing furnaceInfo
- Publication number
- JPH02225626A JPH02225626A JP4496989A JP4496989A JPH02225626A JP H02225626 A JPH02225626 A JP H02225626A JP 4496989 A JP4496989 A JP 4496989A JP 4496989 A JP4496989 A JP 4496989A JP H02225626 A JPH02225626 A JP H02225626A
- Authority
- JP
- Japan
- Prior art keywords
- transfer speed
- target
- speed
- temp
- succeeding
- 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
Links
- 238000000137 annealing Methods 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title claims description 22
- 239000000463 material Substances 0.000 claims abstract description 86
- 238000010438 heat treatment Methods 0.000 abstract description 38
- 229910000831 Steel Inorganic materials 0.000 abstract description 22
- 239000010959 steel Substances 0.000 abstract description 22
- 238000003466 welding Methods 0.000 abstract description 4
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 230000002950 deficient Effects 0.000 abstract 1
- 238000007796 conventional method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010304 firing Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
Landscapes
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
- Control Of Heat Treatment Processes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、連続焼鈍炉における帯材の温度制御を行うた
めの帯材の移送速度制御方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for controlling the transport speed of a strip material for controlling the temperature of the strip material in a continuous annealing furnace.
〔従来の技術及び発明が解決しようとする課題〕鋼板の
連続焼鈍炉では、その加熱帯として連続加熱炉が用いら
れ、鋼板の機械的特性等の面から定められた特有のヒー
トサイクルを確保すべく鋼板の熱処理を行っている。こ
のような連続焼鈍炉においては、鋼板を連続的に熱処理
するために炉の入側で通板中の鋼板の後端と、次に通板
される鋼板の先端とを溶接によって接合している。この
ように鋼板を接合した場合、夫々の鋼板の寸法目標板温
及び材質が接合部の前後で異なる場合には、加熱炉の出
口板温が目標板温となるように操作量である移送速度及
び炉温を変更して熱処理を行っている。[Prior art and problems to be solved by the invention] In a continuous annealing furnace for steel plates, a continuous heating furnace is used as the heating zone, and a specific heat cycle determined from the mechanical properties of the steel plate is ensured. We are currently heat treating steel plates. In such a continuous annealing furnace, in order to heat-treat the steel plate continuously, the rear end of the steel plate being threaded is joined by welding to the tip of the steel plate being threaded next on the entrance side of the furnace. . When steel plates are joined in this way, if the size target plate temperature and material of each steel plate are different before and after the joint, the transfer speed, which is a manipulated variable, should be adjusted so that the outlet plate temperature of the heating furnace becomes the target plate temperature. Heat treatment is performed by changing the furnace temperature.
前記移送速度を操作量として出口板温を制御する方法に
ついて説明する。A method of controlling the outlet plate temperature using the transfer speed as a manipulated variable will be explained.
第5図は従来の連続焼鈍炉のライン速度制御方法を示す
タイムチャートである。これは(a)に示すように先行
材の板厚H1が次行材の板厚11□より小さく (II
I<I+□) 、(b)に示すように先行材の目標板温
T1が次行材の目標板温T、よりも小さい(Ti<Tz
)場合、(d)に示すように炉温か一定の条件で目標板
温T、を達成すべく(C)に示す移送速度をV、よりv
2へと減少させる場合の例を示すものである。FIG. 5 is a time chart showing a conventional line speed control method for a continuous annealing furnace. This is because, as shown in (a), the thickness H1 of the preceding material is smaller than the thickness 11□ of the succeeding material (II
I<I+□), as shown in (b), the target plate temperature T1 of the preceding material is smaller than the target plate temperature T of the subsequent material (Ti<Tz
), in order to achieve the target plate temperature T, with a constant furnace temperature as shown in (d), the transfer speed shown in (C) is set from V to v.
This shows an example of reducing the number to 2.
この場合、移送速度の減少により鋼材の内存焼時間が長
くなり、(e)に示す加熱炉出口板温が上昇する。しか
しながら加熱炉出口板温か目標板温T2に安定するまで
には板温外れ部eに示す如(一定の時間が必要である。In this case, due to the reduction in the transfer speed, the internal firing time of the steel material becomes longer, and the plate temperature at the exit of the heating furnace shown in (e) increases. However, a certain amount of time is required until the plate temperature at the exit of the heating furnace stabilizes at the target plate temperature T2 (as shown in the plate temperature deviation part e).
