JPS63125622A - Method for continuous cooling of steel strip in heat treatment stage - Google Patents
Method for continuous cooling of steel strip in heat treatment stageInfo
- Publication number
- JPS63125622A JPS63125622A JP27091786A JP27091786A JPS63125622A JP S63125622 A JPS63125622 A JP S63125622A JP 27091786 A JP27091786 A JP 27091786A JP 27091786 A JP27091786 A JP 27091786A JP S63125622 A JPS63125622 A JP S63125622A
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- steel strip
- region
- cooling water
- temp
- 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
Links
- 238000001816 cooling Methods 0.000 title claims abstract description 72
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 43
- 239000010959 steel Substances 0.000 title claims abstract description 43
- 238000010438 heat treatment Methods 0.000 title claims abstract description 10
- 238000000034 method Methods 0.000 title claims description 8
- 239000000498 cooling water Substances 0.000 claims abstract description 30
- 238000009835 boiling Methods 0.000 claims abstract description 22
- 239000000112 cooling gas Substances 0.000 claims abstract description 19
- 239000003595 mist Substances 0.000 claims abstract description 15
- 230000007704 transition Effects 0.000 claims abstract description 13
- 238000000137 annealing Methods 0.000 claims abstract description 6
- 238000010583 slow cooling Methods 0.000 claims abstract 3
- 239000000463 material Substances 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 230000004907 flux Effects 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 230000017525 heat dissipation Effects 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000008646 thermal stress Effects 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、鋼帯を連続焼鈍炉や連続焼準炉等で連続熱処
理する際の冷却技術に関し、特に冷却水と冷却気体との
混合ミストを加熱鋼帯に噴射して該鋼帯を連続的に冷却
する気水冷却の方法について提案ずろ。Detailed Description of the Invention (Field of Industrial Application) The present invention relates to cooling technology when continuously heat treating steel strip in a continuous annealing furnace, a continuous normalizing furnace, etc. We propose a method of air-water cooling in which the heated steel strip is injected with water to continuously cool the steel strip.
(従来の技術)
従来、鋼帯は熱処理炉(以ドは「連続焼鈍炉」の例での
べる)で熱処理する場合、加熱、均熱処理を経た高温状
態の鋼帯Sは、炉の冷却帯に第2図の矢印で示す方向か
ら通板される間に板面に噴射された気水冷却剤の作用に
より、所定の温度まで冷却される。図中の符号1は冷却
水用ヘッダ、2は気体導入用プレナムチャンバである。(Prior art) Conventionally, when a steel strip is heat treated in a heat treatment furnace (hereinafter referred to as an example of a "continuous annealing furnace"), the high temperature steel strip S that has undergone heating and soaking treatment is placed in the cooling zone of the furnace. While the plate is passed from the direction indicated by the arrow in FIG. 2, the air-water coolant sprayed onto the plate surface cools it to a predetermined temperature. The reference numeral 1 in the figure is a cooling water header, and 2 is a plenum chamber for introducing gas.
これらに供給された冷却水W、冷却気体Gはそれぞれヘ
ッダ1、プレナムチャンバ2から噴出させた段階で、前
記チャンバ2に設けたノズル2a部において混合ミスト
となり、そのまま被冷却通板材Sに向けて吹付けられる
。When the cooling water W and the cooling gas G supplied to these are ejected from the header 1 and plenum chamber 2, respectively, they become a mixed mist at the nozzle 2a provided in the chamber 2, and are directly directed toward the sheet material S to be cooled. Sprayed.
また、この第2図には従来の冷却方法により鋼帯の冷却
を行ったときの冷却曲線を併せて示す。FIG. 2 also shows a cooling curve when the steel strip is cooled by a conventional cooling method.
この冷却曲線は、高温の鋼帯Sを、冷却帯の長さ方向全
域にわたって均一の気水混合比ならびに均一の吹付は速
度で常温まで気水冷却した結果の図である。すなわち、
鋼帯Sの温度が高い高温領域Δでは急激な冷却がなされ
、その後はしばらくは緩やかな冷却がなされる。しかし
、図中αで示ず点では鋼帯Sの表面が霧化された混合ミ
スト中の冷却水Wによって濡れ始めることから次第に強
冷却となり、領域Bを過ぎると再び急激に冷却されて常
温となる。This cooling curve is a diagram showing the result of cooling a high-temperature steel strip S with air and water to room temperature at a uniform air-water mixing ratio and a uniform spraying speed over the entire length of the cooling zone. That is,
In the high temperature region Δ where the temperature of the steel strip S is high, rapid cooling is performed, and thereafter, gradual cooling is performed for a while. However, at a point not indicated by α in the figure, the surface of the steel strip S begins to be wetted by the cooling water W in the atomized mixed mist, so it gradually becomes strongly cooled, and after passing through region B, it is rapidly cooled again and returns to room temperature. Become.
