JPH06108166A - Method for controlling cooling - Google Patents

Method for controlling cooling

Info

Publication number
JPH06108166A
JPH06108166A JP4256909A JP25690992A JPH06108166A JP H06108166 A JPH06108166 A JP H06108166A JP 4256909 A JP4256909 A JP 4256909A JP 25690992 A JP25690992 A JP 25690992A JP H06108166 A JPH06108166 A JP H06108166A
Authority
JP
Japan
Prior art keywords
cooling
zone
strip
cooled
band
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
Application number
JP4256909A
Other languages
Japanese (ja)
Other versions
JP2803490B2 (en
Inventor
Kazutaka Tamura
和孝 田村
Akiyoshi Honda
昭芳 本田
Noboru Taguchi
昇 田口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP4256909A priority Critical patent/JP2803490B2/en
Publication of JPH06108166A publication Critical patent/JPH06108166A/en
Application granted granted Critical
Publication of JP2803490B2 publication Critical patent/JP2803490B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To restrain the strip temp. from exceeding the allowance range in a cooling zone and to improve the quality of a product by securing the stable cooling capacity operation while effectively utilizing a CC zone having a small cooling capacity in spite of various kind conditions of a material to be cooled. CONSTITUTION:In the cooling control method for cooling the material 2 to be cooled in the rapid cooling (GJC) zone using cooling gas blow 11 and the slow cooling (CC) zone using a cooling tube 12, when the cooling capacity of the material to be cooled passing through the slow cooling zone is lower than the max. furnace hearth load in the preset slow cooling zone, the strip temp. on the outlet side of the rapid cooling zone is controlled basing on the relation being almost proportional to the CC zone furnace hearth load. When the cooling capacity of the material to be cooled passing through the slow cooling zone according to the variation, etc., of various kind conditions of the material to be cooled exceeds the max. furnace hearth load, the strip temp. on the outlet side of the rapid cooling zone is obtd. basing on the preset max. furnace hearth load to control the strip temp. on the outlet side of the rapid cooling zone.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、連続溶融亜鉛メッキラ
インを初め、各種のストリップ移送ライン等に利用され
る冷却制御方法に係わり、特に急速冷却帯と徐冷帯とか
らなる冷却帯を移送する被冷却材の板厚や移送速度の変
更等に対し、徐冷帯の冷却能力を考慮しつつ被冷却材の
温度を適切に制御する機能をもった冷却制御方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cooling control method used for various strip transfer lines including a continuous hot-dip galvanizing line, and particularly for transferring a cooling zone composed of a rapid cooling zone and a slow cooling zone. The present invention relates to a cooling control method having a function of appropriately controlling the temperature of a material to be cooled while taking into consideration the cooling capacity of the slow cooling zone in response to changes in the plate thickness of the material to be cooled, transfer speed, and the like.

【0002】[0002]

【従来の技術】従来、ストリップを連続移送する連続移
送ラインのストリップを冷却するに際し、冷却ガスブロ
ーを用いた急速冷却帯{以下、GJC(Control Jet
Co-oling )帯と呼ぶ}と冷却チューブを用いた徐冷
帯 {以下、CC(ControlCooling)帯と呼ぶ}とで
構成される冷却帯を通すことにより、ストリップを所定
の温度に冷却することが行われている。
2. Description of the Related Art Conventionally, in cooling a strip in a continuous transfer line for continuously transferring the strip, a rapid cooling zone using a cooling gas blow {hereinafter, referred to as GJC (Control Jet)
The strip can be cooled to a predetermined temperature by passing it through a cooling zone composed of a "Col-oling) zone" and a slow cooling zone (hereinafter referred to as "CC (Control Cooling) zone") using a cooling tube. Has been done.

【0003】ところで、このような連続移送ラインにお
いては、GJC帯とCC帯とではその用途,機能等の観
点からそれぞれ冷却能力が異なる。例えばGJC帯の場
合には、冷却能力が大きいが、ストリップの巾方向に温
度ムラが発生しやすい。これに対し、CC帯の場合に
は、冷却能力が小さいが、ストリップの巾方向,長手方
向に均一な温度が得られる。
By the way, in such a continuous transfer line, the cooling capacity is different between the GJC band and the CC band from the viewpoints of their applications and functions. For example, in the case of the GJC band, the cooling capacity is large, but temperature unevenness easily occurs in the width direction of the strip. On the other hand, in the case of the CC band, although the cooling capacity is small, a uniform temperature can be obtained in the width direction and the length direction of the strip.

【0004】そこで、この種のストリップ移送ラインで
は、各冷却帯の冷却能力を考慮しつつ、鋼種の冷却条件
を満足し、かつ、均一の冷却を行うために、ラインの前
段側にGJC帯を設置してストリップを大きく冷却する
一方、ラインの後段側にCC帯を設置して均一冷却を行
う冷却制御方法が採用されている。その1つとして、例
えば連続溶融鍍金ラインの冷却制御方法が上げられ、後
記する図1に示すような冷却炉が用いられている。
Therefore, in this type of strip transfer line, in order to satisfy the cooling conditions of the steel types and to perform uniform cooling while considering the cooling capacity of each cooling zone, a GJC zone is provided on the upstream side of the line. A cooling control method is adopted in which a strip is installed and the strip is cooled significantly, while a CC band is installed on the downstream side of the line for uniform cooling. As one of them, for example, a cooling control method for a continuous melting plating line is proposed, and a cooling furnace as shown in FIG. 1 described later is used.