この時間が経過する間に加熱される鋼材は所定の熱処理
条件を満たしていないため鋼材が所定の機械的特性を得
ることができないという問題があった。Since the steel material heated during this period of time does not satisfy the predetermined heat treatment conditions, there is a problem in that the steel material cannot obtain predetermined mechanical properties.
本発明は斯かる事情に鑑みてなされたものであり、予め
定められた目標応答時間にて加熱炉出口板温か目標板温
に安定するように移送速度の変更を行う連続焼鈍炉の移
送速度制御方法を提供することを目的とする。The present invention has been made in view of the above circumstances, and provides a transfer speed control for a continuous annealing furnace in which the transfer speed is changed so that the plate temperature at the exit of the heating furnace is stabilized at the target plate temperature within a predetermined target response time. The purpose is to provide a method.
〔課題を解決するための手段〕
本発明に係る連続焼鈍炉の移送速度制御方法は、寸法、
目標温度、材質の少なくとも1つが異なる先行材と次行
材とを接合した帯材の温度制御を行うために、該寸法、
目標温度、材質により予め次行材の移送速度を定め、こ
の移送速度になすべく次行材の移送速度を制御する連続
焼鈍炉の移送速度制御方法において、前記次行材の移送
速度が先行材の移送速度より速い場合は、次行材を前記
移送速度より速い速度に一旦保持した後、前記移送速度
になすべく制御し、一方次行材の移送速度が先行材の移
送速度より遅い場合は、次行材を前記移送速度より遅い
速度に一旦保持した後、次行材の移送速度になすべく制
御することを特徴とする。[Means for Solving the Problems] The method for controlling the transfer speed of a continuous annealing furnace according to the present invention has the following advantages:
In order to control the temperature of the strip material made by joining the preceding material and the succeeding material, which differ in at least one of the target temperature and material, the dimensions,
In a method for controlling the transfer speed of a continuous annealing furnace, in which the transfer speed of the next material is determined in advance based on the target temperature and material, and the transfer speed of the next material is controlled to reach the set transfer speed, the transfer speed of the next material is set to be the same as that of the preceding material. If the transfer speed is faster than the transfer speed, the next material is temporarily held at a speed higher than the transfer speed, and then controlled to reach the transfer speed.On the other hand, if the transfer speed of the next material is slower than the transfer speed of the preceding material , the next row material is once held at a speed lower than the transport speed, and then the next row material is controlled to be at the transport speed of the next row material.
予め定められた次行材の移送速度が先行材の移送速度よ
り速い場合は、次行材を予め定められた移送速度に制御
する前に該移送速度より速い速度に一旦保持すると、帯
材の温度の変化率が大きくなるため、該温度がその目標
値まで短時間にて到達する。これと同様に予め定められ
た次行材の移送速度が先行材の移送速度より遅い場合は
、次行材を予め定められた移送速度に制御する前に該移
送速度より遅い速度に一旦保持すると、帯材の温度の変
化率が大きくなるため該温度が目標値まで短時間にて到
達する。If the predetermined transfer speed of the next material is faster than the transfer speed of the preceding material, once the next material is held at a faster speed than the predetermined transfer speed before controlling the next material to the predetermined transfer speed, the strip material Since the rate of change of temperature increases, the temperature reaches its target value in a short time. Similarly, if the predetermined transfer speed of the next material is slower than the transfer speed of the preceding material, once the next material is held at a slower speed than the predetermined transfer speed before controlling the next material to the predetermined transfer speed. , since the rate of change in temperature of the strip increases, the temperature reaches the target value in a short time.
〔実施例]
以下、本発明に係る連続焼鈍炉の移送速度制御方法をそ
の実施例を示す図面に基づいて説明する。[Example] Hereinafter, a method for controlling the transfer speed of a continuous annealing furnace according to the present invention will be described based on drawings showing examples thereof.
第1図は本発明方法を実施する場合に用いる連続焼鈍炉
の加熱@置と移送速度制御系統を示す模式図である。FIG. 1 is a schematic diagram showing the heating position and transfer speed control system of a continuous annealing furnace used when carrying out the method of the present invention.
