JPS6358207B2 - - Google Patents
Info
- Publication number
- JPS6358207B2 JPS6358207B2 JP10003183A JP10003183A JPS6358207B2 JP S6358207 B2 JPS6358207 B2 JP S6358207B2 JP 10003183 A JP10003183 A JP 10003183A JP 10003183 A JP10003183 A JP 10003183A JP S6358207 B2 JPS6358207 B2 JP S6358207B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- cooling water
- nozzle
- cylinder
- pipe
- 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
- 238000001816 cooling Methods 0.000 claims description 74
- 239000000498 cooling water Substances 0.000 claims description 52
- 238000007654 immersion Methods 0.000 claims description 18
- 229910000831 Steel Inorganic materials 0.000 claims description 7
- 239000010959 steel Substances 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims 1
- 239000000463 material Substances 0.000 description 16
- 238000005096 rolling process Methods 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000005098 hot rolling Methods 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000011176 pooling Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B21—MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
- B21B—ROLLING OF METAL
- B21B45/00—Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
- B21B45/02—Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for lubricating, cooling, or cleaning
- B21B45/0203—Cooling
- B21B45/0209—Cooling devices, e.g. using gaseous coolants
- B21B45/0215—Cooling devices, e.g. using gaseous coolants using liquid coolants, e.g. for sections, for tubes
- B21B45/0224—Cooling devices, e.g. using gaseous coolants using liquid coolants, e.g. for sections, for tubes for wire, rods, rounds, bars
-
- 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
- C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
- C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
- C21D9/54—Furnaces for treating strips or wire
- C21D9/56—Continuous furnaces for strip or wire
- C21D9/573—Continuous furnaces for strip or wire with cooling
- C21D9/5732—Continuous furnaces for strip or wire with cooling of wires; of rods
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Description
本発明は、線材、棒鋼用の浸漬冷却管に関す
る。
周知の如く、熱間圧延により製造される線材、
棒鋼等の線条材は、仕上圧延機列後に設置された
冷却帯において、機械的性質のコントロール及び
スケール生成の抑制などのために、熱間圧延直後
の高温から所定温度にまで冷却される。このよう
な冷却帯においては、冷却媒体として通常水が用
いられている。この水冷に際しては、線条材の周
囲、長手方向及び断面方向に均一に冷却するこ
と、並びに高い冷却能を実現することなどが大切
である。冷却能を向上させることは、所定の温度
降下量を得るための冷却水流量を節減できるた
め、ポンプ動力を小さくできるなどの利点があ
る。
また熱間連続圧延においては、中間圧延機列と
仕上圧延機列との間などのスタンド間冷却帯で、
圧延材に冷却水を供給した後、再度仕上圧延機列
により圧延する制御圧延が行なわれている。この
制御圧延は、加熱温度、圧延温度、圧下率等を制
御して行なう熱間圧延法であつて、線条材におけ
る結晶粒の微細均一化、機械的性質の改善を目的
としており、圧延仕上りの状態で焼ならし処理材
と同等の組織及び機械的性質を有する線条材を製
造することができるものである。この制御圧延の
温度パターンを実現させるためにも、スタンド間
冷却帯は出来るだけ高い冷却能(熱伝達係数)を
有し、かつ制御範囲が大きなものでなければなら
ない。
上記各種の圧延工程における冷却帯において
は、従来種々の形式の冷却帯が用いられている。
例えば、冷却管内管の両端部付近に内管の周方
向に一定間隔に配置したノズル(スリツト)か