(発明が解決しようとする問題点)
叙上の高温領域Aでの急激な冷却は、鋼帯Sが極めて高
温であるた於に相対的に放熱量が多いことから生ずる。(Problems to be Solved by the Invention) The rapid cooling in the high temperature region A described above is caused by the fact that the steel strip S has a relatively large amount of heat dissipation since it is at an extremely high temperature.
また、比較的低温(450〜350℃)から低温(20
0〜150℃)へ向う領域Bでの急激な冷却は、第3図
に示すような沸騰特性を有するミスト中の冷却水Wが膜
沸騰域Xから核沸騰域Yへ移行する遷移沸騰域Zに移る
際に最小熱流束(1)から最大熱流束(旧へと冷却能力
が増大することから生ずる。Also, from relatively low temperature (450 to 350℃) to low temperature (20℃).
The rapid cooling in region B toward 0 to 150° C.) occurs in the transition boiling region Z where the cooling water W in the mist having boiling characteristics as shown in FIG. 3 moves from the film boiling region X to the nucleate boiling region Y. This results from the increase in cooling capacity from the minimum heat flux (1) to the maximum heat flux (old) when moving from the minimum heat flux (1) to the maximum heat flux (old).
鋼帯Sの冷却過程で上述のような急激な冷却が生ずると
、鋼帯Sが不均一冷却されることとなり、鋼帯Sの幅方
向において材質の不均一化や熱応力−による皺、伸び等
の形状不良を生じて品質が悪化してしまうという問題点
があった。If the above-mentioned rapid cooling occurs during the cooling process of the steel strip S, the steel strip S will be cooled unevenly, resulting in uneven material quality in the width direction of the steel strip S, wrinkles and elongation due to thermal stress. There was a problem in that the quality deteriorated due to shape defects such as.
要するに本発明の目的は、温度勾配が急激に変化しない
均一冷却を実現できる冷却方法を提供するところにある
。In short, an object of the present invention is to provide a cooling method that can realize uniform cooling without sudden changes in temperature gradient.
(問題点を解決するための手段)
上掲の目的は、次に記述する構成を要旨とする方法、即
ち、焼鈍炉等の熱処理炉で加熱された鋼帯を冷却水と冷
却気体との混合ミストを噴射することにより高温域から
常温にまで連続的に冷却するに当り、前記鋼帯の温度が
高温の領域にあるとき及び混合ミスト中の冷却水の遷移
沸騰領域以下の領域にあるときについては冷却水の供給
量を緩冷却きなるように調整することを特徴とする鋼帯
熱処理時の連続冷却方法を採用することによって確実に
実現される。(Means for solving the problem) The purpose of the above is to use a method whose gist is the configuration described below, that is, to mix a steel strip heated in a heat treatment furnace such as an annealing furnace with cooling water and cooling gas. When the temperature of the steel strip is in the high temperature range and below the transition boiling range of the cooling water in the mixed mist when continuously cooling from a high temperature range to room temperature by spraying mist This can be reliably achieved by employing a continuous cooling method during steel strip heat treatment, which is characterized by adjusting the supply amount of cooling water to provide gradual cooling.
(作 用)
本発明方法の着想の基本とするところは、鋼帯冷却時の
温度勾配の大きな所、すなわち、高温領域と混合ミスト
による冷却作用が膜沸騰から核沸騰に変化するために急
激な抜熱作用を伴う遷移沸騰領域とについては、
冷却水の供給量を抑制することにより、冷却能を低下せ
しめ、全体として均一な冷却速度となるような冷却を行
うところにある。(Function) The basic concept of the method of the present invention is that the temperature gradient during cooling of the steel strip is large, that is, the cooling effect of the high temperature region and the mixed mist changes rapidly from film boiling to nucleate boiling. Regarding the transition boiling region accompanied by a heat removal effect, the cooling capacity is reduced by suppressing the amount of cooling water supplied, and cooling is performed so that the overall cooling rate is uniform.
その結果として、熱歪などによる形状不良を無くすこと
ができるのである。As a result, shape defects due to thermal distortion and the like can be eliminated.
