JPH0617147A - Continuous heat treatment for steel strip - Google Patents

Continuous heat treatment for steel strip

Info

Publication number
JPH0617147A
JPH0617147A JP19461092A JP19461092A JPH0617147A JP H0617147 A JPH0617147 A JP H0617147A JP 19461092 A JP19461092 A JP 19461092A JP 19461092 A JP19461092 A JP 19461092A JP H0617147 A JPH0617147 A JP H0617147A
Authority
JP
Japan
Prior art keywords
steel strip
strip
temperature
cooling
cooling zone
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP19461092A
Other languages
Japanese (ja)
Inventor
Jinichi Tamoto
仁一 田本
Tadaaki Nakagawa
忠昭 中川
Akihiko Hasegawa
明彦 長谷川
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP19461092A priority Critical patent/JPH0617147A/en
Publication of JPH0617147A publication Critical patent/JPH0617147A/en
Pending legal-status Critical Current

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  • Control Of Heat Treatment Processes (AREA)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Abstract

PURPOSE:To cool a steel strip down to the desired temp. at the time when the sheet passing amount of the steel strip and the desired temp. are changed in continuous heat treatment for the steel strip. CONSTITUTION:When the sheet passing amount of a steel strip 3 and/or the desired sheet temp. of the steel strip 3 is changed, the values before and after the change are compared. On the basis of the comparison, the forced cooling for the steel strip in a cooling zone 4 is stopped and the inside of the cooling zone 4 is heated by an electrical means 12 or a radiant tube to rise the temp. of the steel strip 3 to the desired temp., or, the inside of the cooling zone 4 is heated by an electrical means 12 or a radiant tube and also the steel strip 3 is cooled down to the desired temp. by the forced cooling for the steel strip 3.

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、鋼帯の連続熱処理方法
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous heat treatment method for steel strip.

【0002】[0002]

【従来の技術】鋼帯の連続熱処理において、各材質のヒ
ートパターンを予め設定しておき、炉温を変化させ、短
時間で鋼種の異なる鋼帯の焼鈍温度を目標焼鈍温度に設
定することが特開平2−205634号公報に開示され
ている。
2. Description of the Related Art In continuous heat treatment of steel strips, it is possible to set a heat pattern for each material in advance, change the furnace temperature, and set the annealing temperature of steel strips of different steel types to a target annealing temperature in a short time. It is disclosed in Japanese Patent Laid-Open No. 2-205634.

【0003】一般に、鋼帯の連続熱処理設備、連続溶融
亜鉛メッキ設備等においては、鋼帯の最大板厚、最大板
幅および最大通板速度で加熱、均熱し、確実に焼鈍でき
るだけの炉の容量を備えている。また、加熱、均熱に引
続き徐冷、急冷等の冷却を施す炉においても、加熱およ
び均熱と同様に最大板厚、最大板幅および最大通板速度
で確実に冷却処理できるだけの炉の容量を備えている。
Generally, in continuous heat treatment equipment for steel strips, continuous hot-dip galvanizing equipment, etc., the capacity of the furnace for heating and soaking at the maximum strip thickness, the maximum strip width and the maximum strip-passing speed of steel strips and for reliable annealing. Is equipped with. In addition, even in a furnace that performs heating, soaking, followed by slow cooling, rapid cooling, etc., the capacity of the furnace that can reliably perform cooling with the maximum plate thickness, maximum plate width, and maximum plate passing speed as in the case of heating and soaking. Is equipped with.

【0004】この冷却炉での冷却は、非酸化性雰囲気ガ
スで充満された冷却帯内に鋼帯を通板し、その際に通板
鋼帯に冷却ガスを吹付けて強制冷却を行い、鋼帯を目標
板温まで冷却する。
In the cooling in this cooling furnace, a steel strip is passed through a cooling zone filled with a non-oxidizing atmosphere gas, and at that time, a cooling gas is sprayed onto the passing steel strip to perform forced cooling. Cool the steel strip to the target plate temperature.