ら、該内層の軸心部を走行する圧延材に対し、圧
延材の進行方向に冷却水をスプレー状に噴射する
スプレー方式のものがある。
このスプレー方式のものでは、圧延材に高圧水
が直接あたつている所では冷却能は高いが、他の
部分では低いという欠点があり、冷却帯の長さや
冷却水流量及びポンプ動力に比して冷却効率が小
さいものである。
そこで本願出願人は、実公昭57−14965号にお
いて冷却能の優れた浸漬型式の冷却管を提供し
た。これによると、冷却管両端部に設けた環状ノ
ズルから冷却水を対向して噴出させて冷却管の開
口を施蓋する水膜を形成すると共に、冷却管の長
手方向中央部から冷却水を管内に供給し、管内部
に冷却水を充満させるものであつた。この浸漬型
式の冷却管によれば、冷却管の軸心部を走行する
高温の線条材は、管内に充満した冷却水に浸漬さ
れた状態となり、冷却水との接触時間が長くな
り、かつ均一に冷却されることになり、極めて高
い冷却能を得ることができる。この浸漬型式の冷
却管は、冷却水をいかにして管内に充満させるか
を主眼点として開発されたものであつた。
しかし、その後の研究により、浸漬型式の冷却
管の冷却能は、管内での冷却水の流れの状態によ
り大きな影響を受けることが判明した。そして流
れの状態は、管の構造、並びにノズルの指向角度
及びノズルのスリツト巾の選択に影響されること
が判明した。
そこで、本発明は、前記研究に基づき新規な冷
却管の構造を提供し、及びノズルの諸元を特定す
ることにより、冷却能の向上を図つた線材、棒鋼
用の浸漬冷却管を提供することを目的とする。従
つて、その特徴とする処は、水平軸心を有する筒
体の両端部に該軸心と同心状に設けられた環状ノ
ズルから筒体内方に向けて冷却水を噴出せしめて
筒体内部に冷却水を充満させ、該冷却水で筒体軸
心部を貫通して走行する線材又は棒鋼を浸漬冷却
する冷却管において、筒体の軸方向中途部の側面
に内部の冷却水を排出させる排水口が開設される
と共に、前記環状ノズルの内向き指向角度は筒体
軸心に対して30°以上60゜以下の範囲に設定され、
かつノズルのスリツト巾は3mm以上7mm以下の範
囲に設定されている点にある。
以下、本発明の実施例を図面に基づき詳述す
る。
第1図に示す本発明に係る浸漬型式の冷却管1
は、水平状に配置される両端開口の筒体2と、筒
体2の両端部外周面に外嵌されたジヤケツト3
と、該ジヤケツト3に接続された冷却水供給管4
と、前記筒体2の両端面に同心状に延設された入
口ガイド部5と出口ガイド部6とからなる。入口
ガイド部5の内面はテーパー面に形成されてい
る。
前記筒体2の軸方向中央部の下面には、排水口
7が開設されている。筒体2の両端部で前記ジヤ
ケツト3の内方に位置している部分と入側ガイド
部5及び出側ガイド部6とは、各々ジヤケツト3
内部と筒体2内部とを連通する環状のノズル8を
構成している。このノズル8は筒体軸心と同心状
で筒体2の内向きに開口し、筒体2の軸心に対す
る指向角度を第1図に示すように入口側をθ1、出
口側をθ2とすると、
30゜≦(θ1、θ2)≦60゜
になるよう設定されている。またノズル8のスリ
ツト巾をtとすると、
3mm<t<7mm
に設定されている。
前記本発明に係る冷却管1によれば、所定圧力
の冷却水が供給管4を介してジヤケツト3内に供
給され、該冷却水は環状ノズル8から筒体2内部
内方に向つて噴出される。このノズル8からの噴
出流は筒体2の中心部に向つて流れ、中央部で衝
突して筒体2内に充満しようとする。このとき、
冷却水の一部は排水口7より排出されるが、供給
された冷却水の残りの部分は筒体2の両端部開口
から排出され、この開口部を水流によつて満た
す。これらの結果として、給水開始後迅速に筒体
2内部は冷却水で充満されて、浸漬状態に達す
る。
しかして、上記浸漬状態において、入口ガイド
部5より線材又は棒鋼の線条材9が筒体2の軸心
部を貫通して走行することにより、線条材9は冷
却水に浸漬された状態で冷却される。
前記冷却管1において、その筒体2の中途部の
側面に排水口7を設けたので、冷却管1内におけ
る冷却水の有効な置換率(冷却水供給量Qsに対
する冷却管中央部排水口7からの冷却水の排出量
Qeの比;Qe/Qs)を高めることができた。
一般に、浸漬型式の冷却管においては、この冷
却水の有効な置換率が低ければ、それは冷却管内
に冷却水の一部が留まることを意味し、該冷却水
の溜まりにより冷却管内の平均水温が上昇し、圧
延材定常部に対する冷却能は、圧延材先端部に対
する冷却能に比べ低くなる。即ち、線条材の先端
部と定常部とでは冷却水温度に差が生じ、長手方
向に不均一な冷却となる。
これに対し、冷却管中央部から冷却水を管内に
供給し、冷却管の両端部より排水する従来の構造
の冷却管(実公昭57−14965号に記載のもの)で
あれば、冷却管の長さが短かい場合は冷却水の入
れ替わりが良好に行なわれるため問題ないが、冷
却管の長さが長くなると(本実施例では筒体2の
内径は約60mm〜120mm、長さは700mm〜1000mm)、
冷却水の一部が管内に溜まることになり、冷却水
の置換率が低下して好ましいものではなかつた。
本実施例では、筒体2の中途部の側面に排水口
7を設けることにより冷却水の有効置換率を高め
たので、このような不均一冷却の問題点が解決さ
れた。
次に、ノズル8の指向角度θ1及びθ2、及びスリ
ツト巾tを限定した理由につき説明する。
浸漬型式の冷却管1の冷却能は、管内の冷却水
の流れの状態に影響を受ける。
一般的な傾向として、冷却水供給量Qsが多く
なるほど、また、同一冷却水供給量でもノズル8
のスリツト巾tが小さくなるほど、ノズル8から
の冷却水の噴出速度が大きくなり、冷却管1の入
口側及び出口側からの空気の吸込みが多くつて、
冷却管1内での気泡発生が多くなる。また同一ス
リツト巾tであれば、ノズル8の指向角θ1,θ2が
小さい方が気泡が発生しやすい傾向にある。この
ような気泡の生成は、線条材9と冷却水との間に
断熱層を存在させることになり、冷却表面の沸騰
膜(蒸気膜)除去のために好ましくなく、冷却能
の低下をもたらすことになる。
そこで、冷却水供給量Qs、ノズル指向角θ1,θ2
及びスリツト巾tを種々変えて実験を行なつた結
果、ノズル8の指向角度θ1,θ2が30゜程度より小
さくなると気泡の発生量がかなり多くなることが
判明した。またスリツト巾tが、3mm程度よりも
小さくなると気泡の発生量が多くなることが判明
したのである。
しかして、θ1、θ2≧30゜、t≧3mmに決定した。