そのために、本発明では、第1図に示すように1次冷却
帯10〜3次冷却帯30は、それぞれ独立して冷却水W
と冷却気体Gの流は制御ができるように構成された炉を
使うことが必要である。For this reason, in the present invention, as shown in FIG. 1, the primary cooling zone 10 to the tertiary cooling zone 30 each independently have
It is necessary to use a furnace constructed so that the flow of the cooling gas G and the flow of the cooling gas G can be controlled.
なお、上述の説明において、高温領域とは約1200〜
約700℃程度を、また遷移沸騰領域とは約400〜約
300℃程度の領域を指し、これは鋼帯Sの大きさ、材
質、冷却水や冷却気体の種類等によって変動するもので
ある。In addition, in the above explanation, the high temperature region is about 1200~
The transition boiling region refers to a region of about 400 to about 300° C., which varies depending on the size and material of the steel strip S, the type of cooling water or cooling gas, etc.
また、本発明方法は、鋼帯Sの急激な冷却が生じ易い高
温領域へと遷移沸騰域以下の領域Bにおいて、冷却の度
合を調整して全領域に亘って均一で緩やかな冷却が達成
できるようにすることにある。この意味において、高温
領域Δにおいて冷却水Wを全く供給せずに冷却気体Gの
みで冷却したり、或いは冷却水Wと冷却気体Gとを全く
供給せずに、放熱のみで冷却を実施しても良く、また遷
移沸騰域以下の領域Bにおいて、冷却気体と共に冷却水
を少量供給して冷却を実施するようにしても良い。In addition, the method of the present invention can achieve uniform and gradual cooling over the entire region by adjusting the degree of cooling in the region B below the transition boiling region to the high temperature region where rapid cooling of the steel strip S is likely to occur. The purpose is to do so. In this sense, in the high temperature region Δ, cooling is performed only by cooling gas G without supplying any cooling water W, or cooling is performed only by heat radiation without supplying cooling water W and cooling gas G at all. Alternatively, in region B below the transition boiling region, cooling may be performed by supplying a small amount of cooling water together with the cooling gas.
(実施例)
以下に本発明を鋼の連続焼鈍炉の冷却帯に適用した実施
例を図面を参照して説明する。(Example) An example in which the present invention is applied to a cooling zone of a continuous steel annealing furnace will be described below with reference to the drawings.
まず、本発明を実施する冷却帯を第1図に基づいて説明
する。上流の加熱、均熱工程で1000℃以上の高温に
加熱された鋼帯Sが通板される冷却帯は、その上流側か
ら1次冷却帯10.2次冷却帯20.3次冷却帯30の
3つの冷却帯により構成されている。前記1次冷却帯1
0は、この実施例の炉では全長3.5mであり、ファン
11を介して冷却気体〈空気〉 Gが供給されるプレナ
ムチャンバ12と、ポンプ13を介して冷却水Wが供給
されるヘッダ]4とを備えている。そして、この1次冷
却帯10において、プレナムチャンバ12から冷却気体
Gを30m/secで噴出させると共にヘッダ14から
冷却水Wを80cc/minで噴出させるとノズル2a
部で混合ミストとなる。この混合ミストを、ライン速度
60 m/mで通板される犀さ0.8mm、幅1,3
mの鋼帯Sに向けて吹付は約700℃まで緩冷却する。First, a cooling zone for implementing the present invention will be explained based on FIG. The cooling zones through which the steel strip S heated to a high temperature of 1000°C or higher in the upstream heating and soaking process is passed are, from the upstream side, primary cooling zone 10, secondary cooling zone 20, and tertiary cooling zone 30. It consists of three cooling zones. The primary cooling zone 1
0 has a total length of 3.5 m in the furnace of this embodiment, and includes a plenum chamber 12 to which cooling gas (air) G is supplied via a fan 11, and a header to which cooling water W is supplied via a pump 13] 4. In this primary cooling zone 10, when cooling gas G is jetted out from the plenum chamber 12 at a rate of 30 m/sec and cooling water W is jetted out from the header 14 at a rate of 80 cc/min, the nozzle 2a
becomes a mixed mist. This mixed mist was passed through a plate with a thickness of 0.8 mm and a width of 1.3 mm at a line speed of 60 m/m.
The spraying is carried out toward the steel strip S of m to slowly cool it to about 700°C.
