JPS6237693B2 - - Google Patents
Info
- Publication number
- JPS6237693B2 JPS6237693B2 JP22849682A JP22849682A JPS6237693B2 JP S6237693 B2 JPS6237693 B2 JP S6237693B2 JP 22849682 A JP22849682 A JP 22849682A JP 22849682 A JP22849682 A JP 22849682A JP S6237693 B2 JPS6237693 B2 JP S6237693B2
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- refrigerant
- steel wire
- control device
- cooling
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING 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
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/62—Quenching devices
- C21D1/63—Quenching devices for bath quenching
- C21D1/64—Quenching devices for bath quenching with circulating liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Control Of Heat Treatment Processes (AREA)
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Description
【発明の詳細な説明】
本発明は鋼線材直接熱処理設備の制御装置に関
し、鋼線材を正確に所定の目標温度に冷却し得る
ように企図したものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a control device for direct heat treatment equipment for steel wire rods, and is designed to accurately cool steel wire rods to a predetermined target temperature.
熱間圧延された高温の鋼線材は、液状の冷媒で
ある溶融塩に直接接触させられて冷却される。こ
の場合、冷却された鋼線材の性質が均一になるよ
うに、冷却された鋼線材が常に所定の目標温度に
なることが要請されるため、溶融塩もある一定の
温度に保持される必要がある。 The hot-rolled high-temperature steel wire is cooled by being brought into direct contact with molten salt, which is a liquid coolant. In this case, the molten salt must also be maintained at a certain temperature because it is required that the cooled steel wire always reach a predetermined target temperature so that the properties of the cooled steel wire are uniform. be.
鋼線材の処理量が少ない場合には、冷却槽に貯
留された溶融塩を電熱で加熱したり、冷却槽の外
面を空冷したりすることにより溶融塩の温度を保
持していた。このように処理量が少ないため溶融
塩に持ち込まれる熱量が小さい場合には、上述し
たような簡便な手段によつても充分に溶融塩の温
度を一定に保持できた。 When the amount of steel wire to be processed is small, the temperature of the molten salt stored in the cooling tank is maintained by heating it with electric heat or by cooling the outer surface of the cooling tank with air. When the amount of heat carried into the molten salt was small due to the small amount of treatment, the temperature of the molten salt could be sufficiently kept constant even by the above-mentioned simple means.
一方、鋼線材の処理量が多くなると鋼線材から
溶融塩に伝わる熱量が非常に大きくなるため、空
冷だけでは冷却能力が不足となる。そこで鋼線材
を多量に冷却処理するには、一般に第1図に示す
ような説備が使用される。つまり、第1図に示す
ように冷却槽1には溶融塩2が貯溜されており、
熱間圧延されて搬送されてきた高温の鋼線材3
は、特に第2図に示すようにループ状にされて図
中冷却槽1の左側から溶融塩2中に浸漬されて冷
却されるとともに、冷却槽1の右側から引き上げ
られる。鋼線材3から熱を受けて高温となつた溶
融塩2はポンプ4により熱交換器5に送られ、こ
こで冷却され、冷却された溶融塩2は再び冷却槽
1に戻される。前記熱交換器5での溶融塩の冷却
は、熱交換器5に供給される水6により行なわれ
る。 On the other hand, as the amount of steel wire rods processed increases, the amount of heat transferred from the steel wire rods to the molten salt becomes very large, so air cooling alone becomes insufficient in cooling capacity. Therefore, in order to cool a large amount of steel wire, a procedure as shown in FIG. 1 is generally used. That is, as shown in FIG. 1, molten salt 2 is stored in the cooling tank 1,
High temperature steel wire rod 3 that has been hot rolled and transported
In particular, as shown in FIG. 2, it is made into a loop shape and is immersed in the molten salt 2 from the left side of the cooling tank 1 in the figure to be cooled, and is pulled up from the right side of the cooling tank 1. The molten salt 2, which has become high in temperature due to receiving heat from the steel wire 3, is sent to a heat exchanger 5 by a pump 4, where it is cooled, and the cooled molten salt 2 is returned to the cooling tank 1 again. Cooling of the molten salt in the heat exchanger 5 is performed by water 6 supplied to the heat exchanger 5.