【0005】この鍍金ラインの冷却炉は、ストリップが
冷却炉を構成するGJC帯を通過するが、このとき冷却
ガスブローから冷却ガスをストリップに当てて強制対流
伝達冷却を行う他、炉壁とストリップとの輻射伝熱冷却
を行うことにより、入り側と出側とのストリップの冷却
温度差を約200°Cとなるように冷却する。引き続
き、ストリップがGJC帯から冷却炉を構成するCC帯
に移行するが、ここでは主として炉壁とストリップとの
輻射伝熱冷却を行うことにより、入り側と出側とのスト
リップの温度差がGJC帯よりも一般に冷却能力の小さ
い約100°Cとなるように冷却する。
In the cooling furnace of this plating line, the strip passes through the GJC band which constitutes the cooling furnace. At this time, the cooling gas is applied from the cooling gas blow to the strip for forced convection transfer cooling, and the furnace wall and the strip. The radiant heat transfer cooling is performed so that the cooling temperature difference between the strip on the inlet side and the strip on the outlet side is about 200 ° C. Subsequently, the strip moves from the GJC zone to the CC zone which constitutes the cooling furnace. Here, the temperature difference between the strip on the inlet side and the strip on the outlet side is GJC because the heat transfer cooling is mainly performed between the furnace wall and the strip. Cooling is performed to about 100 ° C., which generally has a smaller cooling capacity than the strip.

【0006】[0006]

【発明が解決しようとする課題】しかし、以上のような
CC帯では、輻射伝熱冷却であるので、炉温下限値によ
る冷却可能熱量に制約があり、このような冷却可能熱量
の制約は同時に単位巾当りの冷却熱量に対する制約(こ
れを炉床負荷と呼ぶ)となる。そのため、炉床負荷制約
によりCC帯で取り去るべき冷却熱量の上限値が決定さ
れる。一方、GJC帯では、そのGJC帯出側の目標板
温度が固定となつている。その結果、連続移送ラインに
おけるストリップの冷却温度の制御に対し、次のような
問題が生じてくる。
However, in the CC band as described above, since radiation heat transfer cooling is used, there is a limit to the amount of heat that can be cooled by the furnace temperature lower limit value. This is a constraint on the amount of cooling heat per unit width (this is called the hearth load). Therefore, the upper limit of the amount of cooling heat to be removed in the CC band is determined by the hearth load constraint. On the other hand, in the GJC band, the target plate temperature on the GJC band exit side is fixed. As a result, the following problems arise in controlling the cooling temperature of the strip in the continuous transfer line.

【0007】すなわち、ストリップのサイズ(例えば板
厚,板巾等)や移送速度の変更時、前述したようにCC
帯の冷却熱量に制約があることから、CC帯出側で所要
とする冷却温度から外れる,いわゆる板温外れが発生す
る。そこで、この板温外れを回避するために、オペレー
タが思考錯誤的にストリップの移送速度、時にはGJC
帯出側の目標板温度を可変するように人為的に操作して
いるが、能率(ton/hr)ダウンは否めず、また操
作ミスによって同様に板温外れが発生し、製品の品質に
も悪影響を与える問題がある。
That is, when the strip size (eg, plate thickness, plate width, etc.) or the transfer speed is changed, the CC
Since there is a restriction on the amount of cooling heat of the zone, so-called plate temperature deviation occurs, which is outside the required cooling temperature on the CC zone exit side. Therefore, in order to avoid this plate temperature deviation, the operator erroneously thinks about the strip transfer speed and sometimes the GJC.
Although it is artificially operated to change the target plate temperature on the take-out side, efficiency (ton / hr) down is unavoidable, and the plate temperature is also off due to an operation error, which adversely affects the product quality. There is a problem giving.

【0008】本発明は上記実情に鑑みてなされたもの
で、CC帯の冷却熱量特性を考慮しつつGJC帯出側の
板温度を制御することにより、被冷却材の種々の条件の
変更にもかかわらず、CC帯による最適な冷却熱量運転
を可能にし、よって冷却帯の板温外れを抑制し、製品の
品質向上に大きく寄与する冷却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-mentioned circumstances, and it is possible to change various conditions of the material to be cooled by controlling the plate temperature on the outlet side of the GJC band while considering the cooling heat quantity characteristic of the CC band. It is an object of the present invention to provide a cooling control method that enables optimum cooling heat quantity operation in the CC band, suppresses plate temperature deviation in the cooling band, and greatly contributes to product quality improvement.

【0009】[0009]

【課題を解決するための手段】上記課題を解決するため
に、請求項1に対応する発明は、冷却ガスブローを用い
たGJC帯と冷却チューブを用いたCC帯とによって被
冷却材を冷却する冷却制御方法において、前記CC帯の
冷却熱量特性と少なくとも被冷却材の移送速度,密度お
よび比熱等とから前記GJC帯の出側板温度を求め、前
記GJC帯の出側板温度を制御する冷却制御方法であ
る。
In order to solve the above problems, the invention according to claim 1 is a cooling system for cooling a material to be cooled by a GJC band using a cooling gas blow and a CC band using a cooling tube. In the control method, a cooling control method for determining the outlet plate temperature of the GJC band from the cooling heat quantity characteristic of the CC band and at least the transfer speed, density, specific heat and the like of the material to be cooled, and controlling the outlet plate temperature of the GJC band. is there.

