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JPH0480975B2 - - Google Patents
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JPH0480975B2 - - Google Patents

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Publication number
JPH0480975B2
JPH0480975B2 JP60185622A JP18562285A JPH0480975B2 JP H0480975 B2 JPH0480975 B2 JP H0480975B2 JP 60185622 A JP60185622 A JP 60185622A JP 18562285 A JP18562285 A JP 18562285A JP H0480975 B2 JPH0480975 B2 JP H0480975B2
Authority
JP
Japan
Prior art keywords
temperature
cooling
feo
cooled
cooling stop
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.)
Expired - Lifetime
Application number
JP60185622A
Other languages
Japanese (ja)
Other versions
JPS6244528A (en
Inventor
Koro Takatsuka
Akinori Ootomo
Izuo Takahashi
Yoshikazu Oobanya
Mitsuo Kitamura
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP60185622A priority Critical patent/JPS6244528A/en
Publication of JPS6244528A publication Critical patent/JPS6244528A/en
Publication of JPH0480975B2 publication Critical patent/JPH0480975B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B37/00Control devices or methods specially adapted for metal-rolling mills or the work produced thereby
    • B21B37/74Temperature control, e.g. by cooling or heating the rolls or the product
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D9/00Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/52Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54Furnaces for treating strips or wire
    • C21D9/56Continuous furnaces for strip or wire
    • C21D9/573Continuous furnaces for strip or wire with cooling

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Control Of Metal Rolling (AREA)
  • Control Of Heat Treatment Processes (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、例えば鉄鋼業の熱間圧延プロセスに
おいて高温の被圧延材を水冷却する場合の被冷却
材の強制冷却停止温度の推定方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for estimating the forced cooling stop temperature of a material to be cooled when a hot rolled material is water-cooled in a hot rolling process in the steel industry, for example. It is something.

(従来技術) 熱間圧延プロセス等において、高温の被冷却材
は材質制御等の目的で水冷却されるが、この場
合、成品の品質保持上冷却停止温度を管理するこ
とは重要である。
(Prior Art) In hot rolling processes and the like, high-temperature materials to be cooled are cooled with water for the purpose of material quality control, etc. In this case, it is important to control the cooling stop temperature in order to maintain the quality of the finished product.

例えば、従来ホツトストリツプミルにおいて
は、ランアウトテーブルにて水冷却が実施されて
おり、上記冷却停止温度を管理するため、冷却装
置の中間あるいは出側に温度計が設置され、被冷
却材である鋼板の温度計測が行れていた(特公昭
53−25701号公報)。そして、このホツトストリツ
プミルにて製造されるのは薄板であり、水冷却後
の板厚方向の温度の平均化すなわち複熱が非常に
速いため、表面温度を鋼板代表温度として、この
温度より冷却停止温度を求めても問題となること
はなかつた。
For example, in conventional hot strip mills, water cooling is performed on a run-out table, and in order to control the cooling stop temperature mentioned above, a thermometer is installed in the middle or on the outlet side of the cooling device, and the material to be cooled is The temperature of a certain steel plate was being measured (Tokuko Sho)
53-25701). This hot strip mill produces thin plates, and since the temperature in the thickness direction after water cooling is averaged, that is, double heat is extremely fast, the surface temperature is taken as the representative temperature of the steel plate. There was no problem even if the cooling stop temperature was found to be higher.

ところが、近年冷却技術の進歩に伴い厚板工場
や棒鋼工場に強制水冷却が適用されるに至り、表
面温度と被冷却材代表温度(例えば、板であれば
板厚方法平均温度、棒であれば断面内平均温度
等)をオンライン計測により決定するに際し、
種々の外乱(操業条件の違いも含む。)のため、
十分な空冷時間を経た後でなければならず、冷却
停止温度を求めるのに時間がかかり、生産性の低
下等を引き起こすという問題があつた。
However, in recent years, with advances in cooling technology, forced water cooling has come to be applied to plate factories and steel bar factories. When determining the average cross-sectional temperature, etc.) by online measurement,
Due to various disturbances (including differences in operating conditions),
This has to be done after a sufficient air cooling time has elapsed, and it takes time to determine the cooling stop temperature, which causes problems such as a decrease in productivity.