第1図に示す設備によれば、充分な冷却能力が
あるため、多量の鋼線材3を冷却することができ
る。さらに、鋼線材3の線径・搬送速度が一定で
あるならば、熱交換器3の冷却量をある一定の値
にしておけば、溶融塩2から引き上げられた直後
の鋼線材3の温度は、あらかじめ定めた目標温度
とほぼ等しくなる。 According to the equipment shown in FIG. 1, since there is sufficient cooling capacity, a large amount of steel wire rod 3 can be cooled. Furthermore, if the wire diameter and transport speed of the steel wire 3 are constant, and the cooling amount of the heat exchanger 3 is set to a certain value, the temperature of the steel wire 3 immediately after being lifted from the molten salt 2 will be , becomes almost equal to the predetermined target temperature.
しかし上述した技術では冷却された鋼線材3の
温度と目標温度とを正確に一致させることは難し
いばかりでなく、線径の異なる鋼線材を冷却した
り鋼線材の搬送速度を変えたりした場合には、冷
却された鋼線材の温度と目標温度とが大きく相違
してしまう。さらに、複数の目標温度を設定して
おき、そのうちの一つを正確に選択するというこ
とも困難であつた。 However, with the above technology, it is not only difficult to accurately match the temperature of the cooled steel wire 3 with the target temperature, but also when cooling steel wires with different diameters or changing the conveyance speed of the steel wires. In this case, the temperature of the cooled steel wire rod and the target temperature are greatly different. Furthermore, it is difficult to set a plurality of target temperatures and accurately select one of them.
本発明は、上記実状に鑑み、鋼線材を正確に所
定の目標温度に冷却し得る制御装置を提供するこ
とを目的とする。かかる目的を達成する本発明
は、鋼線材の線径・搬送速度および所定の目標温
度を設定することにより鋼線材の温度と冷媒の温
度との間にあるあらかじめ定まつた熱バランス式
を基に、鋼線材を目標温度に冷却するのに最適な
冷媒の温度を演算し、冷媒が演算した温度になる
ように制御する点をその技術思想の基礎とする。 SUMMARY OF THE INVENTION In view of the above circumstances, an object of the present invention is to provide a control device that can accurately cool a steel wire to a predetermined target temperature. The present invention achieves the above object by setting the wire diameter and conveyance speed of the steel wire and a predetermined target temperature, based on a predetermined heat balance equation between the temperature of the steel wire and the temperature of the refrigerant. The basis of its technical philosophy is to calculate the temperature of the refrigerant that is optimal for cooling the steel wire to a target temperature, and to control the refrigerant to the calculated temperature.
ここで本発明を説明するのに先だち熱バランス
式を次式(1)に示しておく。なお冷却槽は完全混合
系とする。 Before explaining the present invention, a heat balance equation will be shown in the following equation (1). The cooling tank will be a complete mixing system.
但し
α:冷媒(溶融塩)と鋼線材の熱伝達率
A:鋼線材の表面積(鋼線材の処理量、搬送速
度および線径の関数)
C1:鋼線材の比熱
C2:冷媒(溶融塩)の比熱
W1:鋼線材処理量
W2:冷媒(溶融塩)循環流量
T1I:冷媒(溶融塩)に浸漬される直前の鋼線
材の温度(一定とみなす)
T1O:(溶融塩)から引き上げられた直後の鋼
線材の温度
T2I:熱交換器から冷却槽に戻される冷媒(溶
融塩)の温度
T2:冷却槽内の冷媒(溶融塩)の温度
Δtm:
QL:熱損失
Q2:熱交換器による冷却量
とする。 However, α: Heat transfer coefficient between refrigerant (molten salt) and steel wire rod A: Surface area of steel wire rod (function of throughput of steel wire rod, conveyance speed, and wire diameter) C 1 : Specific heat of steel wire rod C 2 : Refrigerant (molten salt) ) Specific heat of steel wire W 1 : Steel wire throughput W 2 : Refrigerant (molten salt) circulation flow rate T 1I : Temperature of steel wire just before being immersed in refrigerant (molten salt) (assumed to be constant) T 1O : (molten salt) T 2I : Temperature of the refrigerant (molten salt) returned from the heat exchanger to the cooling tank T 2 : Temperature of the refrigerant (molten salt) in the cooling tank Δtm: Q L : Heat loss Q 2 : Amount of cooling by the heat exchanger.