【0005】[0005]

【発明が解決しようとする課題】しかし、鋼帯の通板量
が低下した場合、例えば鋼帯の板厚および/または板幅
サイズが縮小した場合は、鋼帯の加熱、均熱による顕熱
がサイズ縮小により小さくなることから炉内の温度が低
下し、冷却帯での強制冷却を停止させても鋼帯は過冷却
となる。また、通板速度が設備トラブル等で低下した場
合は、通板速度の低下により冷却帯での滞在時間が長く
なり、同様に鋼帯の加熱、均熱による顕熱が結果的に少
なくなり、炉内の温度が低下し、強制冷却を停止させて
も鋼帯は過冷却となる。また、鋼帯の材質変化等による
目標板温変化、特に目標板温上昇の場合は、加熱、均熱
による顕熱は同じである為炉内温度は一定であるが、板
温低下幅が小さくなるため、強制冷却を停止させても鋼
帯は過冷却となる。
However, when the passing amount of the steel strip is reduced, for example, when the plate thickness and / or the width size of the steel strip is reduced, the sensible heat by heating and soaking of the steel strip is obtained. Is reduced due to the size reduction, the temperature in the furnace is lowered, and the steel strip is overcooled even if the forced cooling in the cooling zone is stopped. Also, when the strip running speed decreases due to equipment troubles, etc., the staying time in the cooling zone becomes longer due to the decrease in the strip running speed, and similarly, heating of the steel strip and sensible heat due to soaking eventually decrease, Even if the forced cooling is stopped because the temperature inside the furnace decreases, the steel strip will be overcooled. When the target plate temperature changes due to changes in the material of the steel strip, especially when the target plate temperature rises, the sensible heat due to heating and soaking is the same, so the furnace temperature is constant, but the plate temperature decrease width is small. Therefore, even if the forced cooling is stopped, the steel strip is overcooled.

【0006】つまり、冷却帯であるため加熱機構がな
く、鋼帯の持ち込む熱量で帯内温度が昇温するのを待つ
ことになり、その間鋼帯の冷却が続いて目標温度以上に
冷却されてしまうことになる。その結果、このような連
続処理においては、鋼帯のサイズ縮小の際鋼帯が冷却帯
で過冷却されて材質を損ない、また溶融亜鉛メッキの前
処理の場合には、メッキ不良等の決定的な欠点を伴うこ
とになる。
That is, since it is a cooling zone, it has no heating mechanism and waits for the temperature inside the zone to rise due to the amount of heat carried into the steel strip, during which the steel strip continues to be cooled above the target temperature. Will end up. As a result, in such a continuous treatment, the steel strip is overcooled in the cooling zone when the size of the steel strip is reduced, and the material is damaged. There are some drawbacks.

【0007】本発明の目的は、鋼帯サイズが変更された
時や通板速度が変化した時、また目標板温上昇の時等に
おいて、冷却帯内での鋼帯の過冷却を防止することであ
る。
An object of the present invention is to prevent overcooling of the steel strip in the cooling zone when the size of the steel strip is changed, the strip running speed is changed, or when the target strip temperature rises. Is.

【0008】[0008]

【課題を解決するための手段】本発明の要旨は、以下の
通りである。
The gist of the present invention is as follows.

【0009】 加熱、均熱および冷却を施す鋼帯の連
続熱処理方法において、鋼帯の通板量および/または鋼
帯の目標板温が変化した時に、冷却帯での鋼帯強制冷却
を停止するとともに冷却帯内を電気的手段またはラジア
ントチューブで加熱し、鋼帯を目標温度まで昇温させる
ことを特徴とする鋼帯の連続熱処理方法。
In the continuous heat treatment method for a steel strip to be heated, soaked and cooled, when the strip running amount of the steel strip and / or the target strip temperature of the steel strip changes, the forced cooling of the steel strip in the cooling zone is stopped. At the same time, the continuous heat treatment method for a steel strip is characterized in that the inside of the cooling strip is heated by an electric means or a radiant tube to raise the temperature of the steel strip to a target temperature.

【0010】 加熱、均熱および冷却を施す鋼帯の連
続熱処理方法において、鋼帯の通板量および/または鋼
帯の目標板温が変化した時に、冷却帯内を電気的手段ま
たはラジアントチューブで加熱するとともに、鋼帯の強
制冷却により鋼帯を目標温度まで冷却することを特徴と
する鋼帯の連続熱処理方法。
In a continuous heat treatment method for a steel strip to be heated, soaked and cooled, an electric means or a radiant tube is used in the cooling zone when the amount of steel strip passed and / or the target strip temperature of the steel strip changes. A continuous heat treatment method for a steel strip, which comprises heating and cooling the steel strip to a target temperature by forced cooling.