次に、これらの値の上限を決定する。この種の
浸漬型式冷却管1においては、常に冷却管1内に
冷却水を充満させた状態で圧延材を冷却する必要
がある。即ち、不充分な浸漬状態では、圧延材の
周方向或いは長手方向の冷却が不均一となるから
である。
また浸漬状態に達するまでの冷却水供給量
Qminが小さい方が、冷却水流量の制御範囲を大
きくとれることになつて望ましい。即ち、使用す
る冷却水の最水供給量をQmaxとすると、Qmax
−Qminの値が大きくなつて、冷却水流量の制御
範囲を大きくとれる。この制御範囲が大きいこと
は、特に制御圧延において重要である。
そこで、ノズル8の指向角度θ1,θ2及びスリツ
ト巾tを種々変えて、浸漬状態に達するまでの冷
却水供給量Qminを測定した。その結果を第2図
及び第3図に示す。
第2図は、スリツト巾tが一定(t=5mm)の
場合のノズル指向角θとQmimとの関係を示す。
Qminの値はノズル指向角θが60°超えるとかなり
大きくなる傾向にある。
第3図は、ノズル指向角θが一定(θ=45°の
場合のスリツト巾tとQminとの関係を示す。
Qminの値はスリツト巾tが7mmを超えるとかな
り大きくなる傾向にある。
従つて、θ1、θ2≦60゜、t≦7mmに設定する。
以上を要約すれば、この種の浸漬型式の冷却管
1においては、スリツト角度θ1,θ2及びスリツト
巾tは、各々30゜、3mmよりも小さくなると、冷
却管1内の気泡発生量が著しく大きくなり、冷却
能が低下する。またこれらが各々60゜、7mmより
も大きくなるとQminの値、すなわち、冷却管1
内に冷却水が充満する(浸漬状態となる)のに必
要な冷却水量が大きくなつて、冷却水流量の制御
範囲が小さくなり好ましくない。
表1に、この種の浸漬型式の冷却管1において
ノズル指向角θ1=θ2=45゜で、スリツト巾t=5
mmとt=2.0mmの場合の冷却能の比較を示す。
The present invention relates to an immersion cooling pipe for wire rods and steel bars. As is well known, wire rods manufactured by hot rolling,
A wire material such as a steel bar is cooled from a high temperature immediately after hot rolling to a predetermined temperature in a cooling zone installed after the finish rolling mill row in order to control mechanical properties and suppress scale formation. In such cooling zones, water is usually used as the cooling medium. In this water cooling, it is important to uniformly cool the wire material in its circumference, longitudinal direction, and cross-sectional direction, and to achieve high cooling performance. Improving the cooling capacity has the advantage that the flow rate of cooling water required to obtain a predetermined temperature drop can be reduced, so that the pump power can be reduced. In addition, in continuous hot rolling, in the cooling zone between stands, such as between the intermediate rolling mill row and the finishing rolling mill row,
After cooling water is supplied to the rolled material, controlled rolling is performed in which the material is rolled again by the finishing mill row. Controlled rolling is a hot rolling method in which the heating temperature, rolling temperature, rolling reduction rate, etc. are controlled, and the purpose is to make the crystal grains fine and uniform in the wire material and improve the mechanical properties. In this state, it is possible to produce a wire material having the same structure and mechanical properties as the normalized material. In order to realize this controlled rolling temperature pattern, the inter-stand cooling zone must have as high a cooling capacity (heat transfer coefficient) as possible and a wide control range. Conventionally, various types of cooling zones have been used in the above-mentioned various rolling processes. For example, cooling water is supplied from nozzles (slits) arranged at regular intervals in the circumferential direction of the