なお本発明は冷媒の温度を検出してこの検出し
た温度が、式(1)を基に演算した温度になるように
冷媒を制御するものであるが、鋼線材温度を検出
して鋼線材温度をフイードバツク制御する制御系
を形成することも考えられるが、このような制御
系では鋼線材を正確に所定の目標温度に冷却する
よう制御することは困難である。この理由として
は、一つには鋼線材がループ状になり冷媒(溶融
塩)に浸漬させられて搬送されるため、この鋼線
材の温度を連続的に精度よく検出することが困難
であることが挙げられ、他の一つとしては、鋼線
材が冷媒中を通過する時間が10〜20秒程度である
のに対し冷却槽の熱容量が大きい(熱交換器から
冷却槽に戻される冷媒の温度変化に対する冷却槽
内温度の時定数は30分程度)ことが挙げられる。 Note that the present invention detects the temperature of the refrigerant and controls the refrigerant so that the detected temperature becomes the temperature calculated based on equation (1). Although it is conceivable to form a control system that performs feedback control of the temperature, it is difficult to control the steel wire to accurately cool it to a predetermined target temperature with such a control system. One reason for this is that since the steel wire is transported in a loop shape and immersed in a refrigerant (molten salt), it is difficult to continuously and accurately detect the temperature of the steel wire. Another reason is that the time it takes for steel wire to pass through the refrigerant is about 10 to 20 seconds, whereas the heat capacity of the cooling tank is large (the temperature of the refrigerant returned from the heat exchanger to the cooling tank is The time constant of the temperature inside the cooling tank relative to changes is about 30 minutes).
以下、本発明の実施例を図面に基づき詳細に説
明する。なお従来技術と同一部分には同一番号を
付し重複する説明は省略する。 Hereinafter, embodiments of the present invention will be described in detail based on the drawings. Note that parts that are the same as those in the prior art are given the same numbers and redundant explanations will be omitted.
第3図は本発明の第1の実施例を示す。同図に
示すように、冷媒温度検出器7は、冷却槽1内に
配置されてこの冷却槽1に貯留された溶融塩2に
温度T2を検出し、検出値を冷媒温度制御装置8
に送出する。演算装置9は、鋼線材3の線径(d)・
搬送速度(ν)および所定の目標温度(式(1)にお
いて温度T1Oをある所定の温度としたもの)から
なる運転条件が設定(インプツト)されると、前
述した熱バランス式(1)を基に鋼線材3を目標温度
に冷却するのに最適な溶融塩2の温度を演算す
る。この演算によつて求められる温度は、冷却槽
1内の溶融塩2の温度T2がなるべき温度T2′、ま
たは熱交換器5から冷却槽1に戻される溶融塩の
温度T2Iがなるべき温度T2I′である。つまり演
算装置9は、運転条件が設定されると次式(2),(3)
の演算を行う。 FIG. 3 shows a first embodiment of the invention. As shown in the figure, a refrigerant temperature detector 7 is arranged in a cooling tank 1 and detects a temperature T 2 of a molten salt 2 stored in the cooling tank 1, and transmits the detected value to a refrigerant temperature control device 8.
Send to. The calculation device 9 calculates the wire diameter (d) of the steel wire 3.