一般に、水冷却された被冷却材の温度回復は同
一材質の場合、水量密度が低い冷却ほどまたは薄
い寸法のものほど速い。しかし、例えば厚さ10mm
の鋼板を水量密度1m3/min・m2で水冷し、板厚
方向の平均温度を約800℃から550℃にしたとき、
冷却後の板厚方向での複熱に約150秒もかかる。
すなわち、冷却停止温度を推定するためには、冷
却停止後150秒経過後でなければならないことに
なる。
In general, when the material is the same, the temperature recovery of a water-cooled material is faster as the water density is lower or the material is thinner. But for example thickness 10mm
When a steel plate is cooled with water at a water density of 1 m 3 /min・m 2 and the average temperature in the thickness direction is increased from approximately 800°C to 550°C,
After cooling, it takes about 150 seconds for the compound heat to build up in the thickness direction.
That is, in order to estimate the cooling stop temperature, it is necessary to wait 150 seconds after the cooling stops.

(発明の目的) 本発明は、上記従来の問題点に鑑みてなされた
もので、その目的は強制冷却後の被冷却材が複熱
した後は勿論、冷却後の複熱完了を待たずに被冷
却材の冷却停止温度を求めることを可能とした被
冷却材の強制冷却停止温度の推定方法を提供する
ことにある。
(Object of the Invention) The present invention has been made in view of the above-mentioned conventional problems, and its purpose is to prevent the material from being cooled after forced cooling, not only after the material to be cooled undergoes multiple heating, but also without waiting for the completion of the multiple heating after cooling. An object of the present invention is to provide a method for estimating the forced cooling stop temperature of a cooled material, which makes it possible to determine the cooling stop temperature of the cooled material.

(発明の構成) 上記の目的を達成するために、本発明は、高温
の被冷却材を強制冷却した後、空冷時間を設け
て、被冷却材の表面温度を測定し、強制冷却停止
時の被冷却材移送方向に対して直交する断面の代
表温度を求める被冷却材の強制冷却停止温度推定
方法において、被冷却材の代表点を少なくとも1
つ設定し、その代表点にて、あるサンプル時間を
経て、被冷却材表面温度を少なくとも2回測定し
て得たサンプ値から代表表面温度TAVを求めると
ともに、代表点における温度が上昇中であるか否
かを判定し、上昇中の場合には、2つの適宜基準
温度Tl(l=1,2)毎に複熱完了時の表面温度
と上記代表表面温度TAVとの差DTlと、複熱完了
時の表面温度とその点における板厚方向平均温度
との差ΔTplと、強制冷却停止後複熱完了までの
間の空冷による降下温度ΔTfplとを水量密度、被
冷却材の厚さおよび代表温度平均の関数として表
わし、基準冷却停止温度TfTlを次式 TfTl=TAV+DTl+ΔTpl+ΔTfpl により算出とともに、適宜目標冷却停止温度Tfp
を設定して、冷却停止温度Tfeoを次式 Tfeo=TfT1+(TfT2−TfT1)・(T′fe1−T1) /(T2−T1) により算出し、計算精度向上のための必要に応じ
て、上記冷却停止温度Tfeoを用いて修正後の冷却
停止温度Tfeo+1を求める計算を次式 Tfeo+1=TfT1+(TfT2−TfT1)・(Tfeo−T1) /(T2−T1) により算出してTfeo+1を新たにTfeoとし、この計
算を適宜回数繰返して冷却停止温度Tfeoを算出す
る一方、上記代表点における温度が上昇中でない
場合には、上記基準温度Tl(l=1,2)毎に代
表表面温度TAVと、その温度の時の板厚方向の平
均温度との差ΔTnlと、強制冷却停止後のサンプ
リングまでの間の空冷による降下温度ΔTfnlとを
被冷却材の厚さおよび空冷時間の関数として表わ
し、基準冷却停止温度TfTlを次式 TfA1=TAV+ΔTnl+ΔTfnl により算出して、以下上記同様にして冷却停止温
度Tfeoを算出するようにした。
(Structure of the Invention) In order to achieve the above object, the present invention provides an air cooling time after forcibly cooling a high-temperature material to be cooled, measures the surface temperature of the material to be cooled, and measures the surface temperature of the material to be cooled when the forced cooling is stopped. In a method for estimating the forced cooling stop temperature of a material to be cooled, which calculates the representative temperature of a cross section perpendicular to the direction of transport of the material to be cooled, at least one representative point of the material to be cooled is determined.
The representative surface temperature T AV is determined from the sample value obtained by measuring the surface temperature of the material to be cooled at least twice after a certain sample time at the representative point, and also indicates that the temperature at the representative point is rising. If the temperature is rising, the difference between the surface temperature at the completion of compound heating and the above-mentioned representative surface temperature T AV is determined for each two appropriate reference temperatures T l (l = 1, 2). , the difference between the surface temperature at the completion of compound heating and the average temperature in the plate thickness direction at that point, ΔT pl , and the temperature drop due to air cooling, ΔT fpl , from the stop of forced cooling until the completion of compound heating, are expressed as the water density, the material to be cooled. The standard cooling stop temperature T fTl is calculated by the following formula T fTl = T AV + DT l + ΔT pl + ΔT fpl , and the target cooling stop temperature T fp is calculated as appropriate.
The cooling stop temperature T feo is calculated using the following formula T feo = T fT1 + (T fT2 − T fT1 )・(T′ fe1 − T 1 ) / (T 2T 1 ) to improve calculation accuracy. If necessary, calculate the corrected cooling stop temperature T feo+1 using the above cooling stop temperature T feo using the following formula: T feo+1 = T fT1 + (T fT2 − T fT1 )・( T feo - T 1 ) / (T 2 - T 1 ) T feo+1 is newly set as T feo , and this calculation is repeated an appropriate number of times to calculate the cooling stop temperature T feo . If the temperature is not rising, the difference ΔT nl between the representative surface temperature T AV and the average temperature in the plate thickness direction at that temperature, and the forced cooling for each reference temperature T l (l = 1, 2) The temperature drop ΔT fnl due to air cooling after stopping until sampling is expressed as a function of the thickness of the material to be cooled and the air cooling time, and the reference cooling stop temperature T fTl is calculated using the following formula: T fA1 = T AV + ΔT nl + ΔT fnl Then, the cooling stop temperature T feo was calculated in the same manner as above.