【0011】[0011]

【作用】本発明では前述した課題を解決するために、鋼
帯のサイズが変更された時や通板速度が変化した時、ま
た目標板温上昇の時等において、冷却帯内を電気加熱ま
たはラジアントチューブ加熱により昇温し、冷却帯内で
の鋼帯の過冷却を防止する。また、電気加熱またはラジ
アントチューブ加熱により鋼帯を昇温し、強制冷却によ
り鋼帯を目標温度に調整する。強制冷却による鋼帯の温
度調整は精密にできるので、電気加熱またはラジアント
チューブ加熱により冷却帯内を冷却目標温度より高く加
熱し、強制冷却により精密に目標温度にするのである。
In the present invention, in order to solve the above-mentioned problems, the inside of the cooling zone is electrically heated or changed when the size of the steel strip is changed, the strip running speed is changed, or when the target strip temperature rises. Raising the temperature by heating the radiant tube prevents supercooling of the steel strip in the cooling zone. Further, the steel strip is heated by electric heating or radiant tube heating, and the steel strip is adjusted to a target temperature by forced cooling. Since the temperature of the steel strip can be precisely adjusted by forced cooling, the inside of the cooling zone is heated above the cooling target temperature by electric heating or radiant tube heating, and the target temperature is precisely set by forced cooling.

【0012】冷却帯としては、徐冷帯と急冷帯を連設す
ることがある。この場合、双方において電気加熱または
ラジアントチューブ加熱により過冷却を防止することが
好ましい。
As the cooling zone, a slow cooling zone and a rapid cooling zone may be provided in series. In this case, it is preferable to prevent supercooling on both sides by electric heating or radiant tube heating.

【0013】このような鋼帯の連続熱処理方法は、例え
ば連続溶融亜鉛メッキラインの前処理炉の操業、鋼帯の
連続焼鈍設備の操業等に有利に適用することができる。
Such a continuous heat treatment method for steel strip can be advantageously applied to, for example, the operation of a pretreatment furnace of a continuous hot-dip galvanizing line, the operation of continuous annealing equipment for steel strip, and the like.

【0014】[0014]

【実施例1】図1に示すように、記憶装置1に平均単重
20tのコイル毎に鋼帯の板厚、板幅、材質を処理順に
記憶しておき、検出センサー2で鋼帯3の溶接点を検出
し、次の鋼帯コイルから巻き戻された鋼帯3の冷却帯4
への通板量予告をトラッキング装置5を介して演算機構
6へ導入する。
[Embodiment 1] As shown in FIG. 1, the plate thickness, the plate width, and the material of the steel strip are stored in the storage device 1 in the order of processing for each coil having an average single weight of 20 tons. Cooling zone 4 of steel strip 3 which has detected the welding point and has been unwound from the next steel strip coil
An advance notice of the passing amount is introduced into the calculation mechanism 6 via the tracking device 5.

【0015】一方、記憶装置1から現在冷却処理してい
る鋼帯3の板厚、板幅、材質、通板速度を演算機構6へ
導入し、単位時間当りの通板量を演算するとともに、次
に加熱、均熱処理を終え冷却処理すべき鋼帯3の板厚、
板幅、材質、通板速度を演算機構6へ導入し、現鋼帯の
通板速度の実績から予測単位時間当りの通板量を演算
し、両者を比較する。演算式は数1である。
On the other hand, the plate thickness, the plate width, the material and the plate passing speed of the steel strip 3 currently being cooled are introduced from the storage device 1 into the calculating mechanism 6 to calculate the plate passing amount per unit time, Next, the thickness of the steel strip 3 to be cooled after finishing heating and soaking,
The strip width, the material, and the strip running speed are introduced into the computing mechanism 6, the strip running amount per predicted unit time is calculated from the actual strip running speed of the current steel strip, and the two are compared. The arithmetic expression is Equation 1.

【0016】[0016]

【数1】THpr=THma2 ×(THn0/THma1 ) THn0=DS×TH×WA×LS 但し、 THpr :次鋼帯の予測通板量 THma2 :次鋼帯の規定通板量 THma1 :現鋼帯の規定通板量 THn0 :現鋼帯の実績通板量 DS :ストリップ密度 TH :板厚 WA :板幅 LS :ライン速度[ Formula 1] TH pr = TH ma2 x (TH n0 / TH ma1 ) TH n0 = DS x TH x WA x LS where TH pr : Predicted strip amount of the next steel strip TH ma2 : Specified strip of the next steel strip Amount TH ma1 : Specified strip running amount of the current steel strip TH n0 : Actual strip running amount of the current steel strip DS: Strip density TH: Strip thickness WA: Strip width LS: Line speed

【0017】また、記憶装置1から現在冷却処理してい
る鋼帯3の目標温度を演算機構6へ導入するとともに、
次に加熱、均熱処理を終え冷却処理すべき鋼帯3の目標
温度も演算機構6へ導入し、目標板温が変化する場合、
両者を比較する。
In addition, the target temperature of the steel strip 3 currently being cooled is introduced from the storage device 1 into the calculation mechanism 6, and
Next, when the target temperature of the steel strip 3 to be cooled after heating and soaking is also introduced into the calculation mechanism 6 and the target plate temperature changes,
Compare both.