When the operating conditions consisting of the conveyance speed (ν) and a predetermined target temperature (temperature T 1O is set to a certain predetermined temperature in equation (1)) are set (input), the heat balance equation (1) described above is Based on this, the optimum temperature of the molten salt 2 for cooling the steel wire rod 3 to the target temperature is calculated. The temperature obtained by this calculation is the temperature T 2 ' that the temperature T 2 of the molten salt 2 in the cooling tank 1 should be, or the temperature T 2I of the molten salt returned to the cooling tank 1 from the heat exchanger 5. The power temperature is T 2I '. In other words, the calculation device 9 calculates the following equations (2) and (3) when the operating conditions are set.
Perform the calculation.
T2′=1(d,ν,T1O) ……(2)
T2′I=2(d,ν,T1O) ……(3)
そして本実施例では、演算された温度T2′,T2
I′のうち、温度T2′のみが冷媒温度制御装置8に
送出されるようになつている。冷媒温度制御装置
8は、前記冷媒温度検出器7で検出された温度
T2と演算装置9で演算された温度T2′とを比較
し、温度T2が温度T2′に等しくなるように冷却量
制御装置10を制御する。つまり冷却量制御装置
10は、冷媒温度制御装置8で制御されることに
より、温度T2が温度T2′よりも大きいときには給
水弁11を大きく開いて熱交換器5の冷却量が増
加するようにし、温度T2が温度T2′よりも小さい
ときには給水弁11をしぼり熱交換器5の冷却量
が減少するよう操作される。なお、同図の符号で
12は給水量検出器でありこれの検出値は冷却量
制御装置10に入力される。 T 2 ′= 1 (d, ν, T 1O ) ...(2) T 2 ′ I = 2 (d, ν, T 1O ) ...(3) And in this example, the calculated temperature T 2 ′ ,T 2
Of I ', only the temperature T2 ' is sent to the refrigerant temperature control device 8. A refrigerant temperature control device 8 controls the temperature detected by the refrigerant temperature detector 7.
The temperature T 2 is compared with the temperature T 2 ′ calculated by the calculation device 9, and the cooling amount control device 10 is controlled so that the temperature T 2 becomes equal to the temperature T 2 ′. In other words, the cooling amount control device 10 is controlled by the refrigerant temperature control device 8, so that when the temperature T 2 is higher than the temperature T 2 ′, the water supply valve 11 is opened wide to increase the cooling amount of the heat exchanger 5. When the temperature T 2 is lower than the temperature T 2 ', the water supply valve 11 is throttled to reduce the cooling amount of the heat exchanger 5. In addition, the reference numeral 12 in the figure is a water supply amount detector, and the detected value of this is inputted to the cooling amount control device 10.
上述した如く本実施例では冷却槽1内の冷媒3
の温度T2が、鋼線材2が目標温度に冷却される
よう演算された最適な温度T2′に等しくなるよう
に冷媒2の温度が制御される結果、冷媒3から引
き上げられた直後の鋼線材3の温度は精度よくあ
らかじめ設定した目標温度になる。 As mentioned above, in this embodiment, the refrigerant 3 in the cooling tank 1
As a result of controlling the temperature of the refrigerant 2 so that the temperature T 2 of the steel wire rod 2 becomes equal to the optimum temperature T 2 ' calculated to cool the steel wire rod 2 to the target temperature, the temperature of the steel immediately after being lifted from the refrigerant 3 The temperature of the wire 3 becomes a preset target temperature with high accuracy.
第4図は本発明の第2の実施例を示す。この実
施例では、冷媒温度検出器7は、熱交換器5で冷
却されて冷却槽7に戻される溶融塩2に接触する
ように配置されており、この溶融塩2の温度T2I
を測定する。そしてこの温度T2Iは冷媒温度制御
装置8に送出される。一方、演算装置9は演算し
た温度T2′,T2I′のうち温度T2I′のみを冷媒温度
制御装置8に送出する。そして温度T2Iが温度T
2I′に等しくなるように冷媒2の温度が制御さ
れ、鋼線材3は目標温度に冷却される。なお第1
の実施例と同一部分には同一番号を付し、重複す
る説明は省く。 FIG. 4 shows a second embodiment of the invention. In this embodiment, the refrigerant temperature detector 7 is arranged so as to be in contact with the molten salt 2 that is cooled by the heat exchanger 5 and returned to the cooling tank 7, and the temperature T 2I of this molten salt 2
Measure. This temperature T 2I is then sent to the refrigerant temperature control device 8. On the other hand, the computing device 9 sends only the temperature T 2I ′ out of the computed temperatures T 2 ′ and T 2I ′ to the refrigerant temperature control device 8 . And the temperature T 2I is the temperature T
The temperature of the refrigerant 2 is controlled to be equal to 2I ', and the steel wire 3 is cooled to the target temperature. Note that the first
The same parts as those in the embodiment are given the same numbers, and redundant explanations will be omitted.