【0010】次に、請求項2に対応する発明は、冷却ガ
スブローを用いたGJC帯と冷却チューブを用いたCC
帯とによって被冷却材を冷却する冷却制御方法におい
て、予めCC帯の最大炉床負荷が設定され、前記CC帯
を通過する被冷却材の冷却熱量が前記最大炉床負荷以下
のとき、CC帯炉床負荷にほぼ比例する関係で前記GJ
C帯の出側板温度を制御し、一方、被冷却材の種々の条
件の変更等に伴って前記CC帯を通過する被冷却材の冷
却熱量が前記最大炉床負荷を越えたとき、予め設定され
た最大炉床負荷に基づいて前記GJC帯の出側板温度を
求め、GJC帯の出側板温度を制御する冷却制御方法で
ある。
Next, the invention corresponding to claim 2 is a GJC band using a cooling gas blow and a CC using a cooling tube.
In the cooling control method of cooling the cooled material by the zone, the maximum hearth load of the CC zone is set in advance, when the cooling heat amount of the cooled material passing through the CC zone is less than or equal to the maximum hearth load, the CC zone The GJ is almost proportional to the hearth load.
When the outlet plate temperature of the C zone is controlled and the cooling heat amount of the cooled material passing through the CC zone exceeds the maximum hearth load due to changes in various conditions of the cooled material, etc., it is preset. This is a cooling control method in which the outlet plate temperature of the GJC band is obtained based on the maximum hearth load, and the outlet plate temperature of the GJC band is controlled.

【0011】[0011]

【作用】従って、請求項1の発明は以上のような手段を
講じたことにより、冷却能力の小さいCC帯の冷却熱量
特性と被冷却材の種々の条件の変更とを考慮しつつ、G
JC帯の出側板温度を決定するので、CC帯の冷却不足
をカバーでき、板温外れを抑えることができる。
Therefore, according to the invention of claim 1, by taking the measures as described above, the G heat quantity characteristic of the CC band having a small cooling capacity and the change of various conditions of the material to be cooled are taken into consideration.
Since the outlet plate temperature of the JC band is determined, it is possible to cover the insufficient cooling of the CC band and suppress the plate temperature deviation.

【0012】次に、請求項2に対応する発明は、CC帯
を通過する被冷却材の冷却熱量が最大炉床負荷以下のと
き、CC帯炉床負荷と比例するようにGJC帯の出側板
温度を制御し、被冷却材の種々の条件の変更に伴ってC
C帯を通過する被冷却材の冷却熱量が最大炉床負荷を越
えたとき、そのCC帯で取り去れない熱量分だけGJC
帯の出側板温度を下げることにより、冷却能力の小さい
CC帯を最適な状態で安定操業を行うことができ、よっ
て板温外れを未然に回避でき、高品質の被冷却材料を得
ることができる。本発明は、特に溶融亜鉛鍍金ラインの
ように、冷却帯出側板温を精度よく制御する場合に効果
が大きい。
Next, the invention according to claim 2 is, when the cooling heat amount of the material to be cooled passing through the CC zone is less than the maximum hearth load, the outlet plate of the GJC zone so as to be proportional to the CC zone hearth load. The temperature is controlled, and C changes with changes in various conditions of the material to be cooled.
When the amount of cooling heat of the material to be cooled that passes through the C zone exceeds the maximum hearth load, the amount of heat that cannot be removed in the CC zone is GJC.
By lowering the temperature of the strip output side plate, stable operation of the CC band having a small cooling capacity can be performed in an optimal state, so that the plate temperature deviation can be avoided in advance and a high quality cooled material can be obtained. . INDUSTRIAL APPLICABILITY The present invention is particularly effective in the case of controlling the cooling zone outlet side plate temperature with high accuracy, as in a molten zinc plating line.

【0013】[0013]

【実施例】以下、本発明に係わる冷却制御方法の一実施
例を説明する。
EXAMPLE An example of the cooling control method according to the present invention will be described below.

【0014】GJC帯とCC帯とを組合わせた冷却帯に
ついては、冷却能力の小さいCC帯の冷却熱量特性に十
分な注意を払いつつ冷却制御を行う必要がある。そこ
で、本発明においては、次のような制御方法および知見
に基づいて実施する。
For the cooling zone in which the GJC zone and the CC zone are combined, it is necessary to perform cooling control while paying sufficient attention to the cooling heat quantity characteristic of the CC zone having a small cooling capacity. Therefore, the present invention is implemented based on the following control method and knowledge.

【0015】(1) 先ず、制御方法は、冷却能力の小
さいCC帯を有効に運転させるために、CC帯の冷却熱
量特性に基づいて2つに分けて考える。その1つは、C
C帯の有する冷却熱量上限(最大炉床負荷)までの有効
利用であり、さらに他の1つはCC帯の冷却熱量の制約
となる上限値,つまり最大炉床負荷を越えたときの対策
を考える必要がある。
(1) First, regarding the control method, in order to effectively operate the CC band having a small cooling capacity, the control method is divided into two parts based on the cooling heat quantity characteristic of the CC band. One of them is C
It is effective utilization up to the upper limit of cooling heat (maximum hearth load) of the C band, and the other one is to take measures when the upper limit of the cooling heat amount of the CC band, that is, the maximum hearth load is exceeded. I need to think.