inner cooling pipe in the direction of movement of the rolled material running along the axial center of the inner layer. There is a spray type that sprays out a spray. With this spray method, the cooling capacity is high in areas where the high-pressure water is directly in contact with the rolled material, but it is low in other areas. Therefore, the cooling efficiency is low. Therefore, the applicant of the present application provided an immersion type cooling pipe with excellent cooling performance in Japanese Utility Model Publication No. 14965/1983. According to this method, cooling water is jetted out in opposite directions from annular nozzles provided at both ends of the cooling pipe to form a water film that covers the opening of the cooling pipe, and cooling water is directed into the pipe from the longitudinal center of the cooling pipe. The pipe was supplied with cooling water to fill the inside of the pipe. According to this immersion type cooling pipe, the high-temperature wire material running along the axis of the cooling pipe is immersed in the cooling water filling the pipe, which increases the contact time with the cooling water, and Uniform cooling results in extremely high cooling performance. This immersion type cooling pipe was developed with the main focus on how to fill the pipe with cooling water. However, subsequent research has revealed that the cooling capacity of immersion-type cooling pipes is greatly affected by the state of the flow of cooling water within the pipes. It has been found that the flow conditions are influenced by the tube structure and the selection of the nozzle pointing angle and nozzle slit width. Therefore, the present invention provides a novel cooling pipe structure based on the above research, and specifies the specifications of the nozzle to provide an immersion cooling pipe for wire rods and steel bars with improved cooling capacity. With the goal. Therefore, the feature is that cooling water is jetted inward from the annular nozzles provided at both ends of the cylinder having a horizontal axis and concentrically with the axis. In a cooling pipe that is filled with cooling water and immerses and cools a wire rod or steel bar that runs through the axial center of the cylinder, a drainage system that discharges the internal cooling water to the side surface of the axially midway part of the cylinder. When the mouth is opened, the inward pointing angle of the annular nozzle is set in a range of 30° or more and 60° or less with respect to the axis of the cylinder body,
Moreover, the slit width of the nozzle is set within a range of 3 mm or more and 7 mm or less. Hereinafter, embodiments of the present invention will be described in detail based on the drawings. Immersion type cooling pipe 1 according to the present invention shown in FIG.