第5図は本発明の第3の実施例を示す。本実施
例は、第2の実施例に、熱交換器5の水のレベル
を検出するレベル検出器13とレベル調節計14
を付加したものであり、熱交換器5の冷却量をよ
り正確に調節することができる。 FIG. 5 shows a third embodiment of the invention. In this embodiment, a level detector 13 for detecting the water level of the heat exchanger 5 and a level controller 14 are added to the second embodiment.
The amount of cooling of the heat exchanger 5 can be adjusted more accurately.
以上実施例とともに具体的に説明したように本
発明によれば、鋼線材の線径・搬送速度が異なつ
ていてもこれを設定することにより、鋼線材を正
確に所定の目標温度に冷却することができる。ま
た目標温度自体も種々の値に設定できる。 As specifically explained above with the embodiments, according to the present invention, even if the wire diameter and conveyance speed of the steel wire rod are different, by setting these, the steel wire rod can be accurately cooled to a predetermined target temperature. be able to. Further, the target temperature itself can be set to various values.
第1図は鋼線材直接熱処理設備を示す概略構成
図、第2図は冷媒中に浸漬される鋼線材の形態を
示す斜視図、第3図〜第5図はそれぞれ本発明の
第1〜第3の実施例を鋼線材直接熱処理設備に備
えた態様で示す概略構成図である。
図面中、1は冷却槽、2は溶融塩(冷媒)、3
は鋼線材、5は熱交換器、6は水、7は冷媒温度
検出器、8は冷媒温度制御装置、9は演算装置、
10は冷却量制御装置、11は給水弁である。
Fig. 1 is a schematic configuration diagram showing a steel wire direct heat treatment equipment, Fig. 2 is a perspective view showing the form of steel wire immersed in a refrigerant, and Figs. FIG. 3 is a schematic configuration diagram illustrating the third embodiment as installed in steel wire direct heat treatment equipment. In the drawing, 1 is a cooling tank, 2 is a molten salt (refrigerant), and 3 is a cooling tank.
is a steel wire, 5 is a heat exchanger, 6 is water, 7 is a refrigerant temperature detector, 8 is a refrigerant temperature control device, 9 is a calculation device,
10 is a cooling amount control device, and 11 is a water supply valve.
Claims (1)
却槽に貯留された液状の冷媒に一旦浸漬させてか
ら引き上げることにより冷却する鋼線材冷却装置
と、前記冷却槽から冷媒が流入されてこの冷媒を
冷却するとともに冷却した冷媒を再び冷却槽に戻
す熱交換器とで構成されて、高温の前記鋼線材を
所定の目標温度にまで冷却する鋼線材直接熱処理
設備に備えられる制御装置において、前記冷却槽
内の冷媒に浸漬されるよう配置されるかまたは前
記熱交換器から冷却槽に戻される冷媒に接触する
よう配置されて配置位置における冷媒の温度を検
出する冷媒温度検出器と、鋼線材の線径・搬送速
度および前記所定の目標温度が設定されることに
より鋼線材の温度と冷媒の温度との間にあるあら
かじめ定まつた熱バランス式を基に鋼線材を目標
温度に冷却するのに最適な冷媒の温度を演算する
演算装置と、前記熱交換器の冷却量を調節する冷
却量制御装置と、冷媒温度検出器で検出された温
度と演算装置で演算された温度とを比較し検出さ
れた温度が演算された温度に等しくなるように前
記冷却量制御装置を制御する冷媒温度制御装置と
を具備することを特徴とする制御装置。1. A steel wire cooling device that cools a hot rolled hot steel wire by transporting it, immersing it in a liquid refrigerant stored in a cooling tank, and then pulling it up; A control device included in a steel wire direct heat treatment facility that cools the high-temperature steel wire to a predetermined target temperature, the control device comprising a heat exchanger that cools a refrigerant and returns the cooled refrigerant to the cooling tank again, and that cools the high-temperature steel wire to a predetermined target temperature. a refrigerant temperature detector arranged to be immersed in the refrigerant in the cooling tank or in contact with the refrigerant returned from the heat exchanger to the cooling tank to detect the temperature of the refrigerant at the arrangement position; and a steel wire rod. The steel wire rod is cooled to the target temperature based on a predetermined heat balance formula between the temperature of the steel wire rod and the temperature of the refrigerant by setting the wire diameter and conveyance speed of the steel wire rod and the predetermined target temperature. a calculation device that calculates the optimal temperature of the refrigerant, a cooling amount control device that adjusts the cooling amount of the heat exchanger, and a temperature detected by the refrigerant temperature detector and the temperature calculated by the calculation device. A control device comprising: a refrigerant temperature control device that controls the cooling amount control device so that the detected temperature becomes equal to the calculated temperature.