【0018】このようにして、次コイルの鋼帯が冷却帯
4へ通板する時に両者の通板量や目標板温が変化した場
合に、次鋼帯の目標板温が冷却帯4内で過冷却になると
判断すると、電気加熱により冷却帯4を昇温することが
必要となるので、炉温設定タイミング算定機構7と炉温
設定値算定機構8へそれぞれ指示し、強制冷却の停止お
よび電気加熱開始タイミングと炉温設定値を炉温設定機
構9を介して炉温調節装置10へ導入する。炉温調節装
置10では、現在炉温を温度計11により測定した結果
を導入し、炉温設定値に基づく加熱量を判断し、電力量
を算出してヒーター12へ通電し、冷却帯4内を炉温設
定値になるように加熱し、強制冷却器13を停止し、ノ
ズル14からの鋼帯3への冷却ガス吹き付けを停止す
る。炉温設定値は数2で求める。
In this way, when the steel strip of the next coil passes through the cooling zone 4 when the stripping amount and the target strip temperature of the two coils change, the target strip temperature of the next steel strip is within the cooling zone 4. When it is determined that the supercooling will occur, it is necessary to raise the temperature of the cooling zone 4 by electric heating. Therefore, the furnace temperature setting timing calculating mechanism 7 and the furnace temperature setting value calculating mechanism 8 are instructed respectively to stop the forced cooling and to turn on the electric power. The heating start timing and the furnace temperature set value are introduced into the furnace temperature adjusting device 10 via the furnace temperature setting mechanism 9. In the furnace temperature adjusting device 10, the result of measuring the current furnace temperature by the thermometer 11 is introduced, the heating amount based on the furnace temperature set value is determined, the electric power amount is calculated, the heater 12 is energized, and the cooling zone 4 is cooled. Is heated to the furnace temperature set value, the forced cooler 13 is stopped, and the blowing of the cooling gas from the nozzle 14 to the steel strip 3 is stopped. The furnace temperature set value is calculated by Equation 2.

【0019】[0019]

【数2】TF=TS+C1 {TH(QSot−QSit)}
/(2・HS) 但し、 TF :炉温 TS :目標板温 C1 :調整パラメータ TH :次鋼帯の予測通板量 QSot :入側板温の熱容量 QSit :出側板温の熱容量 HS :熱伝達係数
[Formula 2] TF = TS + C 1 {TH (QS ot −QS it )}
/ (2 · HS) where TF: Reactor temperature TS: Target strip temperature C 1 : Adjustment parameter TH: Predicted strip amount of the next steel strip QS ot : Heat capacity of inlet strip temperature QS it : Heat capacity of outlet strip temperature HS: Heat transfer coefficient

【0020】また、演算機構6で、鋼帯サイズ、材質、
通板速度から次鋼帯が冷却帯4へ通板する時に電気加熱
とともに強制冷却により処理すると判断した場合は、同
様に炉温設定タイミング算定機構7、炉温設定値算定機
構8および炉温設定機構9を介して炉温調節装置10へ
指示し、同様にヒーター12へ通電し、冷却帯4内を加
熱するとともに強制冷却器13を稼働し、冷却帯4内の
雰囲気ガスの一部を取り出し、冷却器13で循環冷却
し、ノズル14から鋼帯3へ吹き付け、設定温度に冷却
する。
Further, in the calculation mechanism 6, the steel strip size, material,
If it is judged from the strip passing speed that the next steel strip is passed through the cooling zone 4 by electric cooling together with electric heating, the furnace temperature setting timing calculation mechanism 7, the furnace temperature set value calculation mechanism 8 and the furnace temperature setting are similarly set. The furnace temperature control device 10 is instructed via the mechanism 9, and the heater 12 is similarly energized to heat the cooling zone 4 and operate the forced cooler 13 to take out a part of the atmospheric gas in the cooling zone 4. Then, it is circulated and cooled by the cooler 13, sprayed from the nozzle 14 to the steel strip 3, and cooled to the set temperature.