(実施例) 次に、本発明の一実施例を図面にしたがつて説
明する。
(Example) Next, an example of the present invention will be described with reference to the drawings.

第1図は、本発明に係る方法が適用される厚板
仕上圧延設備ラインの概略を示し、通板方向に沿
つて仕上圧延機1、冷却設備2、ホツトレベラ3
が配設してあり、鋼板4をパスライン5に沿つ
て、図中右から左へと通すようになつている。ま
た、冷却設備2の前後には厚鋼板4の表面温度を
測定するために入側温度計6、出側温度計7が設
けてある。なお、図中二点鎖線にて示すように冷
却設備2、出側温度計7はホツトレベラ3の通板
方向前方に配置することもある。
FIG. 1 schematically shows a thick plate finishing rolling equipment line to which the method according to the present invention is applied.
is arranged, and the steel plate 4 is passed along the pass line 5 from right to left in the figure. Furthermore, an inlet thermometer 6 and an outlet thermometer 7 are provided before and after the cooling equipment 2 in order to measure the surface temperature of the thick steel plate 4. In addition, as shown by the two-dot chain line in the figure, the cooling equipment 2 and the outlet thermometer 7 may be arranged in front of the hot leveler 3 in the sheet passing direction.

冷却設備2による冷却方法は、鋼板4を搬送し
ながら、その搬送方向前端から後端に向かつて遂
次冷却する一方向通板冷却方法である。ちなみに
冷却方法には、この他鋼板4を往復させながら冷
却するオツシレーシヨン通板により冷却するもの
があるが、下記する本発明に係る方法の適用に関
して、冷却方法は何ら限定するものではない。
The cooling method using the cooling equipment 2 is a one-way cooling method in which the steel plate 4 is sequentially cooled from the front end toward the rear end in the transport direction while being transported. Incidentally, other cooling methods include cooling by oscillation passing, which cools the steel plate 4 while reciprocating, but the cooling method is not limited in any way to the application of the method according to the present invention described below.

そして、上記の設備において、仕上圧延機1を
出た鋼板4を冷却設備2での冷却終了後、ホツト
レベラ3前まで搬送して、一旦静止させ、つづい
て、本発明に係る方法を実施するために出側温度
計7により鋼板4の温度を測定する。すなわち、
同一場所にて温度に関して多時点のサンプリング
を行うようにしてある。測定後、再度鋼板4の搬
送を始めてホツトレベラ3にて鋼板4のレベリン
グを行い、内部応力、歪を除去する。
In the above-mentioned equipment, after the steel plate 4 leaving the finishing mill 1 has been cooled in the cooling equipment 2, it is conveyed to the front of the hot leveler 3 and once stopped, and then the method according to the present invention is carried out. Then, the temperature of the steel plate 4 is measured using the outlet thermometer 7. That is,
Temperature sampling is performed at multiple times at the same location. After the measurement, the steel plate 4 is conveyed again, and the steel plate 4 is leveled by the hot leveler 3 to remove internal stress and distortion.