図においてlは内部に帯状の鋼板Hを移送するための複
数個のハースロール2.2・・・を備えた連続焼鈍炉加
熱帯である加熱炉であって、鋼板Hの移送ラインの加熱
炉1の出側には駆動モータMで駆動される上下1対のプ
ライドルロール3が配され、前記駆動モータMはモータ
速度制御n装置4によって速度が制御されるようになっ
ている。In the figure, l denotes a heating furnace which is a continuous annealing furnace heating zone equipped with a plurality of hearth rolls 2.2 for transferring the strip-shaped steel plate H, and is a heating furnace in the transfer line of the steel plate H. A pair of upper and lower priddle rolls 3 driven by a drive motor M are disposed on the output side of the roller 1, and the speed of the drive motor M is controlled by a motor speed control device 4.
6は鋼板Hの寸法、目標板温、材質により前記移送ライ
ンの移送速度を設定する移送速度設定器であって、7は
板温を変化させる場合加熱炉出口の板温か目標板温に整
定されるまでの目標応答時間1pを設定する目標応答時
間設定器であり、8は前記加熱帯出口板温の応答の時定
数Tを設定する時定数設定器である。Reference numeral 6 is a transfer speed setting device that sets the transfer speed of the transfer line according to the dimensions, target plate temperature, and material of the steel plate H, and 7 is a transfer speed setting device that sets the plate temperature at the outlet of the heating furnace to the target plate temperature when changing the plate temperature. A target response time setting device 8 sets a target response time 1p until the heating zone temperature reaches 1, and a time constant setting device 8 sets a time constant T of the response of the plate temperature at the outlet of the heating belt.
前記移送速度設定器6.目標応答時間設定器7時定数設
定器8の出力信号は夫々移送速度制御器5へ入力される
。移送速度制御器5では移送速度設定器6より入力され
る先行材移送速度設定値Vl。Said transfer speed setting device6. The output signals of the target response time setter 7 and the time constant setter 8 are input to the transfer speed controller 5, respectively. In the transfer speed controller 5, the preceding material transfer speed setting value Vl is inputted from the transfer speed setting device 6.
次行材移送速度設定値v!、目標応答時間設定器7より
入力される目標応答時間Lp2時定数設定器8より入力
される時定数Tに基づき後述する移送速度制御パターン
を決定し、これを実現すべく前記モータ速度制御装置4
へ移送速度制御信号を入力させる。モータ速度制御装置
4では前記移送速度制御信号に基づき駆動モータMの駆
動制御を行い鋼板Hの移送ラインの移送速度を制御する
。Next material transfer speed setting value v! , the target response time Lp2 input from the target response time setter 7, the time constant T inputted from the time constant setter 8, determines a transfer speed control pattern to be described later, and in order to realize this, the motor speed control device 4
A transfer speed control signal is input to. The motor speed control device 4 controls the drive motor M based on the transfer speed control signal to control the transfer speed of the steel plate H on the transfer line.
次に本発明の移送速度制御方法の原理を説明する。Next, the principle of the transfer speed control method of the present invention will be explained.
第2図は移送速度の変化に対する加熱炉出口板温の応答
を示すタイムチャートであり、第3図は本発明方法に用
いる移送速度制御のタイムチャートである。FIG. 2 is a time chart showing the response of the plate temperature at the outlet of the heating furnace to changes in the transfer speed, and FIG. 3 is a time chart of the transfer speed control used in the method of the present invention.
例えば、第2図に示す如く加熱炉出口板温を低下させる
べく移送速度を先行材移送速度設定値v1から次行材移
送速度設定値ν、へ変化させる場合(vl<ν、)、加
熱炉出口温度を目標応答時間1pにて安定させるために
は、第3図に示す如く、先行材と次行材との接合部が例
えば加熱炉に入る時を時刻1=0とし、この時刻1=0
にて移送速度を先行材移送速度設定値V、より後述する
板速度設定値V、ヘステップ状に増加させ、これを時刻
し。For example, as shown in FIG. 2, when changing the transfer speed from the preceding material transfer speed set value v1 to the next material transfer speed set value ν in order to lower the plate temperature at the heating furnace outlet (vl<ν,), the heating furnace In order to stabilize the outlet temperature at the target response time 1p, as shown in FIG. 0
At , the transfer speed is increased stepwise from the preceding material transfer speed setting value V to the plate speed setting value V, which will be described later, and this is timed.