【0021】次に、速度検出器15で速度変化を検出し
た場合には、記憶装置1から現在冷却処理している鋼帯
3の板厚、板幅、材質、速度変化前の通板速度を演算機
構6へ導入して単位時間当りの通板量を演算すると共
に、次に速度変化後の通板速度を導入し、同様に単位時
間当りの通板量を演算する。そして両者を比較し、現コ
イルと鋼帯3が冷却帯4内で通板中に過冷却になると判
断すると、電気加熱により冷却帯4を昇温することが必
要となるので、炉温設定タイミング算定機構7、炉温設
定値算定機構8および炉温設定機構9を介して炉温調節
装置10へ指示し、同様にヒーター12へ通電し、冷却
帯4内を加熱すると共に強制冷却器13を停止し、ノズ
ル14から鋼帯3への冷却ガス吹き付けを停止する。
Next, when a speed change is detected by the speed detector 15, the plate thickness, the plate width, the material, and the strip running speed before the speed change of the steel strip 3 currently being cooled are stored in the storage device 1. The sheet passing amount per unit time is calculated by introducing it into the calculation mechanism 6, and then the sheet passing speed after the speed change is introduced and similarly the sheet passing amount per unit time is calculated. Then, when both are compared and it is determined that the current coil and the steel strip 3 will be supercooled during the passage in the cooling zone 4, it is necessary to raise the temperature of the cooling zone 4 by electric heating. The furnace temperature adjusting device 10 is instructed through the calculation mechanism 7, the furnace temperature set value calculation mechanism 8 and the furnace temperature setting mechanism 9, and similarly, the heater 12 is energized to heat the inside of the cooling zone 4 and the forced cooler 13 is set. Then, the blowing of the cooling gas from the nozzle 14 to the steel strip 3 is stopped.

【0022】また、速度検出器15で速度変化を検出し
た場合に、演算機構6で鋼帯サイズ、材質、速度変化前
および速度変化後の通板速度から同様に単位時間当りの
通板量を演算すると共に両者の比較を行い、電気加熱と
ともに強制冷却により処理すると判断した場合は、同様
に炉温設定タイミング算定機構7、炉温設定値算定機構
8および炉温設定機構9を介して炉温調節装置10へ指
示し、同様にヒーター12へ通電し、冷却帯4内を加熱
するとともに強制冷却器13を稼働し、冷却帯4内の雰
囲気ガスの一部を取り出し、冷却器13で循環冷却し、
ノズル14から鋼帯3へ吹き付け、設定温度に冷却す
る。
When a speed change is detected by the speed detector 15, the arithmetic mechanism 6 similarly determines the passing amount per unit time from the steel strip size, the material, the passing speed before and after the speed change. When it is determined that both the electric heating and the forced cooling should be performed, the temperature of the furnace is set via the furnace temperature setting timing calculating mechanism 7, the furnace temperature set value calculating mechanism 8 and the furnace temperature setting mechanism 9. The controller 12 is instructed to similarly energize the heater 12, heat the inside of the cooling zone 4 and operate the forced cooler 13, take out a part of the atmospheric gas in the cooling zone 4, and circulate and cool it with the cooler 13. Then
The steel strip 3 is sprayed from the nozzle 14 and cooled to a set temperature.

【0023】[0023]

【実施例2】図2に示すように、記憶装置1に平均単重
20tのコイル毎に鋼帯の板厚、板幅、材質を処理する
順番に記憶しておき、検出センサー2で鋼帯3の溶接点
を検出し、次の鋼帯コイルから巻き戻された鋼帯3の冷
却帯4への通板量予告をトラッキング装置5を介して演
算機構6へ導入する。
[Embodiment 2] As shown in FIG. 2, the steel sheet thickness, the sheet width, and the material of the steel strip are stored in the storage device 1 in order of processing for each coil having an average single weight of 20 tons. A welding point of No. 3 is detected, and a notice of the passing amount of the steel strip 3 unwound from the next steel strip coil to the cooling zone 4 is introduced to the arithmetic mechanism 6 via the tracking device 5.

【0024】一方、記憶装置1から現在冷却処理してい
る鋼帯3の板厚、板幅、材質、通板速度を演算機構6へ
導入し、単位時間当りの通板量を演算するとともに、次
に加熱、均熱処理を終え冷却処理すべき鋼帯3の板厚、
板幅、材質、通板速度を演算機構6へ導入し、現鋼帯の
通板速度の実績から予測単位時間当りの通板量を演算
し、両者を比較する。演算式は数3である。
On the other hand, the plate thickness, the plate width, the material, and the plate passing speed of the steel strip 3 currently being cooled are introduced from the storage device 1 into the calculating mechanism 6 to calculate the plate passing amount per unit time, Next, the thickness of the steel strip 3 to be cooled after finishing heating and soaking,
The strip width, the material, and the strip running speed are introduced into the computing mechanism 6, the strip running amount per predicted unit time is calculated from the actual strip running speed of the current steel strip, and the two are compared. The arithmetic expression is Equation 3.