【0016】そこで、GJC帯においては、CC帯の冷
却熱量上限に至るまでCC帯の炉床負荷に比例するよう
なGJC帯出側板温度に設定すること。一方、CC帯の
最大炉床負荷を越えたとき、CC帯で冷却熱量分を取り
去れないので、このときGJC帯では、CC帯で取り去
れない冷却熱量分だけ、GJC帯出側の板温度を下げる
ことにより、冷却熱量をカバーするような制御方法を実
施する。
Therefore, in the GJC zone, the GJC zone outlet side plate temperature is set so as to be proportional to the CC zone hearth load up to the CC zone cooling heat amount upper limit. On the other hand, when the maximum hearth load of the CC zone is exceeded, the cooling heat amount cannot be removed in the CC zone. At this time, therefore, in the GJC zone, the plate temperature on the outlet side of the GJC zone is changed by the cooling heat amount that cannot be removed in the CC zone. By lowering it, a control method that covers the cooling heat amount is implemented.

【0017】(2) 次に、ストリップのサイズや移送
速度を変更したとき、CC帯出側の板温度を一定の目標
値とするため、GJC帯出側の目標板温度を変化させる
必要があるが、このとき冷却炉の冷却途中過程であるG
JC帯出側板温度が広い許容温度範囲で操業できるかが
問題となる。
(2) Next, it is necessary to change the target plate temperature on the GJC banding side in order to set the plate temperature on the CC banding side to a constant target value when the size of the strip or the transfer speed is changed. At this time, G which is in the process of cooling the cooling furnace
The issue is whether the JC strip outlet side plate temperature can be operated within a wide allowable temperature range.

【0018】因みに、例えば溶融亜鉛鍍金ラインにおい
ては、CC帯出側の板温度が約±10°Cであるのに較
べ、GJC帯側の板温度が約±40°Cのように非常に
広い許容温度範囲をもっている。ゆえに、このようにス
トリップ移送ラインでは、GJC帯とCC帯とで1つの
冷却炉と見なし、GJC帯出側の板温度を管理してもス
トリップの材質上には何ら問題が生じない。
Incidentally, for example, in a hot dip galvanizing line, the plate temperature on the GJC band side is about ± 40 ° C, while the plate temperature on the CC band outlet side is about ± 10 ° C. Has a temperature range. Therefore, in the strip transfer line, even if the GJC zone and the CC zone are regarded as one cooling furnace and the plate temperature on the GJC zone exit side is controlled, no problem occurs in the material of the strip.

【0019】そこで、本発明方法は、前記(2)の知見
を踏まえつつ、前記(1)のような冷却制御方法を実施
するが、このときGJC帯出側の板温度は、CC帯の冷
却熱量特性の他、ストリップの移送速度,密度,比熱等
を含む下記の関係式から決定する。
Therefore, the method of the present invention implements the cooling control method as described in the above (1) based on the knowledge of the above (2). At this time, the plate temperature on the GJC zone exit side is the cooling heat quantity of the CC zone. In addition to the characteristics, it is determined from the following relational expressions including strip transfer speed, density, specific heat, etc.

【0020】すなわち、このGJC帯出側の板温度の決
定に際し、ストリップの板厚,板巾および移送速度から
CC帯を通過するストリップの冷却熱量Q[k cal/h
r]を計算し、このCC帯の冷却熱量Qが最大炉床負荷
Qmax [k cal/hr・m ]以下ならば、CC帯の冷却能
力(ton /hr)にほぼ比例する冷却熱量となる板温度を
設定する。つまり、 単位巾当たりの冷却熱量Q/W[k cal/hr・m ]≦炉
床負荷Qmax [k cal/hr・m ]の時、 TGJ=TCC+(K/Cp ) …… (1) なる関係式からGJC帯出側板温度TGJ(°C)を決定
する。
That is, in determining the strip temperature on the GJC strip exit side, the cooling heat quantity Q [k cal / h] of the strip passing through the CC strip is determined from the strip thickness, strip width and transfer speed.
r], and if the cooling heat quantity Q of this CC band is equal to or less than the maximum hearth load Qmax [k cal / hr · m], the plate will have a cooling heat quantity almost proportional to the cooling capacity (ton / hr) of the CC band. Set the temperature. That is, when the amount of cooling heat per unit width Q / W [kcal / hr · m] ≦ hearth load Qmax [kcal / hr · m], T GJ = T CC + (K / C p ) ... ( 1) Determine the GJC strip output side plate temperature T GJ (° C) from the following relational expression.