The cylinder body 2 is arranged horizontally and has both ends open, and the jacket 3 is fitted onto the outer peripheral surface of both ends of the cylinder body 2.
and a cooling water supply pipe 4 connected to the jacket 3.
The cylindrical body 2 includes an inlet guide part 5 and an outlet guide part 6 extending concentrically on both end surfaces of the cylinder body 2. The inner surface of the entrance guide portion 5 is formed into a tapered surface. A drain port 7 is provided on the lower surface of the axially central portion of the cylindrical body 2 . The portions located inside the jacket 3 at both ends of the cylindrical body 2, the entrance guide portion 5, and the exit guide portion 6 are connected to the jacket 3, respectively.
An annular nozzle 8 that communicates between the inside and the inside of the cylinder body 2 is configured. This nozzle 8 is concentric with the axis of the cylinder body and opens inward of the cylinder body 2, and the orientation angle with respect to the axis of the cylinder body 2 is θ 1 on the inlet side and θ 2 on the outlet side, as shown in FIG. Then, it is set so that 30°≦(θ 1 , θ 2 )≦60°. Further, if the slit width of the nozzle 8 is t, it is set to 3 mm<t<7 mm. According to the cooling pipe 1 according to the present invention, cooling water at a predetermined pressure is supplied into the jacket 3 through the supply pipe 4, and the cooling water is jetted inward from the annular nozzle 8 into the cylinder body 2. Ru. The jet stream from the nozzle 8 flows toward the center of the cylindrical body 2, collides at the center, and tends to fill the cylindrical body 2. At this time,
A portion of the cooling water is discharged from the drain port 7, while the remaining portion of the supplied cooling water is discharged from openings at both ends of the cylinder 2, filling these openings with water flow. As a result, the inside of the cylinder 2 is quickly filled with cooling water after the start of water supply, and reaches an immersed state. In the above-mentioned immersed state, the wire rod or steel bar 9 passes through the axial center of the cylinder 2 from the inlet guide portion 5, so that the wire rod 9 is immersed in the cooling water. cooled down. In the cooling pipe 1, the drain port 7 is provided on the side surface of the middle part of the cylindrical body 2, so that the effective replacement rate of cooling water in the cooling pipe 1 (the cooling pipe center drain port 7 for the cooling water supply amount Qs) is Cooling water discharge from
It was possible to increase the Qe ratio (Qe/Qs). In general, in immersion type cooling pipes, if the effective replacement rate of this cooling water is low, it means that some of the cooling water remains in the cooling pipes, and the average water temperature in the cooling pipes increases due to the pooling of cooling water. The cooling capacity for the stationary part of the rolled material becomes lower than the cooling capacity for the tip end of the rolled material. That is, a difference occurs in the temperature of the cooling water between the tip end portion and the stationary portion of the filament, resulting in non-uniform cooling in the longitudinal direction. On the other hand, if the cooling pipe has a conventional structure (as described in Utility Model Publication No. 14965/1983), in which cooling water is supplied from the center of the cooling pipe into the pipe and drained from both ends of the cooling pipe, If the length is short, there is no problem because the cooling water is replaced well, but if the length of the cooling pipe is long (in this example, the inner diameter of the cylinder 2 is about 60 mm to 120 mm, and the length is about 700 mm to 700 mm). 1000mm),
A portion of the cooling water would accumulate in the pipe, which would reduce the cooling water replacement rate, which was not preferable. In this embodiment, the effective replacement rate of the cooling water is increased by providing the drain port 7 on the side surface of the middle part of the cylinder 2, so that the problem of non-uniform cooling is solved. Next, the reason why the directivity angles θ 1 and θ 2 of the nozzle 8 and the slit width t are limited will be explained. The cooling capacity of the immersion type cooling pipe 1 is affected by the state of the flow of cooling water within the pipe. As a general tendency, the larger the cooling water supply amount Qs, the more the nozzle 8
As the slit width t becomes smaller, the speed of cooling water ejected from the nozzle 8 increases, and more air is sucked in from the inlet and outlet sides of the cooling pipe 1.