次に、本発明に係る被冷却材の強制冷却停止温
度推定方法を上記設備に適用して具体的に説明す
る。
Next, the method for estimating the forced cooling stop temperature of a material to be cooled according to the present invention will be specifically explained by applying it to the above equipment.

はじめに、上記のサンプリングを行つた任意の
点の温度変化の様子は第2図に示すようになるこ
とが分かつている。図中横軸は水冷却開始時点か
らの時間で、t=τ〓およびτ〓+Δτpは各々水冷却
停止時点、水冷却停止後の復熱完了時点を示し、
縦軸は温度で、曲線は上記任意点の鋼板4の表
面温度の変化、曲線はこの任意点の代表温度す
なわち、本例では鋼板4の板厚方向の平均温度の
変化を示している。
First, it is known that the temperature change at any point where the above sampling was performed is as shown in FIG. The horizontal axis in the figure is the time from the start of water cooling, and t = τ〓 and τ〓 + Δτ p indicate the time when water cooling is stopped and the time when reheating is completed after stopping water cooling, respectively.
The vertical axis is temperature, and the curve shows the change in the surface temperature of the steel plate 4 at the arbitrary point, and the curve shows the change in the representative temperature at this arbitrary point, that is, in this example, the average temperature in the thickness direction of the steel plate 4.

図示するように、水冷却停止後の状態は2つの
領域により構成されている。すなわち、第1の状
態は水冷却停止後の復熱過程で、時間t=τ〓〜τ〓
+Δτpまでで、第2の状態は復熱完了後の過程、
で、時間t=τ〓+Δτp以降である。
As shown in the figure, the state after water cooling is stopped consists of two regions. That is, the first state is the reheating process after stopping water cooling, and the time t=τ〓~τ〓
+Δτ p , the second state is the process after completion of reheating,
Then, after time t=τ〓+Δτ p .

また、上記のように、本発明においては同一場
所にて、複数時点でサンプリングを実施するので
あるが、以下サンプリング回数が2回の場合を例
として(第2図参照、復熱完了前後の各々で2回
ずつ測定した場合を同じ記号で示してある。)、第
3図に示すフローチヤートに従つて説明する。
In addition, as mentioned above, in the present invention, sampling is carried out at the same location at multiple points in time. Below, we will take an example of a case where the number of samplings is two (see Figure 2, each time before and after the completion of reheating). (The same symbol indicates the case where each measurement was made twice.), will be explained according to the flowchart shown in FIG.

ステツプで水冷却停止後、鋼板4の停止時に
(τi,Ti)をサンプリングする。ここで、 τi:水冷却開始からの時間 Ti:時間t=τiでの鋼板4の表面温度 i:1,2 である。
After water cooling is stopped in the step, (τ i , Ti) is sampled when the steel plate 4 is stopped. Here, τ i : Time from the start of water cooling Ti: Surface temperature of the steel plate 4 at time t=τ i i: 1,2.

ステツプで次式により代表温度の時間経過に
対する変化量Rtと代表表面温度TAVを算出する。
In step, the amount of change Rt in the representative temperature over time and the representative surface temperature TAV are calculated using the following equation.

Rt=(T2−T1)/(τ2−τ1) TAV=(T2+T1)/2 ステツプでRtの正負を判別し、すなわちサン
プリング時点で鋼板4の表面温度が上昇中である
か否かを判別し、Rt>0のときは復熱中の状態
にあり、ステツプに進み、Rt0のときは復
熱完了後の状態にあり、ステツプ〓に進む。
Rt = (T 2 - T 1 ) / (τ 2 - τ 1 ) T AV = (T 2 + T 1 ) / 2 Steps determine whether Rt is positive or negative, that is, the surface temperature of the steel plate 4 is rising at the time of sampling. If Rt > 0, the system is in the state of recuperation, and the process proceeds to step 2. If Rt is 0, the state is in the state after the completion of reheating, and the process proceeds to step 0.