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22849682A JPS59118816A (en) | 1982-12-25 | 1982-12-25 | Control device of installation for direct heat treatment of steel wire rod |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22849682A JPS59118816A (en) | 1982-12-25 | 1982-12-25 | Control device of installation for direct heat treatment of steel wire rod |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59118816A JPS59118816A (en) | 1984-07-09 |
| JPS6237693B2 true JPS6237693B2 (en) | 1987-08-13 |
Family
ID=16877365
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22849682A Granted JPS59118816A (en) | 1982-12-25 | 1982-12-25 | Control device of installation for direct heat treatment of steel wire rod |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59118816A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005024073A1 (en) * | 2003-09-02 | 2005-03-17 | Katsuhiko Yamada | Method of controllably cooling hot-rolled wire material |
-
1982
- 1982-12-25 JP JP22849682A patent/JPS59118816A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2005024073A1 (en) * | 2003-09-02 | 2005-03-17 | Katsuhiko Yamada | Method of controllably cooling hot-rolled wire material |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59118816A (en) | 1984-07-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4330112A (en) | Apparatus for cooling a steel strip in a continuous annealing line | |
| JP3688264B2 (en) | Heat treatment method and heat treatment apparatus | |
| JPS6237693B2 (en) | ||
| EP3927857B1 (en) | Apparatus and method for the drying treatment of an inductor | |
| JPH1081913A (en) | Isothermal quenching device by gas cooling | |
| JP3629325B2 (en) | Sample temperature control method | |
| JP2021063601A (en) | Method for estimating bypass ratio of heat exchange system with bypass flow path for heat medium | |
| US5837189A (en) | Quench management system | |
| JPH08259254A (en) | Optical fiber cooling method and device thereof | |
| JP2640398B2 (en) | Cooling control method of steel pipe in roller hearth heat treatment furnace | |
| JPS605823A (en) | Controlling method of direct heat treating installation for steel wire rod | |
| JP3061067U (en) | Heat exchange equipment | |
| JPS5839743A (en) | Heat treatment and water cooling apparatus thereof | |
| JPS5914182B2 (en) | thermal testing equipment | |
| JPS639569B2 (en) | ||
| JPH0617147A (en) | Continuous heat treatment method for steel strip | |
| WO2024118013A1 (en) | System and method for air cooling after casting | |
| JPS6345454B2 (en) | ||
| JPH0234727A (en) | Method and device for cooling metallic strip | |
| JPS58147523A (en) | Heat treatment device | |
| JPH0319287B2 (en) | ||
| JPH06271859A (en) | Dust suppression device for dry fire extinguishing coke | |
| JPH0135895B2 (en) | ||
| JPS634607B2 (en) | ||
| JPH01294820A (en) | Charging method in heating furnace |