The number of bubbles generated within the cooling pipe 1 increases. Furthermore, if the slit width t is the same, bubbles tend to occur more easily when the directivity angles θ 1 and θ 2 of the nozzle 8 are smaller. Generation of such bubbles causes a heat insulating layer to exist between the filament material 9 and the cooling water, which is undesirable for removing a boiling film (steam film) from the cooling surface, resulting in a decrease in cooling performance. It turns out. Therefore, cooling water supply amount Qs, nozzle orientation angle θ 1 , θ 2
As a result of experiments conducted with various slit widths t, it was found that when the directivity angles θ 1 and θ 2 of the nozzle 8 were smaller than about 30°, the amount of bubbles generated increased considerably. It has also been found that when the slit width t is smaller than about 3 mm, the amount of bubbles generated increases. Therefore, it was determined that θ 1 , θ 2 ≧30°, and t≧3 mm. Next, determine the upper limits of these values. In this type of immersion type cooling pipe 1, it is necessary to cool the rolled material while the cooling pipe 1 is always filled with cooling water. That is, if the immersion state is insufficient, cooling of the rolled material in the circumferential direction or longitudinal direction becomes non-uniform. Also, the amount of cooling water supplied until reaching the immersion state.
It is desirable that Qmin be smaller because it allows for a wider control range of the cooling water flow rate. In other words, if the maximum supply amount of cooling water to be used is Qmax, then Qmax
-The larger the value of Qmin, the larger the control range of the cooling water flow rate. This wide control range is particularly important in controlled rolling. Therefore, the directivity angles θ 1 and θ 2 of the nozzle 8 and the slit width t were variously changed, and the amount Qmin of cooling water supplied until the immersion state was reached was measured. The results are shown in FIGS. 2 and 3. FIG. 2 shows the relationship between the nozzle directivity angle θ and Qmim when the slit width t is constant (t=5 mm).
The value of Qmin tends to become considerably large when the nozzle pointing angle θ exceeds 60°. FIG. 3 shows the relationship between the slit width t and Qmin when the nozzle directivity angle θ is constant (θ=45°).
The value of Qmin tends to become considerably large when the slit width t exceeds 7 mm. Therefore, it is set that θ 1 and θ 2 ≦60°, and t≦7 mm. To summarize the above, in this kind of immersion type cooling pipe 1, when the slit angles θ 1 , θ 2 and the slit width t are smaller than 30° and 3 mm, respectively, the amount of bubbles generated in the cooling pipe 1 is reduced. It becomes significantly larger and the cooling capacity decreases. Also, if these become larger than 60° and 7mm, respectively, the value of Qmin, that is, the cooling pipe 1
The amount of cooling water required to fill the interior with cooling water (become immersed) increases, which is undesirable because the control range of the cooling water flow rate becomes smaller. Table 1 shows that in this type of immersion cooling pipe 1, the nozzle orientation angle θ 1 =θ 2 =45° and the slit width t=5.
A comparison of the cooling capacity when mm and t=2.0 mm is shown.
【表】
この表から明らかな如く、スリツト巾tが2mm
のものは5mmのものより冷却能が低下している。
尚、第4図に示すものは、本発明に係る他の実
施例であり、前記第1図に示す実施例と異なる点
は、筒体2の上側に複数個の排気孔10が開設さ
れている点にある。
このように排気孔10を設けることにより、冷
却管1内に発生する気泡の排出が容易となり、冷
却能向上に寄与する。
尚、本発明は、前記各々の実施例に限定される
ものではなく、排水口7は筒体2の上側に設けら
れていてもよい。
本発明によれば、冷却管内の冷却水の有効な置
換率の向上が図られ冷却能を向上させると共に、
ノズル指向角及びスリツト巾を適切なものとした
ので、冷却管内での気泡発生を防止して冷却能を
向上させ、かつ冷却水供給量の制御範囲を大きく
することができるものであり、圧延線条材の均一
かつ所望の冷却が図られるものである。[Table] As is clear from this table, the slit width t is 2mm.