1次冷却帯10に続く2次冷却帯20は、全長8mであ
り、ファン21を介して冷却気体(空気)6が供給され
るプレナムチャンバ22と、ポンプ23を介して冷却水
(水)Wが供給されるヘッダ24とを備えている。そし
て、この2次冷却帯20においては、プレナムチャンバ
22から冷却気体Gを50+n/secで噴出させると
ともにヘッダ24から冷却水Wを200cc/min噴
出させて形成した混合ミストを、鋼帯Sに吹付けて約4
00℃にまで冷却する。なお、この2次冷却帯20の終
端部は、鋼帯S表面での冷却水Wの沸騰が膜沸騰から核
沸騰へ移る遷移沸騰領域となっており、鋼帯Sの表面は
気水混相の状態がくずれて分離した冷却水Wによって濡
れ始める。The secondary cooling zone 20 following the primary cooling zone 10 has a total length of 8 m, and includes a plenum chamber 22 to which cooling gas (air) 6 is supplied via a fan 21 and cooling water (water) W via a pump 23. A header 24 is provided. In the secondary cooling zone 20, a mixed mist formed by jetting cooling gas G from the plenum chamber 22 at a rate of 50+n/sec and jetting cooling water W at a rate of 200 cc/min from the header 24 is blown onto the steel strip S. Approximately 4
Cool down to 00°C. The terminal end of the secondary cooling zone 20 is a transition boiling region where the boiling of the cooling water W on the surface of the steel strip S changes from film boiling to nucleate boiling, and the surface of the steel strip S is a steam-water mixed phase region. The condition deteriorates and the separated cooling water W starts to get wet.
この2次冷却帯20に続く3次冷却帯30は、全長5m
であり、ファン31を介して冷却気体(空気)Gが供給
されるプレナムチャンバ32を備えている。The tertiary cooling zone 30 following this secondary cooling zone 20 has a total length of 5 m.
It is equipped with a plenum chamber 32 to which cooling gas (air) G is supplied via a fan 31.
そして、この3次冷却帯30においては、プレナムチャ
ンバ32から冷却気体Gを5(’1m/secで噴出さ
せて鋼帯Sに吹イ」け、この鋼帯Sを約200℃まで冷
却する。In the tertiary cooling zone 30, cooling gas G is ejected from the plenum chamber 32 at a rate of 1 m/sec to the steel strip S to cool the steel strip S to about 200°C.
このような冷却を行うと、第1図に示すような冷却曲線
をもって鋼帯Sが冷却される。すなわち、鋼帯Sが高温
の領域△にあって自己の放熱により急激に冷却し易い1
次冷却帯10では、冷却水W及び冷却気体Gの供給量を
少なくして緩やかな冷却を達成し、また、高温領域Δか
ら遷移沸騰域Bまでの領域にある2次冷却帯20では所
要量の冷却水〜へ1と冷却気体Gとにより冷却を施し、
そして、遷移沸騰域B以下の領域にあって冷却水Wの冷
却能力が増大する3次冷却帯30では冷却気体Gのみに
より緩やかな冷却を達成している。この結果、鋼帯Sは
不均一冷却を生ずることなく全体的に緩やかに冷却され
るから形状不良を起すことなく良好な品質の製品が得ら
れた。When such cooling is performed, the steel strip S is cooled with a cooling curve as shown in FIG. In other words, the steel strip S is in the high temperature region △ and is easily cooled down rapidly due to its own heat dissipation.
In the secondary cooling zone 10, the supply amount of cooling water W and cooling gas G is reduced to achieve gradual cooling, and in the secondary cooling zone 20 located in the region from the high temperature region Δ to the transition boiling region B, the required amount Cooling is performed using cooling water ~1 and cooling gas G,
In the tertiary cooling zone 30, which is in the region below the transition boiling region B and where the cooling capacity of the cooling water W increases, gradual cooling is achieved only by the cooling gas G. As a result, the steel strip S was cooled slowly as a whole without uneven cooling, so that a product of good quality was obtained without causing shape defects.
(発明の効果)
以上説明したように本発明にかかる鋼帯熱処理時の連続
冷却方法によれば、鋼帯の急激な冷却が無くなるから、
祠質の不均一化や形状不良等を未然に防11−でき、良
好な品質の鋼板を製造オろことができる、。(Effects of the Invention) As explained above, according to the continuous cooling method during steel strip heat treatment according to the present invention, sudden cooling of the steel strip is eliminated.