ステツプ〜で、2つ以上用意された基準温
度群の中より2つの適宜基準温度Ti(i=1,
2)、例えばT1=300℃,T2=550℃を定め、この
基準温度Ti毎に、復熱完了時の表面温度Tpsと、
代表表面温度TAVとの差DTl(=Tps−TAV)、上記
表面温度Tpsと板厚方向平均温度TPAとの差ΔTpl
(=Tps−TPA)、水冷却停止から復熱完了までの
時間Δτlおよび空冷による鋼板4の表面降下速度
Vclを次のように表わし、各々の値を計算する。
In step ~, two appropriate reference temperatures Ti (i=1,
2) For example, set T 1 = 300°C and T 2 = 550°C, and for each reference temperature Ti, determine the surface temperature T ps at the completion of reheating,
Difference from the representative surface temperature T AV DT l (=T ps − T AV ), difference ΔT pl between the above surface temperature T ps and the average temperature T PA in the plate thickness direction
(=T ps −T PA ), time Δτ l from water cooling stop to completion of reheating, and surface fall rate of steel plate 4 due to air cooling
Express V cl as follows and calculate each value.

DT550=5.176×10-3・ω0.02237・t1.845 ・Rt+(0055・t−2.60)・ logω+0.072t−3.90[℃] ω:下面水量密度(最終バンク)[m3/min・
m2] DT300=3.236×10・ω0.00942・t1.871 ・Rt+0.012t−0.55 ΔTp550=1.274×10-1・t0.960[℃] ΔTp330=2.044×10-2・t0.980 Δτp550=10m1 m1=(−0.131・logt+0.288)・logω+
1.87・logt−1.55 Δτp300=10m2 m2=(−0.0736・logt+0.152)・logω+
1.83・logt−1.56 Vc550=5.929・t-0.8865[℃/sec] Vc330=1.756・t-0.8295 ステツプで、水冷却停止後の時間ΔτPl間にお
ける空冷による降下温度ΔTfPlを次式 ΔTfPl=Vcl・Δτpl [℃] により算出する。
DT 550 = 5.176×10 -3・ω 0.02237・t 1.845・Rt+(0055・t−2.60)・logω+0.072t−3.90 [℃] ω: Bottom water density (final bank) [m 3 /min・
m 2 ] DT 300 = 3.236×10・ω 0.00942・t 1.871・Rt+0.012t−0.55 ΔT p550 = 1.274×10 -1・t 0.960 [℃] ΔT p330 = 2.044×10 -2・t 0.980 Δτ p550 = 10 m1 m1=(-0.131・logt+0.288)・logω+
1.87・logt−1.55 Δτ p300 =10 m2 m2=(−0.0736・logt+0.152)・logω+
1.83・logt−1.56 V c550 = 5.929・t -0.8865 [℃/sec] V c330 = 1.756・t -0.8295 steps, the temperature drop ΔT fPl due to air cooling during the time Δτ Pl after stopping water cooling is calculated by the following formula: ΔT fPl Calculated using =V cl・Δτ pl [°C].

ステツプで、次式により基準停止温度TfTl
算出する。
In step, the reference stop temperature T fTl is calculated using the following formula.

Tf550=TAV+DT550+ΔTp550+ΔTfp550 Tf330=TAV+DT300+ΔTp300+ΔTfp300 ステツプで、適宜目標冷却停止温度T′fpを設
定して、冷却停止温度Tfeoを次式、 Tfeo=Tf300+(Tf550−Tf300) ・(T′fp−300)/(550−300) により算出する。
T f550 = T AV + DT 550 + ΔT p550 + ΔT fp550 T f330 = T AV + DT 300 + ΔT p300 + ΔT fp300 Step, set the target cooling stop temperature T' fp as appropriate, and calculate the cooling stop temperature T feo by the following formula, T feo = Calculated using T f300 + (T f550 − T f300 ) ・(T′ fp −300)/(550−300).

さらに、計算精度向上のために、必要に応じて
ステツプに進んで、上記ステツプの式におい
て目標冷却停止温度T′fpを冷却停止温度Tfeoに置
換えて新たに修正後の冷却停止温度Tfeo+1を求
め、これを新たに冷却停止温度Tfeoとする。すな
わち、修正後の冷却停止温度Tfeo+1を次式 Tfeo+1=Tf300+(Tf550−Tf300) ・(Tfeo−300)/(550−300) により算出して、Tfeo+1を新たにTfeoとする。
Furthermore, in order to improve the calculation accuracy, proceed to the step as necessary to replace the target cooling stop temperature T′ fp with the cooling stop temperature T feo in the formula in the above step to obtain the newly corrected cooling stop temperature T feo+ 1 and set it as the new cooling stop temperature T feo . In other words, the corrected cooling stop temperature T feo+1 is calculated by the following formula T feo+1 = T f300 + (T f550 − T f300 ) ・(T feo −300)/(550−300), and T feo Set +1 as new T feo .