【0021】但し、TCC(°C):CC帯目標板温度、
K:定数(冷却熱量とton /hrとの比例定数)、ρ
Fe[kg/m 3 ]:ストリップの密度、Cp [k cal/kg
・k]:ストリップの比熱である。一方、CC帯の冷却
熱量Qが最大炉床負荷Qmax [k cal/hr・m ]を越え
たならば、冷却熱量をQmax とし、GJC帯出側の板温
度を決定する。つまり、 単位巾当たりの冷却熱量Q/W[k cal/hr・m ]>炉
床負荷Qmax [k cal/hr・m ]の時、 TGJ=TCC+{Qmax /(t・v・ρFe・Cp )} …… (2) なる関係式からGJC帯出側の板温度TGJ(°C)を決
定する。但し、Qmax [k cal/hr・m ]:炉床負荷、
t[m]:板厚、v[m /hr]:移送速度である。
However, T CC (° C): CC band target plate temperature,
K: constant (proportional constant between cooling heat quantity and ton / hr), ρ
Fe [kg / m 3 ]: Density of the strip, C p [k cal / kg
• k]: Specific heat of the strip. On the other hand, when the cooling heat quantity Q in the CC band exceeds the maximum hearth load Qmax [kcal / hr · m], the cooling heat quantity is set to Qmax and the plate temperature on the GJC band exit side is determined. That is, when the cooling heat quantity per unit width Q / W [kcal / hr · m]> hearth load Qmax [kcal / hr · m], T GJ = T CC + {Qmax / (t · v · ρ Fe · C p )} (2) Determine the plate temperature T GJ (° C) on the GJC banding side from the following relational expression. However, Qmax [kcal / hr · m]: hearth load,
t [m]: plate thickness, v [m 2 / hr]: transfer speed.

【0022】従って、以上のような冷却制御方法を採用
することにより、CC帯を通過するストリップの冷却熱
量が最大炉床負荷以下の場合にはCC帯の炉床負荷に比
例してGJC帯出側の板温度を設定するとともに、例え
ばストリップのサイズや移送速度等の条件の変更等に伴
ってCC帯のストリップの冷却熱量が最大炉床負荷を越
えたとき、CC帯で取り去る冷却熱量の上限値,つまり
最大炉床負荷とし、GJC帯出側板温度を設定するの
で、冷却能力の小さいCC帯であっても最適な条件の下
に安定操業を行うことができ、これによってストリップ
長手方向の板温外れを抑えることができ、しかも、スト
リップ巾方向の温度を均一化して高品質なストリップを
得ることができる。
Therefore, by adopting the cooling control method as described above, when the cooling heat quantity of the strip passing through the CC zone is less than the maximum hearth load, the GJC zone exit side is proportional to the CC zone hearth load. The upper limit of the cooling heat quantity to be removed in the CC zone when the cooling heat quantity of the strip in the CC zone exceeds the maximum hearth load due to changes in conditions such as strip size and transfer speed, etc. That is, since the maximum hearth load is set and the GJC zone outlet side plate temperature is set, stable operation can be performed under optimal conditions even in the CC zone with a small cooling capacity. In addition, the temperature in the strip width direction can be made uniform and a high quality strip can be obtained.

【0023】次に、以上のような冷却制御方法を適用し
た装置について図1および図2を参照して説明する。な
お、図1は溶融亜鉛鍍金ラインその他のストリップ連続
移送ライン等に用いる冷却炉の構成を示す図、図2は冷
却炉を含む冷却温度制御装置の構成を示す図である。
Next, an apparatus to which the above cooling control method is applied will be described with reference to FIGS. 1 and 2. 1 is a diagram showing the configuration of a cooling furnace used in a molten zinc plating line and other continuous strip transfer lines, and FIG. 2 is a diagram showing the configuration of a cooling temperature control device including the cooling furnace.

【0024】すなわち、かかる冷却炉は、GJC帯とC
C帯とが適宜な形態をもって連なるように構成され、こ
れらGJC帯内およびCC帯内には所要とする位置関係
をもってガイドロール1,…を配置することにより、ス
トリップ2がガイドロール1,…を介して蛇行状を形成
するような移送ラインを構成する。そして、GJC帯お
よびCC帯の各出側にはそれぞれ温度計3,4が設置さ
れている。5は炉の形態を現す炉殻である。
That is, such a cooling furnace has a GJC band and a C
The strips 2 are arranged so as to be connected to the C band in an appropriate form, and the guide rolls 1, ... Are arranged in the GJC band and the CC band with a required positional relationship, so that the strip 2 guides the guide rolls 1 ,. A transfer line is formed so as to form a meandering shape. Then, thermometers 3 and 4 are installed on the respective output sides of the GJC band and the CC band. Reference numeral 5 is a furnace shell representing the form of the furnace.

【0025】次に、冷却炉を含む冷却温度制御装置は、
図2に示すようにGJC帯の入り側および出側にはそれ
ぞれガスブロー11,11が設置され、外部からそれぞ
れ圧力調節弁21,21を介して送られてくる冷却ガス
媒体を前記ガスブロー11,11を用いてストリップ2
に噴射する構成をなし、一方、CC帯側の入り側および
出側にはそれぞれ冷却チューブ12,12が配置され、
同じく外部からそれぞれ流量調節弁31,31を経由し
て送られてくる冷却媒体を冷却チューブ12,12を通
すことにより、輻射伝達冷却を行う構成となっている。
Next, the cooling temperature control device including the cooling furnace is
As shown in FIG. 2, gas blowers 11 and 11 are installed on the inlet side and the outlet side of the GJC band, respectively, and the cooling gas mediums sent from the outside through the pressure control valves 21 and 21 are supplied to the gas blowers 11 and 11, respectively. With strip 2
On the other hand, cooling tubes 12, 12 are arranged on the inlet side and the outlet side of the CC band side, respectively.
Similarly, the cooling mediums sent from the outside via the flow rate control valves 31 and 31, respectively, are passed through the cooling tubes 12 to perform radiation transfer cooling.