まで保持した後、次行材移送速度設定値v2ヘステンプ
状に減少させれば良い。After holding it up to the next material transfer speed setting value v2, it is sufficient to decrease it in a stepwise manner.
このような制御を行う前にまず、第2図に示す如き移送
速度■をvlから’Jtヘステップ状に変化させた場合
の加熱炉出口板点の応答波形を、炉温−定の条件にて同
一寸法、同一材質の鋼板を用いて多数収集し、これらの
平均をとった応答波形を加熱炉出口板温の初期値よりの
板温変化量ΔT3として下記(1)式の如き1次遅れ系
で近似する。Before carrying out such control, first, the response waveform at the heating furnace outlet plate point when the transfer speed 2 is changed stepwise from vl to 'Jt as shown in Fig. 2, under the condition of a constant furnace temperature. The response waveforms obtained by collecting a large number of steel plates of the same size and the same material and taking the average of these are used as the change in plate temperature ΔT3 from the initial value of the plate temperature at the outlet of the heating furnace, and the first-order lag system as shown in equation (1) below is used. Approximate by
但し θT、/θV:移送速度変化が加熱炉出口板温変
化
に及ぼす影響係数
(’C/mp剛)
T:加熱炉出口板温の
応答の時定数
Sニラプラス演算子
前記(1)式を逆ラプラス変換することにより下記(2
)式に示す如く板温変化量ΔT、を時間関数化(t≧0
)・・・(2)
但し L:移送速度変更時を基準とする時間衣に前記板
速度設定値V、を決定する方法について説明する。However, θT, /θV: Influence coefficient of transfer speed change on heating furnace exit plate temperature change ('C/mp stiffness) T: Time constant of response of heating furnace outlet plate temperature S Nira plus operator Reverse the above equation (1) By Laplace transform, the following (2
), the plate temperature change ΔT is converted into a time function (t≧0
)...(2) However, L: A method for determining the plate speed set value V based on the time when the transfer speed is changed will be explained.
第3図における時刻Oより目標応答時間1pまでの加熱
炉出口板温変化量ΔT、は前記(2)式と同・・・(3
)
目標応答時間Ll、において加熱炉出口板温を目標値に
整定させるためには、移送速度を先行材移送速度設定値
V、より板速度設定値V、へ変化させた場合の目標応答
時間LPにおける加熱炉出口板温変化量と、移送速度を
先行材移送速度設定値V、より次行材移送速度設定値v
2へ変化させた場合の加熱炉出口板温変化量の定常値θ
T、/θ■・ (ν2−ν、)とを一致させれば良い。The amount of change ΔT in the heating furnace outlet plate temperature from time O to target response time 1p in FIG. 3 is the same as the equation (2) above... (3
) In order to settle the heating furnace outlet plate temperature to the target value at the target response time Ll, the target response time LP is obtained when the transfer speed is changed from the preceding material transfer speed setting value V to the plate speed setting value V. The amount of change in plate temperature at the heating furnace outlet and the transfer speed are determined by the preceding material transfer speed setting value V and the next material transfer speed setting value V.
Steady value θ of the amount of change in heating furnace outlet plate temperature when changing to 2
It is sufficient to match T, /θ■·(ν2−ν,).
即ち下記(4)式が成り立てば良い。That is, it is sufficient if the following formula (4) holds true.
前記(4)式より、時刻0において移送速度変更量V、
−V、に対してに3倍の移送速度変更を行い、目標応答
時間jpまでこれを保持すれば、目標応答時間L2にお
いて加熱炉出口板温は目標値に到達する。そして、目標
応答時間り、において移送速度を次行材移送速度設定値
v2ヘステップ状に変化させれば以後、加熱炉出口板温
は目標値に安定に制御される。From the above equation (4), at time 0, the transfer speed change amount V,
-V, if the transfer speed is changed three times and this is maintained until the target response time jp, the furnace outlet plate temperature will reach the target value at the target response time L2. Then, if the transfer speed is changed stepwise to the next material transfer speed setting value v2 during the target response time, the heating furnace outlet plate temperature is stably controlled to the target value.