ステツプで、ステツプで最初の計算により
得た冷却停止温度Tfeoあるいは適宜回数だけステ
ツプ,にのループを繰返して得た冷却停止温
度Tfeoを最終的に冷却停止温度と決定する。
In step, the cooling stop temperature T feo obtained by the initial calculation in step or the cooling stop temperature T feo obtained by repeating the loop of steps and steps an appropriate number of times is finally determined as the cooling stop temperature.

一方、Rt0のときはステツプ〜に進み、
上記同様に表面温度降下速度Vcを表すとともに、
上記代表表面温度TAVと板厚方向平均温度TnA
の差ΔTnl(=TAV−TnA)および空冷による鋼板
4表面の降下温度ΔTfnlを次のように表わし各々
の値を計算する。
On the other hand, when Rt0, proceed to step ~,
In the same way as above, the surface temperature drop rate V c is expressed, and
The difference ΔT nl (= T AV − T nA ) between the representative surface temperature T AV and the average temperature T nA in the plate thickness direction and the temperature drop ΔT fnl on the surface of the steel plate 4 due to air cooling are expressed as follows and the respective values are calculated. .

ΔTn550≒ΔTp550=1.274×10-1・t0.960[℃] ΔTn300≒ΔTp300=2.044×10-2・t0.980 ΔTfn550=Vc550・ΔτAV [℃] ΔTfn300=Vc300・ΔτAV ΔτAV=(τ1+τ2)/2−τ〓 [sec] ただし、ΔτAV:代表空冷時間、τ〓:水冷時間 ステツプで次式により基準停止温度TfT1を算
出する。
ΔT n550 ≒ΔT p550 =1.274×10 -1・t 0.960 [℃] ΔT n300 ≒ΔT p300 =2.044×10 -2・t 0.980 ΔT fn550 =V c550・Δτ AV [℃] ΔT fn300 =V c300・Δτ AV Δτ AV = (τ 1 + τ 2 )/2−τ〓 [sec] However, Δτ AV : representative air-cooling time, τ: water-cooling time. In step, calculate the reference stop temperature T fT1 using the following formula.

Tf550=TAV+ΔTn550+ΔTfn550 Tf300=TAV+ΔTn300+ΔTfn300 ステツプ〜で、上記ステツプ〜と同様
にして冷却停止温度Tfeoを求める。
T f550 = T AV + ΔT n550 + ΔT fn550 T f300 = T AV + ΔT n300 + ΔT fn300 In steps ~, determine the cooling stop temperature T feo in the same manner as in steps ~ above.

第4図は、以上の手順にしたがつて行なつた計
算例を示し、横軸に最初に仮定した目標冷却停止
温度T′fp、縦軸に予測誤差(=Tfei−Tfp,Tfp
冷却停止温度の真の値)をとり、冷却停止温度の
計算を1回だけ行なつて求めた場合(n=1)と
上記ループにより3回繰返して行なつた場合(n
=3)と比較したものである。
Figure 4 shows an example of calculation performed according to the above procedure, where the horizontal axis is the initially assumed target cooling stop temperature T' fp , and the vertical axis is the prediction error (=T fei - T fp , T fp is the true value of the cooling stop temperature), and the case where the cooling stop temperature is calculated only once (n = 1) and the case where it is calculated three times using the above loop (n
=3).

また、図中Aはt=50mm,ω=0.15m3/min・
m2で冷却し、5秒後の測温より予測した場合、B
はt=50mm,ω=1.0m3/min・m2,20秒後の測
温より予測した場合を示している。
In addition, A in the figure is t=50mm, ω=0.15m 3 /min・
When predicted from the temperature measurement after 5 seconds after cooling at m2 , B
shows the case where t=50mm, ω=1.0m 3 /min·m 2 , and predicted from temperature measurement 20 seconds later.