【0026】この冷却温度制御装置20は、カスケード
制御+フィードフォワード制御の組合わせ構成を有し、
具体的には外乱要素となるストリップサイズや移送速度
を取り込み、その他必要なパラメータおよび定数等を用
いて、前記(1)式および(2)式の計算その他所要と
する計算を行ってGJC帯およびCC帯の目標板温度を
求めるプロセスコンピユータ等を用いた目標板温度演算
部30と、この目標板温度演算部30によって求められ
たGJC帯側目標板温度とGJC帯出側温度計3で検出
されたGJC帯出側検出温度との偏差に基づいて例えば
PIまたはPID等の調節演算を行ってGJC帯出側目
標圧力を求める温度調節計22と、同じく目標板温度演
算部30によって求められたCC帯側目標板温度とCC
帯出側温度計4で検出されたCC帯出側検出温度との偏
差に基づいて例えばPIまたはPID等の調節演算を行
ってCC帯出側目標流量を求める流量調節計32とが設
けられている。
The cooling temperature control device 20 has a combination configuration of cascade control + feedforward control,
Specifically, the strip size and the transfer velocity, which are disturbance factors, are taken in, and other necessary parameters and constants are used to perform the calculations of the above formulas (1) and (2) and other required calculations to determine the GJC band and The target plate temperature calculation unit 30 using a process computer or the like for obtaining the target plate temperature in the CC band, the GJC band side target plate temperature calculated by the target plate temperature calculation unit 30 and the GJC band output side thermometer 3 are detected. A temperature controller 22 for obtaining a GJC strip output side target pressure by performing an adjustment calculation such as PI or PID based on a deviation from the GJC strip output side detected temperature, and a CC band side target similarly obtained by the target plate temperature calculation unit 30. Plate temperature and CC
There is provided a flow rate controller 32 for obtaining a CC output side target flow rate by performing an adjustment calculation such as PI or PID based on the deviation from the CC output side detected temperature detected by the output side thermometer 4.

【0027】さらに、この冷却温度制御装置は、前記目
標圧力とGJC帯入り側および出側の冷却ガス媒体供給
路に設けられた圧力検出器23,24からの吐出圧力と
に基づいて所要とする圧力操作信号を出力する圧力調節
計25,26と、前記目標流量とCC帯入り側および出
側の冷却媒体供給路に設けられた流量検出器33,34
からの検出流量とに基づいて所要とする流量操作信号を
出力する流量調節計35,36とが設けられ、前記圧力
調節計35,36からの圧力操作信号に基づいて圧力調
節弁21,21を操作し、一方、流量調節計35,36
からの流量操作信号に基づいて流量調節弁31,31を
操作する構成となっている。
Further, this cooling temperature control device is required based on the target pressure and the discharge pressures from the pressure detectors 23 and 24 provided in the cooling gas medium supply passages on the GJC zone inlet side and the outlet side. Pressure regulators 25 and 26 that output pressure operation signals, and flow rate detectors 33 and 34 that are provided in the target medium flow rate and the cooling medium supply path on the CC band inlet side and outlet side
Flow rate controllers 35 and 36 for outputting a required flow rate operation signal based on the detected flow rate from the pressure regulators 35 and 36, and the pressure control valves 21 and 21 are operated based on the pressure operation signals from the pressure regulators 35 and 36. Operate, while the flow controller 35,36
The flow rate control valves 31 and 31 are operated based on the flow rate control signal from.

【0028】従って、以上のような本発明の冷却制御方
法および冷却温度制御装置を適用しない従来のものは、
図3(a)に示す如く時刻t1においてストリップの移
送速度が増加したとき、冷却熱量をアップそせる必要が
あるにも拘らず、GJC帯目標板温度,実績温度が同じ
であるので、CC帯では冷却能力の上限値オーバーとな
って冷却できない。このため、CC帯出側において実績
温度が上昇し、板温外れが発生する。
Therefore, the conventional ones to which the cooling control method and the cooling temperature control device of the present invention as described above are not applied,
As shown in FIG. 3 (a), when the strip transport speed increases at time t1, the GJC band target plate temperature and the actual temperature are the same, even though the cooling heat amount needs to be increased. Then, the upper limit of the cooling capacity is exceeded and cooling cannot be performed. Therefore, the actual temperature rises on the CC band exit side, and the plate temperature deviation occurs.

【0029】これに対し、本発明の冷却制御方法および
冷却温度制御装置によれば、図3(b)に示すようにス
トリップの移送速度の増加によってCC帯の冷却能力の
上限を越えたとき、GJC出側の目標板温度を下げるこ
とにより、CC帯出側板温度は目標板温度に追従される
ことができ、移送速度の変更によってストリップの品質
に影響を与えることがなくなる。これは、ストリップの
移送速度だけでなく、ストリップサイズの変更その他の
外乱要素においても同様であることはいうまでもない。
On the other hand, according to the cooling control method and the cooling temperature control device of the present invention, when the upper limit of the cooling capacity of the CC band is exceeded due to the increase of the transfer speed of the strip as shown in FIG. 3 (b), By lowering the target plate temperature on the GJC outlet side, the CC strip outlet side plate temperature can be made to follow the target plate temperature, and the strip quality is not affected by changing the transfer speed. It goes without saying that this applies not only to the transfer speed of the strip, but also to changes in the strip size and other disturbance factors.