The cooling capacity of the 5mm one is lower than that of the 5mm one. The embodiment shown in FIG. 4 is another embodiment of the present invention, and the difference from the embodiment shown in FIG. It is in the point where it is. By providing the exhaust hole 10 in this manner, bubbles generated within the cooling pipe 1 can be easily discharged, contributing to an improvement in cooling performance. It should be noted that the present invention is not limited to each of the above-mentioned embodiments, and the drain port 7 may be provided above the cylindrical body 2. According to the present invention, the effective replacement rate of cooling water in the cooling pipe is improved, and the cooling capacity is improved.
Since the nozzle orientation angle and slit width are set to appropriate values, it is possible to prevent the generation of bubbles in the cooling pipe, improve the cooling capacity, and widen the control range of the cooling water supply amount. Uniform and desired cooling of the strip material is achieved.
第1図は本発明の実施例を示す冷却管の断面
図、第2図は前記冷却管においてスリツト巾t=
5mmの場合のノズル指向角θと浸漬状態(冷却管
内に水が充満する)となるまでに必要な冷却水流
量Qminとの関係を示すグラフ、第3図はノズル
指向角θ=45゜の場合のスリツト巾tと浸漬状態
になるまでに必要なQminとの関係を示すグラ
フ、第4図は本発明に係る他の実施例の断面図で
ある。
1……冷却管、2……筒体、7……排水口、8
……環状ノズル、θ……ノズル指向角度、t……
スリツト巾。
FIG. 1 is a sectional view of a cooling pipe showing an embodiment of the present invention, and FIG. 2 is a slit width t=
A graph showing the relationship between the nozzle orientation angle θ and the cooling water flow rate Qmin required to reach the immersion state (the cooling pipe is filled with water) when the nozzle orientation angle θ is 5 mm. Figure 3 is for the nozzle orientation angle θ = 45°. FIG. 4 is a graph showing the relationship between the slit width t and Qmin required to reach the immersion state, and FIG. 4 is a sectional view of another embodiment according to the present invention. 1...Cooling pipe, 2...Cylinder, 7...Drain port, 8
...Annular nozzle, θ...Nozzle pointing angle, t...
Slit width.
Claims (1)
心状に設けられた環状ノズルから筒体内方に向け
て冷却水を噴出せしめて筒体内部に冷却水を充満
させ、該冷却水で筒体軸心部を貫通して走行する
線材又は棒鋼を浸漬冷却する冷却管において、筒
体の軸方向中途部の側面に内部の冷却水を排出さ
せる排水口が開設されると共に、前記環状ノズル
の内向き指向角度は筒体軸心に対して30゜以上60°
以下の範囲に設定され、かつノズルのスリツト巾
は3mm以上7mm以下の範囲に設定されていること
を特徴とする線材、棒鋼用の浸漬冷却管。1. Cooling water is jetted inward of the cylinder from annular nozzles provided at both ends of a cylinder having a horizontal axis so as to be concentric with the axis to fill the inside of the cylinder with cooling water. In a cooling pipe for immersion cooling a wire rod or steel bar that runs through the axial center of the cylinder, a drain port for discharging the internal cooling water is provided on the side surface of the axially midway part of the cylinder, and The inward pointing angle of the nozzle is 30° or more and 60° relative to the axis of the cylinder.
An immersion cooling pipe for wire rods and steel bars, characterized in that the slit width of the nozzle is set in the following range, and the slit width of the nozzle is set in the range of 3 mm or more and 7 mm or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10003183A JPS59226121A (en) | 1983-06-02 | 1983-06-02 | Immersion cooling pipe for wire rod and steel bar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10003183A JPS59226121A (en) | 1983-06-02 | 1983-06-02 | Immersion cooling pipe for wire rod and steel bar |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59226121A JPS59226121A (en) | 1984-12-19 |
| JPS6358207B2 true JPS6358207B2 (en) | 1988-11-15 |
Family
ID=14263158
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10003183A Granted JPS59226121A (en) | 1983-06-02 | 1983-06-02 | Immersion cooling pipe for wire rod and steel bar |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59226121A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102989798A (en) * | 2012-11-28 | 2013-03-27 | 江苏永钢集团有限公司 | Laminar water-cooling device |
-
1983
- 1983-06-02 JP JP10003183A patent/JPS59226121A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59226121A (en) | 1984-12-19 |
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