図より明らかなように、A,Bいずれの場合も
仮定した目標冷却停止温度の値如何でn=1では
予測誤差が増大するが、n=3ではこの目標冷却
停止温度の値に影響されず殆ど一定値となる。す
なわち、目標冷却停止温度大小による計算結果の
ばらつきは、冷却停止温度の計算を3回も繰返え
せば殆どなくなる。
As is clear from the figure, in both cases A and B, the prediction error increases when n = 1, depending on the assumed target cooling stop temperature, but when n = 3, it is not affected by the value of the target cooling stop temperature. It becomes an almost constant value. In other words, variations in calculation results due to the magnitude of the target cooling stop temperature are almost eliminated by repeating the calculation of the cooling stop temperature three times.

(発明の効果) 以上の説明より明らかなように、本発明によれ
ば強制冷却後の状態を復熱過程と復熱完了後の2
つの領域に別けて、いずれの領域において被冷却
材の表面温度をサンプリングしても、各々の領域
の特性に合わせて冷却停止温度を算出するように
してある。このため強制冷却後の被冷却材が復熱
した後は勿論、冷却後の復熱完了を待たずに被冷
却材の停止温度を求めることができるため、製品
の品質管理や、適切な冷却のために強制冷却手段
へのフイードバツクを迅速に行うことができ、生
産性の向上を図れる。
(Effects of the Invention) As is clear from the above explanation, according to the present invention, the state after forced cooling is divided into the recuperation process and the two after completion of reheating.
Even if the surface temperature of the material to be cooled is sampled in any of the two regions, the cooling stop temperature is calculated in accordance with the characteristics of each region. Therefore, the stop temperature of the cooled material can be determined not only after the cooled material has recovered heat after forced cooling, but also without waiting for the completion of recuperation after cooling, which can be used for product quality control and proper cooling. Therefore, feedback to the forced cooling means can be quickly provided, and productivity can be improved.

また、2つの基準温度毎に基準冷却停止温度を
求め、この数値を基にして組立てた計算式を使つ
て冷却停止温度を算出できるようにしてあるた
め、この温度がいくらであつても、温度毎に別の
式を使う必要がなくなり、計算が単純化できる等
の効果を奏する。
In addition, the standard cooling stop temperature is determined for each of the two standard temperatures, and the cooling stop temperature can be calculated using a calculation formula based on these values. There is no need to use a separate formula each time, and calculations can be simplified.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は厚板圧延設備の概略機器構成図、第2
図は鋼板の冷却線模式図、第3図は本発明に係る
フローチヤート、第4図は本発明に係る方法を第
2図に示す模式的なモデルに適用して計算した結
果を示す図である。 2……冷却設備、4……鋼板、7……出側温度
計。
Figure 1 is a schematic equipment configuration diagram of the plate rolling equipment, Figure 2
The figure is a schematic diagram of the cooling line of a steel plate, Figure 3 is a flowchart according to the present invention, and Figure 4 is a diagram showing the results of calculations by applying the method according to the present invention to the schematic model shown in Figure 2. be. 2... Cooling equipment, 4... Steel plate, 7... Outlet side thermometer.

Claims (1)