また、前述の如き制御は加熱炉出口板温を上昇させるべ
く移送速度を先行材移送速度設定値V、から次行材移送
速度設定値V、 (V、>ν2)へ変化させる場合も同
様に適用できる。Furthermore, the above-mentioned control is applied similarly when changing the transfer speed from the preceding material transfer speed setting value V, to the next material transfer speed setting value V, (V, > ν2) in order to increase the plate temperature at the outlet of the heating furnace. Applicable.
前述した如き原理に基づき前記移送速度制御系統により
移送速度制御を行う方法について説明する。A method of controlling the transfer speed using the transfer speed control system based on the principle as described above will be explained.
寸法、目標板温、材質等の条件が異なる先行材と次行材
とを溶接した鋼板Hを炉温一定にて熱処理する場合、前
記移送速度設定器6.目標応答時間設定器71時定数設
定器8へ予め夫々の設定値を人力しておく。これらの設
定値の情報が入力される移送速度制御器5においては、
これらの設定値に基づき前記(4)式により板速度設定
値V、を算出し、先行材より次行材への移送速度変更時
に移送速度をステップ状に先行材移送速度設定値v1よ
り板速度設定値V、まで変更し、移送速度を目標応答時
間1pまで保持し、該目標応答時間tいにおいて移送速
度をステップ状に次行移送速度設定値ν2まで変更する
制御を行うべくモータ速度制御装置4へ移送速度制御信
号を出力する。モータ速度制扉装置4では前記移送速度
制御信号に基づき、駆動モータMの駆動制御を行い、鋼
板11の移送速度を制御する。When heat-treating a steel plate H obtained by welding a preceding material and a subsequent material having different conditions such as dimensions, target plate temperature, material quality, etc. at a constant furnace temperature, the transfer speed setting device 6. The respective set values are manually entered into the target response time setter 71 and the time constant setter 8 in advance. In the transfer speed controller 5 into which information on these setting values is input,
Based on these set values, the plate speed setting value V is calculated using the formula (4) above, and when changing the transfer speed from the preceding material to the next material, the transfer speed is changed in steps from the preceding material transfer speed setting value v1 to the plate speed. The motor speed control device controls the transfer speed to be changed to the set value V, hold the transfer speed until the target response time 1p, and change the transfer speed stepwise to the next transfer speed set value ν2 at the target response time t. A transfer speed control signal is output to 4. The motor speed control door device 4 controls the drive motor M based on the transfer speed control signal to control the transfer speed of the steel plate 11.
本発明に斯かる連続焼鈍炉の移送速度制御方法及び従来
の制御方法を用い、下記第1表に示す条件にて実際に移
送速度制御を行った。その結果を第4図のタイムチャー
トに示す。Using the method of controlling the transfer rate of a continuous annealing furnace according to the present invention and the conventional control method, the transfer rate was actually controlled under the conditions shown in Table 1 below. The results are shown in the time chart of FIG.
第 1 表
第4図は前記移送速度制御の結果を示すタイムチャート
であり、(a)〜(e)に示す各信号において実線は本
発明方法を示し、−点鎖線は従来の方法を示す。この図
から明らかな如く本発明方法によれば加熱帯出口板温は
従来より短くなっており、従来方法では6分間必要であ
った整定時間が2分に短縮された。Table 1 and FIG. 4 are time charts showing the results of the transfer speed control. In each of the signals shown in (a) to (e), the solid line indicates the method of the present invention, and the dashed line indicates the conventional method. As is clear from this figure, according to the method of the present invention, the plate temperature at the exit of the heating belt is shorter than that of the conventional method, and the settling time, which was required for the conventional method from 6 minutes, was shortened to 2 minutes.