【0025】[0025]

【数3】THpr=THma2 ×(THn0/THma1 ) THn0=DS×TH×WA×LS 但し、 THpr :次鋼帯の予測通板量 THma2 :次鋼帯の規定通板量 THma1 :現鋼帯の規定通板量 THn0 :現鋼帯の実績通板量 DS :ストリップ密度 TH :板厚 WA :板幅 LS :ライン速度[ Formula 3] TH pr = TH ma2 x (TH n0 / TH ma1 ) TH n0 = DS x TH x WA x LS where TH pr : Predicted strip amount of the next steel strip TH ma2 : Specified strip of the next steel strip Amount TH ma1 : Specified strip running amount of the current steel strip TH n0 : Actual strip running amount of the current steel strip DS: Strip density TH: Strip thickness WA: Strip width LS: Line speed

【0026】また、記憶装置1から現在冷却処理してい
る鋼帯3の目標温度を演算機構6へ導入するとともに、
次に加熱、均熱処理を終え冷却処理すべき鋼帯3の目標
温度も演算機構6へ導入し、目標板温が変化する場合、
両者を比較する。
Further, the target temperature of the steel strip 3 currently being cooled is introduced from the storage device 1 into the arithmetic mechanism 6, and
Next, when the target temperature of the steel strip 3 to be cooled after heating and soaking is also introduced into the calculation mechanism 6 and the target plate temperature changes,
Compare both.

【0027】このようにして、次コイルの鋼帯が冷却帯
4へ通板した時に両者の通板量や目標板温が変化した場
合に、次鋼帯の目標板温が冷却帯4内で過冷却になると
判断すると、ラジアントチューブ16により冷却帯4を
昇温することが必要となるので、炉温設定タイミング算
定機構7と炉温設定値算定機構8へそれぞれ指示し、強
制冷却の停止およびラジアントチューブ16による加熱
開始タイミングと炉温設定値を炉温設定機構9を介して
炉温調節装置10へ導入する。炉温調節装置10では、
現在炉温を温度計11により測定した結果を導入し、炉
温設定値に基づく加熱量を判断し、ラジアントチューブ
16に流す燃料流量を算出して燃料を流し、冷却帯4内
を炉温設定値に加熱し、強制冷却器13を停止し、ノズ
ル14からの鋼帯3への冷却ガス吹き付けを停止する。
炉温設定値は数4で求める。
In this way, when the steel strip of the next coil passes through the cooling zone 4 and the stripping amount or the target strip temperature of both of them changes, the target strip temperature of the next steel strip is within the cooling zone 4. When it is determined that supercooling will occur, it is necessary to raise the temperature of the cooling zone 4 by means of the radiant tube 16, so the furnace temperature setting timing calculating mechanism 7 and the furnace temperature setting value calculating mechanism 8 are respectively instructed to stop forced cooling and The heating start timing by the radiant tube 16 and the furnace temperature set value are introduced into the furnace temperature adjusting device 10 via the furnace temperature setting mechanism 9. In the furnace temperature control device 10,
The result of measurement of the current furnace temperature by the thermometer 11 is introduced, the heating amount based on the furnace temperature set value is determined, the fuel flow rate flowing in the radiant tube 16 is calculated, and the fuel is flowed to set the furnace temperature in the cooling zone 4. After heating to the value, the forced cooler 13 is stopped, and the blowing of the cooling gas from the nozzle 14 to the steel strip 3 is stopped.
The furnace temperature set value is calculated by Equation 4.

【0028】[0028]

【数4】TF=TS+C1 {TH(QSot−QSit)}
/(2・HS) 但し、 TF :炉温 TS :目標板温 C1 :調整パラメータ TH :次鋼帯の予測通板量 QSot :入側板温の熱容量 QSit :出側板温の熱容量 HS :熱伝達係数
[Formula 4] TF = TS + C 1 {TH (QS ot −QS it )}
/ (2 · HS) However, TF: furnace temperature TS: target strip temperature C 1 : adjustment parameter TH: predicted strip volume of the next steel strip QS ot : heat capacity of inlet strip temperature QS it : heat capacity of outlet strip temperature HS: Heat transfer coefficient

【0029】また、演算機構6で、鋼帯サイズ、材質、
通板速度から次鋼帯が冷却帯4へ通板する時にラジアン
トチューブ加熱とともに強制冷却により処理すると判断
した場合は、同様に炉温設定タイミング算定機構7、炉
温設定値算定機構8および炉温設定機構9を介して炉温
調節装置10へ指示し、同様にラジアントチューブ16
へ燃料を流し、冷却帯4内を加熱するとともに強制冷却
器13を稼働し、冷却帯4内の雰囲気ガスの一部を取り
出し、冷却器13で循環冷却し、ノズル14から鋼帯3
へ吹き付け、設定温度に冷却する。
Further, in the calculation mechanism 6, the steel strip size, material,
If it is determined from the strip running speed that the next steel strip is striped through the cooling zone 4 by the radiant tube heating and the forced cooling, the furnace temperature setting timing calculating mechanism 7, the furnace temperature setting value calculating mechanism 8 and the furnace temperature are similarly set. The furnace temperature control device 10 is instructed via the setting mechanism 9, and similarly the radiant tube 16
The fuel is flown into the cooling zone 4 to heat the cooling zone 4 and the forced cooler 13 is operated.
And cool to the set temperature.