【特許請求の範囲】 1 高温の被冷却材を強制冷却した後、空冷時間
を設けて、被冷却材の表面温度を測定し、強制冷
却停止時の被冷却材移送方向に対して直交する断
面の代表温度を求める被冷却材の強制冷却停止温
度推定方法において、被冷却材の代表点を少なく
とも1つ設定し、その代表点にて、あるサンプリ
ング時間を経て、被冷却材表面温度を少なくとも
2回測定して得たサンプル値から代表表面温度
TAVを求めるとともに、代表点における温度が上
昇中であるか否かを判定し、上昇中の場合には、
2つの適宜基準温度Tl(l=1,2)毎に復熱完
了時の表面温度と上記代表表面温度TAVとの差
DTlと、復熱完了時の表面温度とその点における
板厚方向平均温度との差ΔTplと、強制冷却停止
後復熱完了までの間の空冷による降下温度ΔTfpl
とを水量密度、被冷却材の厚さおよび代表温度変
化の関数として表わし、基準冷却停止温度T′fTl
次式 TfTl=TAV+DTl+ΔTpl+ΔTfpl により算出とともに、適宜目標冷却停止温度T′fp
を設定して、冷却停止温度Tfeoを次式 Tfeo=TfT1+(TfT2−TfT1)・(T′fel−T1) /(T2−T1) により算出し、計算精度向上のための必要に応じ
て、上記冷却停止温度Tfeoを用いて修正後の冷却
停止温度Tfeo+1を求める計算を次式 Tfeo+1=TfT1+(TfT2−TfT1)・(Tfeo−T1) /(T2−T1) により算出してTfeo+1を新たにTfeoとし、この計
算を適宜回数繰返して冷却停止温度Tfeoを算出す
る一方、上記代表点における温度が上昇中でない
場合には、上記基準温度Tl(l=1,2)毎に代
表表面温度TAVと、その温度の時の板厚方向の平
均温度との差ΔTnlと、強制冷却停止後のサンプ
リングまでの間の空冷による降下温度ΔTfnlとを
被冷却材の厚さおよび空冷時間の関数として表わ
し、基準冷却停止温度TfTlを次式 TfAl=TAV+ΔTnl+ΔTfnl により算出して、以下上記同様にして冷却停止温
度Tfeoを算出することを特徴とする被冷却材の強
制冷却停止温度の推定方法。
[Claims] 1. After forcibly cooling a high-temperature material to be cooled, an air cooling period is provided, the surface temperature of the material to be cooled is measured, and a cross section perpendicular to the direction of transport of the material to be cooled when forced cooling is stopped is measured. In the method for estimating the forced cooling stop temperature of a material to be cooled, at least one representative point of the material to be cooled is set, and at that representative point, after a certain sampling time, the surface temperature of the material to be cooled is determined by at least 2 points. The representative surface temperature is calculated from the sample value obtained by measuring twice.
In addition to finding T AV , it is determined whether the temperature at the representative point is rising, and if it is rising,
The difference between the surface temperature at the time of completion of reheating and the above representative surface temperature T AV for each of two appropriate reference temperatures T l (l = 1, 2)
DT l , the difference between the surface temperature at the completion of reheating and the average temperature in the plate thickness direction at that point ΔT pl , and the temperature drop due to air cooling between the forced cooling stop and the completion of reheating ΔT fpl
is expressed as a function of water flow density, thickness of the material to be cooled, and representative temperature change, and the reference cooling stop temperature T' fTl is calculated by the following formula: T fTl = T AV + DT l + ΔT pl + ΔT fpl , and the target cooling stop temperature is calculated as appropriate. T′ fp
The cooling stop temperature T feo is calculated using the following formula T feo = T fT1 + (T fT2 − T fT1 )・(T′ fel − T 1 ) / (T 2T 1 ) to improve calculation accuracy. If necessary, calculate the corrected cooling stop temperature T feo+1 using the above cooling stop temperature T feo using the following formula: T feo+1 = T fT1 + (T fT2 − T fT1 )・( T feo - T 1 ) / (T 2 - T 1 ) T feo+1 is newly set as T feo , and this calculation is repeated an appropriate number of times to calculate the cooling stop temperature T feo . If the temperature is not rising, the difference ΔT nl between the representative surface temperature T AV and the average temperature in the plate thickness direction at that temperature, and the forced cooling for each reference temperature T l (l = 1, 2) The temperature drop ΔT fnl due to air cooling after stopping until sampling is expressed as a function of the thickness of the material to be cooled and the air cooling time, and the standard cooling stop temperature T fTl is calculated using the following formula: T fAl = T AV + ΔT nl + ΔT fnl A method for estimating a forced cooling stop temperature of a material to be cooled, characterized in that the cooling stop temperature T feo is calculated in the same manner as described above.
JP60185622A 1985-08-22 1985-08-22 Method for estimating forced cooling stopping temperature of material to be cooled Granted JPS6244528A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60185622A JPS6244528A (en) 1985-08-22 1985-08-22 Method for estimating forced cooling stopping temperature of material to be cooled

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60185622A JPS6244528A (en) 1985-08-22 1985-08-22 Method for estimating forced cooling stopping temperature of material to be cooled

Publications (2)

Publication Number Publication Date
JPS6244528A JPS6244528A (en) 1987-02-26
JPH0480975B2 true JPH0480975B2 (en) 1992-12-21

Family

ID=16174011

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60185622A Granted JPS6244528A (en) 1985-08-22 1985-08-22 Method for estimating forced cooling stopping temperature of material to be cooled

Country Status (1)

Country Link
JP (1) JPS6244528A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0692312B2 (en) * 1989-02-01 1994-11-16 株式会社赤羽精銀研究所 Method for producing cell activator

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60185623A (en) * 1984-07-10 1985-09-21 Matsushita Electric Ind Co Ltd In-vehicle air purifier

Also Published As

Publication number Publication date
JPS6244528A (en) 1987-02-26

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