11- It is possible to prevent non-uniformity of abrasive quality and defective shapes, etc., and to manufacture steel plates of good quality.
第1図は、本発明方法に従う冷却方法の説明図第2図は
、従来方法に従う冷却方法の説明図、第3図は、冷却水
の沸騰特性を示す温度と熱流東との関係を示すグラフで
ある。
10・・・1次冷却帯 20・・2次冷却帯30
・・・3次冷却帯 11.21,31・・・ファ
ン14、24・・冷却用ヘッダFig. 1 is an explanatory diagram of a cooling method according to the present invention; Fig. 2 is an explanatory diagram of a cooling method according to a conventional method; and Fig. 3 is a graph showing the relationship between temperature and heat flow east, which shows the boiling characteristics of cooling water. It is. 10... Primary cooling zone 20... Secondary cooling zone 30
...Third cooling zone 11.21, 31...Fans 14, 24...Cooling header
Claims (1)
却気体との混合ミストを噴射することにより高温域から
常温にまで連続的に冷却するに当り、前記鋼帯の温度が
高温の領域にあるとき及び混合ミスト中の冷却水の遷移
沸騰領域以下の領域にあるときについては冷却水の供給
量を緩冷却となるように調整することを特徴とする鋼帯
熱処理時の連続冷却方法。1. When a steel strip heated in a heat treatment furnace such as an annealing furnace is continuously cooled from a high temperature range to room temperature by injecting a mixed mist of cooling water and cooling gas, the temperature of the steel strip is high. Continuous cooling during steel strip heat treatment characterized by adjusting the supply amount of cooling water so as to provide slow cooling when the cooling water in the mixed mist is in the region below the transition boiling region and when the cooling water in the mixed mist is in the region below the transition boiling region. Method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27091786A JPS63125622A (en) | 1986-11-15 | 1986-11-15 | Method for continuous cooling of steel strip in heat treatment stage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27091786A JPS63125622A (en) | 1986-11-15 | 1986-11-15 | Method for continuous cooling of steel strip in heat treatment stage |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63125622A true JPS63125622A (en) | 1988-05-28 |
Family
ID=17492789
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27091786A Pending JPS63125622A (en) | 1986-11-15 | 1986-11-15 | Method for continuous cooling of steel strip in heat treatment stage |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63125622A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001200319A (en) * | 1999-12-17 | 2001-07-24 | Stein Heurtey | Method and apparatus for reducing wrinkle formation in strip in quenching zone of heat treatment line |
WO2010079452A1 (en) * | 2009-01-09 | 2010-07-15 | Fives Stein | Method and section for cooling a moving metal belt by spraying liquid |
JP2012082484A (en) * | 2010-10-13 | 2012-04-26 | Sumitomo Metal Ind Ltd | Method of and device for cooling metallic strip |
JP2015038234A (en) * | 2013-08-19 | 2015-02-26 | Jfeスチール株式会社 | Method and installation for production of steel strip |
-
1986
- 1986-11-15 JP JP27091786A patent/JPS63125622A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001200319A (en) * | 1999-12-17 | 2001-07-24 | Stein Heurtey | Method and apparatus for reducing wrinkle formation in strip in quenching zone of heat treatment line |
WO2010079452A1 (en) * | 2009-01-09 | 2010-07-15 | Fives Stein | Method and section for cooling a moving metal belt by spraying liquid |
FR2940978A1 (en) * | 2009-01-09 | 2010-07-16 | Fives Stein | METHOD AND COOLING SECTION OF A METAL BAND THROUGH A PROJECTION OF A LIQUID |
CN102272338A (en) * | 2009-01-09 | 2011-12-07 | 法孚斯坦因公司 | Method and section for cooling a moving metal belt by spraying liquid |
JP2012514694A (en) * | 2009-01-09 | 2012-06-28 | フイブ・スタン | Method and section for cooling a moving metal belt by spraying liquid |
US8918199B2 (en) | 2009-01-09 | 2014-12-23 | Fives Stein | Method and section for cooling a moving metal belt by spraying liquid |
JP2015083719A (en) * | 2009-01-09 | 2015-04-30 | フイブ・スタン | Method of cooling moving metal belt by spraying liquid and section |
JP2012082484A (en) * | 2010-10-13 | 2012-04-26 | Sumitomo Metal Ind Ltd | Method of and device for cooling metallic strip |
JP2015038234A (en) * | 2013-08-19 | 2015-02-26 | Jfeスチール株式会社 | Method and installation for production of steel strip |
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