【0030】次に、速度検出器15で速度変化を検出し
た場合には、記憶装置1から現在冷却処理している鋼帯
3の板厚、板幅、材質、速度変化前の通板速度を演算機
構6へ導入して単位時間当りの通板量を演算すると共
に、次に速度変化後の通板速度を導入し、同様に単位時
間当りの通板量を演算する。そして両者を比較し、現コ
イルの鋼帯3が冷却帯4内で通板中に過冷却になると判
断すると、ラジアントチューブ16により冷却帯4を昇
温することが必要となるので、炉温設定タイミング算定
機構7、炉温設定値算定機構8および炉温設定機構9を
介して炉温調節装置10へ指示し、同様にラジアントチ
ューブ16へ流す燃料を操作し、冷却帯4内を加熱する
と共に強制冷却器13を停止し、ノズル14から鋼帯3
への冷却ガス吹き付けを停止する。
Next, when the speed change is detected by the speed detector 15, the plate thickness, the plate width, the material, and the passing speed before the speed change of the steel strip 3 currently being cooled are stored in the storage device 1. The sheet passing amount per unit time is calculated by introducing it into the calculation mechanism 6, and then the sheet passing speed after the speed change is introduced and similarly the sheet passing amount per unit time is calculated. When the steel strips 3 of the current coil are compared with each other and it is determined that the steel strip 3 will be supercooled during passage in the cooling zone 4, it is necessary to raise the temperature of the cooling zone 4 by the radiant tube 16. The furnace temperature adjusting device 10 is instructed via the timing calculation mechanism 7, the furnace temperature set value calculation mechanism 8 and the furnace temperature setting mechanism 9, and similarly, the fuel flowing to the radiant tube 16 is operated to heat the inside of the cooling zone 4. The forced cooler 13 is stopped, and the steel strip 3 is discharged from the nozzle 14.
Stop blowing cooling gas to.

【0031】また、速度検出器15で速度変化を検出し
た場合に、演算機構6で鋼帯サイズ、材質、速度変化前
および速度変化後の通板速度から同様に単位時間当りの
通板量を演算すると共に両者の比較を行い、ラジアント
チューブによる加熱とともに強制冷却により処理すると
判断した場合は、同様に炉温設定タイミング算定機構
7、炉温設定値算定機構8および炉温設定機構9を介し
て炉温調節装置10へ指示し、同様にラジアントチュー
ブ16へ燃料を流し、冷却帯4内を加熱するとともに強
制冷却器13を稼働し、冷却帯4内の雰囲気ガスの一部
を取り出し、冷却器13で循環冷却し、ノズル14から
鋼帯3へ吹き付け、設定温度に冷却する。
When a speed change is detected by the speed detector 15, the arithmetic mechanism 6 similarly determines the amount of steel passing per unit time from the steel strip size, the material, and the plate passing speed before and after the speed change. When the calculation is performed and the two are compared, and it is determined that the heating is performed by the radiant tube and the forced cooling is performed, the furnace temperature setting timing calculation mechanism 7, the furnace temperature set value calculation mechanism 8, and the furnace temperature setting mechanism 9 are similarly used. The furnace temperature control device 10 is instructed to flow the fuel to the radiant tube 16 in the same manner to heat the cooling zone 4 and operate the forced cooler 13 to take out a part of the atmospheric gas in the cooling zone 4 and cool the cooler. It is circulated and cooled at 13, is sprayed from the nozzle 14 to the steel strip 3, and is cooled to a set temperature.

【0032】[0032]

【発明の効果】本発明により、目標とする鋼帯材質に対
して適切な熱処理をすることができる。また、連続溶融
亜鉛メッキ設備の前処理設備に適用した場合は、材質を
向上すると共にメッキ不良も防止することができる等の
優れた効果が得られる。
According to the present invention, it is possible to perform an appropriate heat treatment on a target steel strip material. Further, when applied to a pretreatment facility of a continuous hot dip galvanizing facility, excellent effects such as improvement of material and prevention of plating failure can be obtained.