(発明の効果〕
以上詳述した如く本発明に斯かる連続焼鈍炉の移送速度
制御方法においては、加熱炉出口板温を制御するために
移送速度を変更する場合、予め定められた目標応答時間
にて加熱炉出口板温が目標板温に安定するように移送速
度を制御することにより加熱炉出口板温がその目標値に
短時間で追従することが可能となる等本発明は優れた効
果を奏する。(Effects of the Invention) As detailed above, in the method for controlling the transfer speed of a continuous annealing furnace according to the present invention, when changing the transfer speed in order to control the plate temperature at the outlet of the heating furnace, the predetermined target response time is The present invention has excellent effects such as controlling the transfer speed so that the plate temperature at the outlet of the heating furnace is stabilized at the target plate temperature, so that the plate temperature at the outlet of the heating furnace can follow the target value in a short time. play.
第1図は本発明方法を実施する場合に用いる連続焼鈍炉
の加熱装置と移送速度制御系統を示す模式図、第2図は
移送速度の変化に帯する加熱炉出口板温の応答を示すタ
イムチャート、第3図は本発明に用いる移送速度制御の
タイムチャート、第4図は本発明方法を示すタイムチャ
ート、第5図は従来の移送速度制御のタイムチャートで
ある。
5・・・移送速度制御器
7・・・目標応答時間設定器
6・・・移送速度設定器
8・・・時定数設定器
特 許 出願人 住友金属工業株式会社代理人 弁理士
河 野 登 夫弔
図
弔
図
弔
図
弔
図Figure 1 is a schematic diagram showing the heating device and transfer rate control system of a continuous annealing furnace used when carrying out the method of the present invention, and Figure 2 is a time diagram showing the response of the plate temperature at the outlet of the heating furnace to changes in the transfer rate. 3 is a time chart of transfer speed control used in the present invention, FIG. 4 is a time chart showing the method of the present invention, and FIG. 5 is a time chart of conventional transfer speed control. 5... Transfer speed controller 7... Target response time setting device 6... Transfer speed setting device 8... Time constant setting device patent Applicant Sumitomo Metal Industries Co., Ltd. Agent Patent attorney Noboru Kono Funeral map Funeral map Funeral map Funeral map
Claims (1)
行材と次行材とを接合した帯材の温度制御を行うために
、該寸法、目標温度、材質により予め次行材の移送速度
を定め、この移送速度になすべく次行材の移送速度を制
御する連続焼鈍炉の移送速度制御方法において、前記次
行材の移送速度が先行材の移送速度 より速い場合は、次行材を前記移送速度より速い速度に
一旦保持した後、前記移送速度になすべく制御し、一方
次行材の移送速度が先行材の移送速度より遅い場合は、
次行材を前記移送速度より遅い速度に一旦保持した後、
次行材の移送速度になすべく制御することを特徴とする
連続焼鈍炉の移送速度制御方法。[Scope of Claims] 1. In order to control the temperature of a strip material made by joining a preceding material and a succeeding material that differ in at least one of dimensions, target temperature, and material, the next material is determined in advance according to the dimensions, target temperature, and material. In a continuous annealing furnace transfer speed control method that determines the transfer speed of a material and controls the transfer speed of the next material to achieve this transfer speed, when the transfer speed of the next material is faster than the transfer speed of the preceding material, Once the next material is held at a speed higher than the transfer speed, it is controlled to reach the transfer speed; on the other hand, if the transfer speed of the next material is slower than the transfer speed of the preceding material,
After once holding the next material at a speed lower than the transfer speed,
A method for controlling the transfer speed of a continuous annealing furnace, characterized by controlling the transfer speed of the next material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4496989A JPH02225626A (en) | 1989-02-23 | 1989-02-23 | Method for controlling transfer speed of continuous annealing furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4496989A JPH02225626A (en) | 1989-02-23 | 1989-02-23 | Method for controlling transfer speed of continuous annealing furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02225626A true JPH02225626A (en) | 1990-09-07 |
Family
ID=12706307
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4496989A Pending JPH02225626A (en) | 1989-02-23 | 1989-02-23 | Method for controlling transfer speed of continuous annealing furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02225626A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017133043A (en) * | 2016-01-25 | 2017-08-03 | Jfeスチール株式会社 | Center speed control method and device for continuous heat treatment line |
-
1989
- 1989-02-23 JP JP4496989A patent/JPH02225626A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2017133043A (en) * | 2016-01-25 | 2017-08-03 | Jfeスチール株式会社 | Center speed control method and device for continuous heat treatment line |
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