【0030】次に、図4はストリップの移送速度85r
pm一定とし、かつ、ストリップのサイズを、イ−板厚
0.66×板幅1280mm、ロ−板厚0.81×板幅1
213mm、ハ−板厚0.71×板幅1130mmの順序で
変更したときのGJC帯目標板温度と実績温度、CC帯
目標板温度と実績温度との関係を示す図である。
Next, FIG. 4 shows the strip transfer speed 85r.
pm is constant, and the strip size is as follows: a plate thickness 0.66 x plate width 1280 mm, roll plate thickness 0.81 x plate width 1
It is a figure which shows the relationship of GJC zone target board temperature and actual temperature, and CC zone target board temperature and actual temperature when it changes in the order of 213 mm, Har plate thickness 0.71 x board width 1130 mm.

【0031】つまり、この冷却制御は、ストリップのサ
イズを変更するごとに、CC帯目標板温度を変更し、か
つ、このCC帯目標板温度を変更するごとに最適なGJ
C帯目標板温度を設定することにあり、これによってC
C帯の目標板温度が良好に追従していることが分かり、
冷却能力の小さいCC帯であっても最適な運転を確保す
ることができる。なお、本発明はその要旨を逸脱しない
範囲で種々変形して実施できる。
That is, in this cooling control, the CC band target plate temperature is changed each time the strip size is changed, and the optimum GJ is changed each time the CC band target plate temperature is changed.
The purpose is to set the C-band target plate temperature.
It can be seen that the target plate temperature in the C band follows well,
Optimal operation can be secured even in the CC band having a small cooling capacity. The present invention can be variously modified and implemented without departing from the scope of the invention.

【0032】[0032]

【発明の効果】以上説明したように本発明によれば、C
C帯の冷却熱量の制約に合わせてGJC帯出側の被冷却
材の温度を制御することにより、被冷却材の種々の条件
の変更にもかかわらず、冷却能力の小さいCC帯を有効
に生かしつつ安定な冷却熱量運転を確保でき、よって冷
却帯の板温外れを抑えることができ、製品の品質向上に
大きく寄与させうる冷却制御方法を提供できる。
As described above, according to the present invention, C
By controlling the temperature of the cooled material on the GJC strip exit side in accordance with the restriction of the cooling heat quantity of the C zone, while effectively changing the various conditions of the cooled material, the CC zone with a small cooling capacity can be effectively used. It is possible to provide a cooling control method which can ensure stable cooling heat quantity operation, can suppress the plate temperature deviation in the cooling zone, and can greatly contribute to the improvement of product quality.

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

【図1】 本発明に係わる冷却制御方法を適用する冷却
炉の構成を示す図。
FIG. 1 is a diagram showing a configuration of a cooling furnace to which a cooling control method according to the present invention is applied.

【図2】 本発明方法を適用した冷却炉を含む冷却温度
制御装置の構成図。
FIG. 2 is a configuration diagram of a cooling temperature control device including a cooling furnace to which the method of the present invention is applied.

【図3】 本発明方法の適用の有無による板温度状態を
説明する図。
FIG. 3 is a diagram for explaining a plate temperature state depending on whether or not the method of the present invention is applied.

【図4】 ストリップのサイズ変更に伴うCC帯とGJ
C帯の目標板温度と実績値との変化状態を説明する図。
[Fig. 4] CC band and GJ accompanying strip size change
The figure explaining the change state of the target board temperature and actual value of C zone.

【符号の説明】[Explanation of symbols]