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

【図1】本発明を実施するための装置の一例を示す説明
図である。
FIG. 1 is an explanatory diagram showing an example of an apparatus for carrying out the present invention.

【図2】本発明を実施するための装置の他の例を示す説
明図である。
FIG. 2 is an explanatory diagram showing another example of an apparatus for carrying out the present invention.

【符号の説明】[Explanation of symbols]

1 記憶装置 2 検出センサー 3 鋼帯 4 冷却帯 5 トラッキング装置 6 演算機構 7 炉温設定タイミング算定機構 8 炉温設定値算定機構 9 炉温設定機構 10 炉温調節装置 11 温度計 12 ヒーター 13 強制冷却器 14 ノズル 15 速度検出器 16 ラジアントチューブ 1 Storage Device 2 Detection Sensor 3 Steel Strip 4 Cooling Zone 5 Tracking Device 6 Calculation Mechanism 7 Reactor Temperature Setting Timing Calculation Mechanism 8 Reactor Temperature Set Value Calculation Mechanism 9 Reactor Temperature Setting Mechanism 10 Reactor Temperature Controller 11 Thermometer 12 Heater 13 Forced Cooling Vessel 14 nozzle 15 speed detector 16 radiant tube

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 加熱、均熱および冷却を施す鋼帯の連続
熱処理方法において、鋼帯の通板量および/または鋼帯
の目標板温が変化した時に、冷却帯での鋼帯強制冷却を
停止するとともに冷却帯内を電気的手段またはラジアン
トチューブで加熱し、鋼帯を目標温度まで昇温させるこ
とを特徴とする鋼帯の連続熱処理方法。
1. In a continuous heat treatment method for a steel strip to be heated, soaked and cooled, forced strip cooling in the cooling zone is carried out when the strip running amount of the steel strip and / or the target strip temperature of the steel strip changes. A continuous heat treatment method for a steel strip, which comprises stopping and heating the inside of the cooling strip by an electric means or a radiant tube to raise the temperature of the steel strip to a target temperature.
【請求項2】 加熱、均熱および冷却を施す鋼帯の連続
熱処理方法において、鋼帯の通板量および/または鋼帯
の目標板温が変化した時に、冷却帯内を電気的手段また
はラジアントチューブで加熱するとともに、鋼帯の強制
冷却により鋼帯を目標温度まで冷却することを特徴とす
る鋼帯の連続熱処理方法。
2. In a continuous heat treatment method for a steel strip to be heated, soaked and cooled, an electric means or a radiant inside the cooling zone is produced when the amount of steel strip passed and / or the target strip temperature of the steel strip changes. A continuous heat treatment method for a steel strip, which comprises heating the steel strip by a tube and cooling the steel strip to a target temperature by forcibly cooling the steel strip.
JP19461092A 1992-06-30 1992-06-30 Continuous heat treatment for steel strip Pending JPH0617147A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19461092A JPH0617147A (en) 1992-06-30 1992-06-30 Continuous heat treatment for steel strip

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19461092A JPH0617147A (en) 1992-06-30 1992-06-30 Continuous heat treatment for steel strip

Publications (1)

Publication Number Publication Date
JPH0617147A true JPH0617147A (en) 1994-01-25

Family

ID=16327406

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19461092A Pending JPH0617147A (en) 1992-06-30 1992-06-30 Continuous heat treatment for steel strip

Country Status (1)

Country Link
JP (1) JPH0617147A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5015712A (en) * 1973-06-15 1975-02-19
JPS5576026A (en) * 1978-11-30 1980-06-07 Nippon Steel Corp Plate temperature control method
JPS5677340A (en) * 1979-11-30 1981-06-25 Mitsubishi Heavy Ind Ltd Method of controlling strip temperature in cooling zone of continuous annealing equipment
JPS5861233A (en) * 1981-10-08 1983-04-12 Nippon Steel Corp Controlling method for temperature of plate
JPS60145327A (en) * 1983-12-30 1985-07-31 Nippon Steel Corp Method and installation for continuous annealing of cold rolled steel sheet

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5015712A (en) * 1973-06-15 1975-02-19
JPS5576026A (en) * 1978-11-30 1980-06-07 Nippon Steel Corp Plate temperature control method
JPS5677340A (en) * 1979-11-30 1981-06-25 Mitsubishi Heavy Ind Ltd Method of controlling strip temperature in cooling zone of continuous annealing equipment
JPS5861233A (en) * 1981-10-08 1983-04-12 Nippon Steel Corp Controlling method for temperature of plate
JPS60145327A (en) * 1983-12-30 1985-07-31 Nippon Steel Corp Method and installation for continuous annealing of cold rolled steel sheet

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