2…ストリップ(被冷却材)、3,4…温度計、11…
ガイブロー、12…冷却チューブ、20…冷却温度制御
装置、22…温度調節計、23,24…圧力検出器、2
5,26…圧力調節計、30…目標板温度演算部、32
…温度調節計、33,34…流量検出器、35,36…
流量調節計。
2 ... Strip (material to be cooled), 3, 4 ... Thermometer, 11 ...
Guy blow, 12 ... Cooling tube, 20 ... Cooling temperature control device, 22 ... Temperature controller, 23, 24 ... Pressure detector, 2
5, 26 ... Pressure controller, 30 ... Target plate temperature calculation unit, 32
... Temperature controller, 33,34 ... Flow rate detector, 35,36 ...
Flow controller.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 冷却ガスブローを用いた急速冷却帯と冷
却チューブを用いた徐冷帯とによって被冷却材を冷却す
る冷却制御方法において、 前記徐冷帯の冷却熱量特性と少なくとも被冷却材の移送
速度,密度および比熱等とから前記急速冷却帯の出側板
温度を求め、前記急速冷却帯の出側板温度を制御するこ
とを特徴とする冷却制御方法。
1. A cooling control method for cooling a material to be cooled by a rapid cooling zone using a cooling gas blow and a slow cooling zone using a cooling tube, wherein the cooling heat quantity characteristic of the slow cooling zone and at least the transfer of the material to be cooled. A cooling control method, characterized in that the outlet plate temperature of the rapid cooling zone is obtained from the speed, density, specific heat, etc., and the outlet plate temperature of the rapid cooling zone is controlled.
【請求項2】 冷却ガスブローを用いた急速冷却帯と冷
却チューブを用いた徐冷帯とによって被冷却材を冷却す
る冷却制御方法において、 予め徐冷帯の最大炉床負荷が設定され、前記徐冷帯を通
過する被冷却材の冷却熱量が前記最大炉床負荷以下のと
き、CC帯炉床負荷にほぼ比例する関係をもって前記急
速冷却帯の出側板温度を制御し、一方、被冷却材の種々
の条件の変更等に伴って前記徐冷帯を通過する被冷却材
の冷却熱量が前記最大炉床負荷を越えたとき、予め設定
された最大炉床負荷に基づいて前記急速冷却帯の出側板
温度を求め、前記急速冷却帯の出側板温度を制御するこ
とを特徴とする冷却制御方法。
2. A cooling control method for cooling a material to be cooled by a rapid cooling zone using a cooling gas blow and an annealing zone using a cooling tube, wherein a maximum hearth load of the annealing zone is set in advance, When the cooling heat amount of the cooled material passing through the cold zone is less than or equal to the maximum hearth load, the outlet plate temperature of the rapid cooling zone is controlled in a relationship substantially proportional to the CC zone hearth load, while When the cooling heat amount of the cooled material passing through the slow cooling zone exceeds the maximum hearth load due to changes in various conditions, etc., the output of the rapid cooling zone is set based on the preset maximum hearth load. A cooling control method, wherein the side plate temperature is obtained and the outlet plate temperature of the rapid cooling zone is controlled.
JP4256909A 1992-09-25 1992-09-25 Cooling control method Expired - Fee Related JP2803490B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4256909A JP2803490B2 (en) 1992-09-25 1992-09-25 Cooling control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4256909A JP2803490B2 (en) 1992-09-25 1992-09-25 Cooling control method

Publications (2)

Publication Number Publication Date
JPH06108166A true JPH06108166A (en) 1994-04-19
JP2803490B2 JP2803490B2 (en) 1998-09-24

Family

ID=17299074

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4256909A Expired - Fee Related JP2803490B2 (en) 1992-09-25 1992-09-25 Cooling control method

Country Status (1)

Country Link
JP (1) JP2803490B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008255414A (en) * 2007-04-04 2008-10-23 Nippon Steel Engineering Co Ltd Method for cooling steel sheet and steel sheet continuous heat-treatment facility
RU2605883C1 (en) * 2015-06-24 2016-12-27 Общество с ограниченной ответственностью ХОЗРАСЧЕТНЫЙ ТВОРЧЕСКИЙ ЦЕНТР УФИМСКОГО АВИАЦИОННОГО ИНСТИТУТА Hardening medium cooling ability determining device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6317895A (en) * 1986-07-11 1988-01-25 Wako Pure Chem Ind Ltd Novel oligosaccharide derivative and determination of alpha-amylase activity using same

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6317895A (en) * 1986-07-11 1988-01-25 Wako Pure Chem Ind Ltd Novel oligosaccharide derivative and determination of alpha-amylase activity using same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008255414A (en) * 2007-04-04 2008-10-23 Nippon Steel Engineering Co Ltd Method for cooling steel sheet and steel sheet continuous heat-treatment facility
RU2605883C1 (en) * 2015-06-24 2016-12-27 Общество с ограниченной ответственностью ХОЗРАСЧЕТНЫЙ ТВОРЧЕСКИЙ ЦЕНТР УФИМСКОГО АВИАЦИОННОГО ИНСТИТУТА Hardening medium cooling ability determining device

Also Published As

Publication number Publication date
JP2803490B2 (en) 1998-09-24

Similar Documents

Publication Publication Date Title
US4440583A (en) Method of controlled cooling for steel strip
US4836774A (en) Method and apparatus for heating a strip of metallic material in a continuous annealing furnace
JPS6314052B2 (en)
JPH06108166A (en) Method for controlling cooling
JPH03207821A (en) Controlling method for cooling strip in cooling zone of continuous annealing
US4725321A (en) Method for cooling a steel strip in a continuous annealing furnace
JP4894686B2 (en) Manufacturing method and manufacturing apparatus for hot-rolled steel sheet
US4724014A (en) Method for cooling a steel strip in a continuous annealing furnace
EP0128734B1 (en) Method for cooling a steel strip in a continuous-annealing furnace
JP2988330B2 (en) Control method of winding temperature of hot rolled steel sheet
JPH0564687B2 (en)
JP7052671B2 (en) Metal band temperature control method and temperature control device
JPS639569B2 (en)
JPH0347924A (en) Method for controlling inner pressure in continuous annealing furnace
JPS6345454B2 (en)
JP4088115B2 (en) Steel strip cooling control method
JP2979908B2 (en) Metal strip cooling device
JPS6160901B2 (en)
JPS60159127A (en) Method for controlling cooling of steel strip in continuous annealing installation
JPH07278682A (en) Sheet temperature control method of continuous heating furnace
JPS61199038A (en) Method for controlling temperature of strip in continuous annealing furnace
JPH032214B2 (en)
JP2001073041A (en) Method for controlling temperature of steel sheet and temperature controlling device
JPH06287643A (en) Device for controlling strip temperature of continuous steel strip heat treatment line
JPH10158747A (en) Method for setting furnace temperature in heating furnace of continuous annealing furnace

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees