JPH10121152A - Method for restraining contamination in continuous heat treatment furnace - Google Patents

Method for restraining contamination in continuous heat treatment furnace

Info

Publication number
JPH10121152A
JPH10121152A JP26840096A JP26840096A JPH10121152A JP H10121152 A JPH10121152 A JP H10121152A JP 26840096 A JP26840096 A JP 26840096A JP 26840096 A JP26840096 A JP 26840096A JP H10121152 A JPH10121152 A JP H10121152A
Authority
JP
Japan
Prior art keywords
furnace
steel strip
gas
heat treatment
continuous heat
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.)
Withdrawn
Application number
JP26840096A
Other languages
Japanese (ja)
Inventor
Norio Sakaba
則男 坂場
Masatoshi Sekiguchi
正俊 関口
Yoshiichi Nomura
芳一 野村
Kazuo Mitsutake
和夫 満武
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP26840096A priority Critical patent/JPH10121152A/en
Publication of JPH10121152A publication Critical patent/JPH10121152A/en
Withdrawn legal-status Critical Current

Links

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To restrain the flowing of atmospheric gas containing CO into a cooling furnace and to prevent the contamination caused by sticking of soot on an inner wall by blowing inert gas faced to the front and the back surfaces of the steel strip in the strip passing direction in a throat part between a heating furnace and a soaking furnace. SOLUTION: In the throat part 7 between the heating furnace 1 and the soaking furnace 2 in a continuous heat treatment furnace 6, the inert gas of nitrogen, etc., is blown so as to face to the front and the back surfaces of the steel strip 10 during passing in the steel strip passing direction. This inert gas blowing is desirable to execute by arranging the introduction pipe 8 provided with gas nozzles 9, 9a in the heating furnace 1 to heat the inert gas to >=200 deg.C with the heat exchange. Further, this blowing angle at about 30-60 deg., the flowing rate at about 10-300Nm<3> /h, the distance between the nozzle and the steel strip at about 70-120mm and the blowing pressure at about 0.1-0.5MPa, are desirable to apply. By this method, CO concn. in the atmospheric gas in the cooling furnace 5 is made to be <=300ppm and the deposition of the developed carbides (soots) is restrained to prevent the lowering of the productivity.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明方法は、連続熱処理炉
の炉内汚れ抑制方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for suppressing contamination in a continuous heat treatment furnace.

【0002】[0002]

【従来の技術】冷間圧延後の鋼帯は、周知のごとく加熱
炉、均熱炉及び冷却炉からなる連続熱処理炉へ導き、鋼
帯の熱処理(焼鈍)を施して軟質化し、鋼帯の加工性を
付与するものである。
2. Description of the Related Art As is well known, a steel strip after cold rolling is led to a continuous heat treatment furnace comprising a heating furnace, a soaking furnace and a cooling furnace, where the steel strip is heat-treated (annealed) to be softened. It imparts processability.

【0003】[0003]

【発明が解決しようとする課題】上記のごとき、鋼帯の
連続熱処理においては、冷間圧延時の圧延油が鋼帯表面
に付着しており、この付着圧延油がほとんど加熱炉の高
温下で分解したCOガスが加熱炉の雰囲気ガス中へ含有
され、鋼帯の通板により随伴して均熱炉へ流入するとと
もに、更に均熱炉で鋼帯に残留する若干の圧延油がCO
ガス化して、COガス含有雰囲気ガスとなる。特に、鋼
帯熱処理の生産性を向上するため高速通板すると、圧延
油の炉内持ち込み量が多くなり、加熱炉内等の雰囲気ガ
ス中のCOガス濃度がより高濃度になる。このようなC
Oガス含有雰囲気ガスが通板鋼帯に随伴されて均熱炉へ
流入し、更に冷却炉へ流入することになり、冷却炉で冷
却された雰囲気ガス中のCOガスが炭化物となり、冷却
炉内壁に煤となって付着して汚れが発生し、これが徐々
に堆積し剥離脱落して通板中(熱処理中)の鋼帯に付着
して品質を劣化させるこになる。このような難点を回避
するためには、定期的に操業を停止して冷却炉内に付着
堆積した煤を除去することになり、操業停止にともなう
稼働率が低下(生産性の低下)する課題がある。本発明
方法は、このような課題を有利に解決するためなされた
ものであり、連続熱処理炉の加熱炉と均熱炉間のスロー
ト部で通板中の鋼帯表裏面に不活性ガスを吹き付けるこ
とにより、COガス含有雰囲気ガスの冷却炉への流入を
抑制し、冷却炉内壁への煤(炭化物)付着による汚れを
抑制する方法を提供することを目的とするものである。
As described above, in the continuous heat treatment of the steel strip, the rolling oil during cold rolling adheres to the surface of the steel strip, and the adhered rolling oil is almost completely removed under the high temperature of the heating furnace. The decomposed CO gas is contained in the atmosphere gas of the heating furnace, and flows into the soaking furnace accompanying the steel strip passing through the strip, and further, some rolling oil remaining in the steel strip in the soaking furnace becomes CO
It is gasified to become a CO gas-containing atmosphere gas. In particular, when high-speed sheet passing is performed to improve the productivity of steel strip heat treatment, the amount of rolling oil brought into the furnace increases, and the CO gas concentration in the atmosphere gas in the heating furnace or the like becomes higher. Such a C
The atmosphere gas containing O gas flows into the soaking furnace along with the strip steel strip, and further flows into the cooling furnace. The CO gas in the atmosphere gas cooled by the cooling furnace becomes carbide, and the inner wall of the cooling furnace is cooled. The soot adheres to the steel strip and forms dirt, which gradually accumulates, peels off and falls off, and adheres to the steel strip in the passing of the sheet (during heat treatment) to deteriorate the quality. In order to avoid such difficulties, the operation is periodically stopped to remove soot that has adhered and accumulated in the cooling furnace, and the operation rate due to the operation stop is reduced (productivity is reduced). There is. The method of the present invention has been made to solve such a problem advantageously, and an inert gas is sprayed on the front and back surfaces of a steel strip during sheet passing in a throat portion between a heating furnace and a soaking furnace of a continuous heat treatment furnace. Accordingly, it is an object of the present invention to provide a method of suppressing the flow of the CO gas-containing atmosphere gas into the cooling furnace and suppressing the contamination due to the adhesion of soot (carbide) to the inner wall of the cooling furnace.

【0004】[0004]

【課題を解決するための手段】本発明方法の特徴とする
ところは、連続熱処理炉の加熱炉と均熱炉間のスロート
部で、通板中の鋼帯表裏面へ鋼帯通板方向に対向して不
活性ガスを吹き付け、加熱炉内雰囲気ガスの冷却炉への
流入を抑制することを特徴とする連続熱処理炉の炉内汚
れ抑制方法。及び連続熱処理炉の加熱炉と均熱炉間のス
ロート部に一対の隔壁を設け、この隔壁間で通板中の鋼
帯表裏面へ鋼帯通板方向に対向して不活性ガスを吹き付
け、加熱炉内雰囲気ガスの冷却炉への流入を抑制するこ
とを特徴とする連続熱処理炉の炉内汚れ抑制方法。及び
連続熱処理炉の加熱炉と均熱炉間のスロート部に一対の
隔壁を設け、この隔壁間の前段隔壁鋼帯出側近傍から隔
壁の鋼帯通過間隙へ向って、通板中の鋼帯表裏面へ鋼帯
通板方向に対向して不活性ガスを吹き付け、加熱炉内雰
囲気ガスの冷却炉への流入を抑制することを特徴とする
連続熱処理炉の炉内汚れ抑制方法である。
A feature of the method of the present invention is that a throat portion between a heating furnace and a soaking furnace of a continuous heat treatment furnace is applied to a front and a back surface of a steel strip in the passing in the direction of the passing of the steel strip. A method for suppressing in-furnace contamination in a continuous heat treatment furnace, characterized by suppressing an inflow of an atmosphere gas in a heating furnace into a cooling furnace by spraying an inert gas in opposition. And a pair of partition walls are provided at the throat portion between the heating furnace and the soaking furnace of the continuous heat treatment furnace, and an inert gas is blown between the partition walls on the front and back surfaces of the steel strip during the passing in the steel strip passing direction, A method for suppressing in-furnace contamination of a continuous heat treatment furnace, characterized by suppressing inflow of atmospheric gas in a heating furnace into a cooling furnace. A pair of partition walls is provided at the throat between the heating furnace and the soaking furnace of the continuous heat treatment furnace, and from the vicinity of the front partition steel strip exit side between the partition walls to the steel strip passage gap of the partition wall, the steel strip table in the passing plate. This is a method for suppressing in-furnace contamination of a continuous heat treatment furnace, which comprises blowing an inert gas to a back surface of the continuous heat treatment furnace in such a manner as to oppose the steel strip in a sheet passing direction, thereby suppressing an atmospheric gas in the heating furnace from flowing into a cooling furnace.

【0005】[0005]

【発明の実施の形態】上記のごとき、連続熱処理炉の加
熱炉と均熱炉間のスロート部で、通板中の鋼帯に吹き付
ける不活性ガスとしては、一般に炉内雰囲気ガスは、H
2 ガス約10%、残りN2 ガスからなっており、従って
2 ガスを用いることが好ましい。不活性ガスの吹き付
けは、一般に配設しているスロート部高さ(800〜9
00mm)であれば、鋼帯の進行方向(通板方向)に対
して30〜60°の吹き付け角度、流量10〜300N
3 /h、ガス吹き付けノズルと鋼帯距離70〜120
mm、吹き付け圧力0.1〜0.5MPaで、確実に鋼
帯が随伴する加熱炉内のCOガス含有雰囲気ガスの均熱
炉内への流入を抑制して、均熱炉に連設した冷却炉内へ
の流入を抑制し、冷却炉内での雰囲気ガス中のCOガス
冷却による炭化物の発生を抑え、冷却炉内壁への堆積を
抑制するものである。
BEST MODE FOR CARRYING OUT THE INVENTION As described above, in the throat section between the heating furnace and the soaking furnace of the continuous heat treatment furnace, the atmosphere gas in the furnace is generally H
About 2 % of the two gases are composed of the remaining N 2 gas. Therefore, it is preferable to use the N 2 gas. The inert gas is blown at the height of the throat part generally provided (800 to 9).
00 mm), a spray angle of 30 to 60 ° and a flow rate of 10 to 300 N with respect to the traveling direction (passing direction) of the steel strip.
m 3 / h, distance between gas spray nozzle and steel strip 70-120
mm, with a spray pressure of 0.1 to 0.5 MPa, the CO gas-containing atmosphere gas in the heating furnace accompanied by the steel strip is reliably prevented from flowing into the soaking furnace, and the cooling provided in the soaking furnace is connected. It suppresses the inflow into the furnace, suppresses the generation of carbides due to cooling of the CO gas in the atmosphere gas in the cooling furnace, and suppresses the deposition on the inner wall of the cooling furnace.

【0006】また、高温の不活性ガス吹き付けにより、
鋼帯の急冷による形状が悪化(ヒートバックル)するの
を防止して以降の炉内搬送ロール位置での蛇行を防ぎ、
鋼帯巾方向両端部の擦疵発生を防止するとともに、均熱
炉内での均熱処理を迅速に施すため、吹き付け不活性ガ
ス温度としては、200℃以上で均熱炉入側温度(約6
50℃)以下が好適である。このような不活性ガス温度
に調整する方法としては、例えば加熱炉内へガス導管を
配置して不活性ガスを加熱炉内経由でスロート部ガスノ
ズルへ供給し、加熱炉内熱と熱交換して高温に調整する
ことによって、コスト的に有利に温度調整することがで
きる。
Further, by blowing a high-temperature inert gas,
Prevents deterioration of the shape (heat buckle) due to rapid cooling of the steel strip and prevents meandering at the position of the transfer rolls in the furnace after that,
In order to prevent the occurrence of scratches at both ends in the width direction of the steel strip and to quickly perform soaking in the soaking furnace, the temperature of the spraying inert gas is 200 ° C. or more and the inlet temperature of the soaking furnace (about 6 ° C.).
(50 ° C.) or lower is preferred. As a method of adjusting to such an inert gas temperature, for example, a gas conduit is arranged in a heating furnace, an inert gas is supplied to a throat gas nozzle through the heating furnace, and heat exchange is performed with heat in the heating furnace. By adjusting the temperature to a high temperature, the temperature can be advantageously adjusted in terms of cost.

【0007】このように加熱炉と均熱炉のスロート部で
通板中の鋼帯に不活性ガスを吹き付け、加熱炉内のCO
ガス含有雰囲気ガスの加熱炉内への流入を抑制し、均熱
炉からの冷却炉への流入を抑制する他、例えばスロート
部に一対の隔壁を設け、この隔壁間で上記のごとく不活
性ガスを投入することにより、前段隔壁(鋼帯進行方向
入側隔壁)とガスノズル間のガス圧を上昇させ、炉内雰
囲気ガスの均熱炉への流入を抑制し、連設した冷却炉へ
の流入を抑制する。
[0007] As described above, the inert gas is blown onto the steel strip being passed through the throat portion of the heating furnace and the soaking furnace, and the CO in the heating furnace is blown.
In addition to suppressing the flow of the gas-containing atmosphere gas into the heating furnace and suppressing the flow from the soaking furnace to the cooling furnace, for example, a pair of partition walls are provided in the throat portion, and an inert gas is provided between the partition walls as described above. To increase the gas pressure between the former partition (partition wall on the entrance side in the steel strip traveling direction) and the gas nozzle, to suppress the inflow of atmospheric gas in the furnace into the soaking furnace, and to flow into the cooling furnace installed continuously. Suppress.

【0008】この他、上記のごとく一対の隔壁間の前段
隔壁(鋼帯進行方向入側隔壁の鋼帯出側(隔壁内)近傍
から隔壁の鋼帯通過間隙部の鋼帯表裏面へ向け、不活性
ガスを吹き付けることにより、鋼帯が加熱炉からスロー
ト部へ随伴する(特に鋼帯表面付近で随伴する)COガ
ス含有雰囲気ガス、即ち境界層流れを隔壁の鋼帯通過間
隙部から加熱炉へ剥離拡散して押し戻し、一層確実に均
熱炉へのCOガス含有雰囲気ガスの流入を抑制すること
ができる。
In addition, as described above, the front partition wall between the pair of partition walls (from the vicinity of the steel strip exit side (inside of the partition wall) of the partition wall on the entrance side in the traveling direction of the steel strip) is directed toward the front and back surfaces of the steel strip in the steel strip passage gap of the partition wall. By blowing the active gas, the steel strip accompanies the heating furnace from the heating furnace to the throat part (especially accompanying the vicinity of the steel strip surface), that is, the atmosphere gas containing the CO gas, that is, the boundary layer flow flows from the steel strip passage gap of the partition wall to the heating furnace. It is possible to peel and diffuse and push back, thereby more surely suppressing the flow of the CO gas-containing atmosphere gas into the soaking furnace.

【0009】このようにして、加熱炉内のCOガス含有
雰囲気ガスが均熱炉内へ流入することを抑制し、均熱炉
に連設した冷却炉へのCOガス含有雰囲気ガス流入を抑
えることにより、冷却炉内雰囲気ガス中のCOガス濃度
の上昇を抑えることができ、冷却炉内壁への炭化物付着
による汚れを抑制するものであるが、冷却炉内雰囲気ガ
ス中のCOガス濃度としては、冷却炉炉温等によって若
干異なるが、一般に使用されている連続熱処理炉の冷却
炉炉温600〜150℃の場合には、冷却炉内雰囲気ガ
ス中のCOガス濃度を300PPm以下にすることによ
って、炭化物の冷却炉内壁への付着堆積による汚れを著
しく抑制することができ、上記のごとき本発明方法によ
って、確実に冷却炉内雰囲気ガス中のCOガス濃度を3
00PPm以下にすることができる。
In this manner, the CO gas-containing atmosphere gas in the heating furnace is prevented from flowing into the soaking furnace, and the CO gas-containing atmosphere gas is prevented from flowing into the cooling furnace connected to the soaking furnace. By this, it is possible to suppress the rise of the CO gas concentration in the atmosphere gas in the cooling furnace, and to suppress the contamination due to the adhesion of the carbide to the inner wall of the cooling furnace. However, as the CO gas concentration in the atmosphere gas in the cooling furnace, Although it varies slightly depending on the cooling furnace temperature, etc., when the cooling furnace temperature of a generally used continuous heat treatment furnace is 600 to 150 ° C., by setting the CO gas concentration in the atmosphere gas in the cooling furnace to 300 PPm or less, Contamination due to the adhesion and deposition of carbides on the inner wall of the cooling furnace can be remarkably suppressed, and the method of the present invention as described above reliably reduces the CO gas concentration in the atmosphere gas in the cooling furnace to 3%.
It can be less than 00 PPm.

【0010】次に、本発明方法の一例を図面によって説
明する。図1において、加熱炉1、均熱炉2及び徐冷炉
3と急冷炉4からなる冷却炉5を連設した連続熱処理炉
6の加熱炉1と均熱炉2間のスロート部7へ不活性ガス
導管8を加熱炉1内を経由して配置し、この不活性ガス
導管8の先端にガスノズル9、9aを設け、鋼帯10進
行方向に対向せしめて鋼帯の表裏面へ指向配置すし、通
板鋼帯10に不活性ガスを吹き付け、鋼帯10が随伴す
る加熱炉1内のCOガス含有雰囲気ガスをシールして均
熱炉2内への流入を抑制して、均熱炉2に連設した冷却
炉5への流入を抑制し、冷却炉5内でのCOガス冷却に
よる発生炭化物(煤)11の冷却炉5内壁への付着を抑
制するものである。鋼帯10への吹き付け不活性ガス
は、加熱炉1の不活性ガス導管8を通過するとき、加熱
炉1内熱により加熱し高温にしてガスノズル9、9aか
ら鋼帯10へ吹き付け、鋼帯10の急冷による形状悪化
を防止して、以降の搬送ロール12位置での蛇行を防止
することによって、鋼帯10巾方向両端部の疵発生を防
止するとともに、均熱炉2での均熱処理を迅速に施す。
Next, an example of the method of the present invention will be described with reference to the drawings. In FIG. 1, an inert gas is supplied to a throat portion 7 between a heating furnace 1 and a soaking furnace 2 of a continuous heat treatment furnace 6 in which a cooling furnace 5 comprising a heating furnace 1, a soaking furnace 2 and an annealing furnace 3 and a quenching furnace 4 are connected. A conduit 8 is disposed inside the heating furnace 1, and gas nozzles 9 and 9 a are provided at the tip of the inert gas conduit 8 so as to be opposed to the traveling direction of the steel strip 10 so as to be directed to the front and back surfaces of the steel strip. An inert gas is blown onto the steel strip 10 to seal the CO-containing atmosphere gas in the heating furnace 1 accompanying the steel strip 10 to suppress the inflow into the soaking furnace 2, and to connect to the soaking furnace 2. This suppresses the inflow into the provided cooling furnace 5 and suppresses the adhesion of the generated carbide (soot) 11 due to the CO gas cooling in the cooling furnace 5 to the inner wall of the cooling furnace 5. When the inert gas sprayed on the steel strip 10 passes through the inert gas conduit 8 of the heating furnace 1, the inert gas is heated by the internal heat of the heating furnace 1 to a high temperature and sprayed from the gas nozzles 9 and 9 a onto the steel strip 10, By preventing the deterioration of the shape due to rapid cooling of the steel strip 10 and the meandering at the position of the transport roll 12 thereafter, it is possible to prevent the generation of flaws at both ends in the width direction of the steel strip 10 and to quickly perform the soaking treatment in the soaking furnace 2. Apply to

【0011】上記のごとく、加熱炉と均熱炉間のスロー
ト部での不活性ガス吹き付けによる加熱炉からのCOガ
ス含有雰囲気ガスの流入を抑制する具体例を挙げる。図
2(イ)に示すごとく、ガスノズル9、9aから鋼帯1
0進行方向に対向して不活性ガスを吹き付け、鋼帯10
が随伴する加熱炉1内のCOガス含有雰囲気ガスをシー
ルする。また、図2の(ロ)に示すごとく、スロート部
7に仕切り壁13、13aからなる隔壁14と、仕切り
壁13b、13cからなる隔壁14aの一対配設し、こ
の隔壁14、14a間の後段隔壁14a(鋼帯10進行
方向出側隔壁14a)の鋼帯10入側から鋼帯10の進
行方向に対向して、ガスノズル9、9aより不活性ガス
を投入し、隔壁14とガスノズル9、9a間のガス圧を
高めて、スロート部7内で加熱炉1内からのCOガス含
有雰囲気ガスをシールして均熱炉2への流入を抑制す
る。更に、図2の(ハ)に示すごとく、前段隔壁14の
鋼帯10出側近傍でガスノズル9、9aから鋼帯10進
行方向に対向して、隔壁14の鋼帯10通過間隙に向っ
て不活性ガスを吹き付け、鋼帯10が随伴する鋼帯10
近傍の加熱炉1内からのCOガス含有雰囲気ガス、即ち
境界層流れを剥離拡散して押し戻すことによって、シー
ルし均熱炉2への流入を抑制する。
As described above, a specific example of suppressing the inflow of the CO gas-containing atmosphere gas from the heating furnace by blowing the inert gas at the throat portion between the heating furnace and the soaking furnace will be described. As shown in FIG. 2 (a), the steel strip 1 is connected to the gas nozzles 9 and 9a.
0 Inert gas is blown against the steel strip 10
Seals the atmosphere gas containing CO gas in the heating furnace 1 accompanied by the gas. Further, as shown in FIG. 2B, a pair of a partition wall 14 composed of the partition walls 13 and 13a and a partition wall 14a composed of the partition walls 13b and 13c are disposed in the throat portion 7, and a subsequent stage between the partition walls 14 and 14a. An inert gas is injected from gas nozzles 9 and 9a from the entrance side of the steel strip 10 from the entrance side of the steel strip 10 of the partition wall 14a (the exit side partition wall 14a in the traveling direction of the steel strip 10). The gas pressure during the heating is increased to seal the CO gas-containing atmosphere gas from the inside of the heating furnace 1 in the throat section 7 to suppress the flow into the soaking furnace 2. Further, as shown in FIG. 2C, the gas nozzles 9 and 9a face the steel strip 10 in the advancing direction in the vicinity of the steel strip 10 exit side of the former partition wall 14 and are not directed toward the steel strip 10 passage gap of the partition wall 14. Activated gas is blown, and steel strip 10 accompanying steel strip 10
The CO gas-containing atmosphere gas from the vicinity of the heating furnace 1, that is, the boundary layer flow is separated and diffused and pushed back, thereby sealing and suppressing the inflow into the soaking furnace 2.

【0012】[0012]

【実施例】次に、本発明方法の実施例を比較例とともに
挙げる。
Next, examples of the method of the present invention will be described together with comparative examples.

【表1】 [Table 1]

【0013】[0013]

【表2】(表1の続き) [Table 2] (Continuation of Table 1)

【0014】[0014]

【表3】(表2の続き) [Table 3] (Continuation of Table 2)

【0015】注1:連続熱処理炉は、一般に使用されて
いる加熱炉、均熱炉及び冷却炉(徐冷炉と急冷炉)から
なり、各炉内雰囲気ガスは、H2 ガス8%、残りN2
スを使用し、板幅700〜1000mm、板厚0.15
〜0.4mmに冷間圧延でパーム系圧延油を用いて圧延
した極低炭素鋼帯を熱処理した。 注2:各炉の在炉時間は、鋼帯の熱処理在炉時間。 注3:スロート部吹き付けガスは、N2 ガスを使用。 注4:ガス吹き付け角度は、鋼帯進行方向への対向角
度。 注5:ガス吹き付け距離は、ガス吹き付けノズルと鋼帯
間距離。 注6:ガス吹き付け位置はのAは、図2(イ)のごとく
加熱炉と均熱炉間のスロート部で鋼帯表裏面にガスを吹
き付けた。Bは、図2(ロ)に示すごとき後段隔壁14
aの鋼帯入側から鋼帯表裏面へガスを吹き付けた。C
は、図2(ハ)に示すごとき前段隔壁14の鋼帯出側近
傍で隔壁14の鋼帯10通過間隙へ向って、鋼帯表裏面
へガスを吹き付けた。 注7:ガス吹き付けノズルは、鋼帯巾方向50mmピッ
チで孔径3mm。 注8:隔壁は、図2(ロ)、(ハ)に示すごとくスロー
ト部(高さ820mm)に上部仕切り壁高さ340m
m、下部仕切り壁高さ310mmからなる隔壁を間隔1
70mmで隔壁一対を配設した。 注9:煤除去間隔は、冷却炉内壁へ煤が付着堆積し、除
去した間隔(期間)。
Note 1: The continuous heat treatment furnace is composed of generally used heating furnace, soaking furnace and cooling furnace (slow cooling furnace and quenching furnace), and the atmosphere gas in each furnace is 8% H 2 gas and the remaining N 2 gas. Using gas, plate width 700 to 1000 mm, plate thickness 0.15
The ultra-low carbon steel strip rolled to a thickness of about 0.4 mm by cold rolling using palm-based rolling oil was heat-treated. Note 2: In-furnace time in each furnace is the time in heat treatment of steel strip. Note 3: throat blowing gas, using N 2 gas. Note 4: The gas spraying angle is the angle facing the steel strip traveling direction. Note 5: The gas spray distance is the distance between the gas spray nozzle and the steel strip. Note 6: In the gas spraying position A, gas was sprayed on the front and back surfaces of the steel strip at the throat portion between the heating furnace and the soaking furnace as shown in FIG. B denotes a rear partition wall 14 as shown in FIG.
Gas was blown from the inlet side of the steel strip to the front and back of the steel strip. C
As shown in FIG. 2C, gas was blown toward the front and back surfaces of the steel strip toward the gap of the steel strip 10 of the partition wall 14 near the exit side of the steel strip of the former partition wall 14 as shown in FIG. Note 7: The gas spray nozzle has a hole diameter of 3 mm at a pitch of 50 mm in the width direction of the steel strip. Note 8: As shown in FIGS. 2 (b) and (c), the partition wall is 340m high at the throat (height: 820mm).
m, partition walls consisting of a lower partition wall height of 310 mm and an interval of 1
A pair of partition walls was provided at 70 mm. Note 9: The soot removal interval is the interval (period) during which soot adhered and accumulated on the inner wall of the cooling furnace and was removed.

【0016】[0016]

【発明の効果】本発明方法によれば、連続熱処理炉の冷
却炉内壁への炭化物(煤)堆積による汚れを著しく抑制
することができ、炭化物除去による連続熱処理炉の稼働
率を向上し、生産性を高めることができる。また、炭化
物除去の間隔が長期になることから、炭化物除去のコス
ト(人手等)を軽減することができる等の優れた効果が
得られる。
According to the method of the present invention, fouling due to the accumulation of carbides (soot) on the inner wall of the cooling furnace of the continuous heat treatment furnace can be remarkably suppressed, and the operation rate of the continuous heat treatment furnace by removing the carbides can be improved to improve the production efficiency. Can be enhanced. In addition, since the intervals of carbide removal are long, excellent effects such as reduction of the cost of removing carbides (manually) can be obtained.

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

【図1】本発明方法の一例を示す側面図である。FIG. 1 is a side view showing an example of the method of the present invention.

【図2】ガスシールの一例を示す側面図である。FIG. 2 is a side view showing an example of a gas seal.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 満武 和夫 愛知県東海市東海町5−3 新日本製鐵株 式会社名古屋製鐵所内 ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Kazuo Manbu 5-3 Tokai-cho, Tokai-shi, Aichi Prefecture Nippon Steel Corporation Nagoya Works

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 連続熱処理炉の加熱炉と均熱炉間のスロ
ート部で、通板中の鋼帯表裏面へ鋼帯通板方向に対向し
て不活性ガスを吹き付け、加熱炉内雰囲気ガスの冷却炉
への流入を抑制することを特徴とする連続熱処理炉の炉
内汚れ抑制方法。
An inert gas is blown at a throat portion between a heating furnace and a soaking furnace of a continuous heat treatment furnace in a direction opposite to a direction in which a steel strip is passed through a steel strip in a sheet passing direction. A method for suppressing in-furnace contamination of a continuous heat treatment furnace, characterized by suppressing inflow of water into a cooling furnace.
【請求項2】 連続熱処理炉の加熱炉と均熱炉間のスロ
ート部に一対の隔壁を設け、この隔壁間で通板中の鋼帯
表裏面へ鋼帯通板方向に対向して不活性ガスを吹き付
け、加熱炉内雰囲気ガスの冷却炉への流入を抑制するこ
とを特徴とする連続熱処理炉の炉内汚れ抑制方法。
2. A pair of partition walls are provided in a throat portion between a heating furnace and a soaking furnace of a continuous heat treatment furnace, and between the partition walls, the front and back surfaces of a steel strip being passed are opposed to each other in a steel strip passing direction and are inactive. A method for suppressing in-furnace contamination in a continuous heat treatment furnace, which comprises blowing gas to suppress inflow of atmospheric gas in the heating furnace into a cooling furnace.
【請求項3】 連続熱処理炉の加熱炉と均熱炉間のスロ
ート部に一対の隔壁を設け、この隔壁間の前段隔壁鋼帯
出側近傍から隔壁の鋼帯通過間隙へ向って、通板中の鋼
帯表裏面へ鋼帯通板方向に対向して不活性ガスを吹き付
け、加熱炉内雰囲気ガスの冷却炉への流入を抑制するこ
とを特徴とする連続熱処理炉の炉内汚れ抑制方法。
3. A pair of partition walls is provided at a throat portion between a heating furnace and a soaking furnace of a continuous heat treatment furnace, and a portion between the partition walls near the exit side of a steel strip of a former partition wall is directed toward a steel strip passage gap of the partition walls. A method for suppressing in-furnace contamination in a continuous heat treatment furnace, characterized in that an inert gas is blown against the front and back surfaces of the steel strip in the direction of passing the steel strip, thereby suppressing the flow of atmospheric gas in the heating furnace into the cooling furnace.
【請求項4】 200℃以上の不活性ガスを吹き付ける
ことを特徴とする請求項1または請求項2または請求項
3に記載の連続熱処理炉の炉内汚れ抑制方法。
4. The method according to claim 1, wherein an inert gas having a temperature of 200 ° C. or higher is blown.
【請求項5】 冷却炉内の雰囲気ガス中のCOガス濃度
を300PPm以下にすることを特徴とする請求項1ま
たは請求項2または請求項3または請求項4に記載の連
続熱処理炉の炉内汚れ抑制方法。
5. The furnace of the continuous heat treatment furnace according to claim 1, wherein the CO gas concentration in the atmosphere gas in the cooling furnace is set to 300 PPm or less. Dirt control method.
JP26840096A 1996-10-09 1996-10-09 Method for restraining contamination in continuous heat treatment furnace Withdrawn JPH10121152A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26840096A JPH10121152A (en) 1996-10-09 1996-10-09 Method for restraining contamination in continuous heat treatment furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26840096A JPH10121152A (en) 1996-10-09 1996-10-09 Method for restraining contamination in continuous heat treatment furnace

Publications (1)

Publication Number Publication Date
JPH10121152A true JPH10121152A (en) 1998-05-12

Family

ID=17457958

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26840096A Withdrawn JPH10121152A (en) 1996-10-09 1996-10-09 Method for restraining contamination in continuous heat treatment furnace

Country Status (1)

Country Link
JP (1) JPH10121152A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002129242A (en) * 2000-10-27 2002-05-09 Chugai Ro Co Ltd Continuous heat treatment furnace for metallic strip
US8850715B2 (en) * 2006-09-07 2014-10-07 Eisenmann Ag Process and installation for drying articles

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002129242A (en) * 2000-10-27 2002-05-09 Chugai Ro Co Ltd Continuous heat treatment furnace for metallic strip
JP4713723B2 (en) * 2000-10-27 2011-06-29 中外炉工業株式会社 Operation method of continuous heat treatment furnace for metal strip
US8850715B2 (en) * 2006-09-07 2014-10-07 Eisenmann Ag Process and installation for drying articles

Similar Documents

Publication Publication Date Title
KR100258008B1 (en) Primary cooling method in continuously annealing steel strip
JPH11302811A (en) In-furnace atmosphere gas controller for continuous galvanizing equipment
US6402852B2 (en) Apparatus and method for continuous removal of oxides from metal
US4242154A (en) Preheat and cleaning system
JPH10121152A (en) Method for restraining contamination in continuous heat treatment furnace
JPH10121151A (en) Method for restraining contamination in continuous heat treatment furnace
JPH06272006A (en) Device for removing zinc fume in snout in hot-dip metal coating line
JP2006144104A (en) Apparatus and method for continuously annealing steel sheet for hot dip galvanizing
JP2820359B2 (en) Atmosphere adjustment method for continuous annealing furnace
JPH08302432A (en) Manufacture of high silicon steel strip
JP2003181522A (en) Method and device for manufacturing steel plate having excellent surface property
JPH06262243A (en) Scale generation preventing method in hot rolling steel plate
JPH07224326A (en) Water cooling method and device after heat treatment of stainless channel steel
JP3267214B2 (en) Continuous plating method and apparatus for zinc-based molten metal
JPH07157854A (en) Method for cleaning inside of snout of hot dip metal coating
JP3327211B2 (en) Method and apparatus for continuous plating of molten metal
JP2006307296A (en) Method for continuously heat-treating metallic strip and horizontal continuous heat treating furnace
JP3088903B2 (en) Prevention of meandering and slippage of metal strip in continuous heat treatment furnace
JP4352953B2 (en) Method of suppressing thermal crown of hearth roll and method of continuous annealing of steel plate
US4826544A (en) Hydrogen cleaning of hot copper rod
JPS5871365A (en) Method and device for accelerating reduction of steel strip in continuous hot dipping line or the like
JPH08109462A (en) Hot spray plating of band-shaped metal and device therefor
JP2001234252A (en) Steel strip carrying method
JPH04311530A (en) Annealing equipment for stainless steel sheet
WO2001091929A1 (en) Apparatus and method for sequential removal of oxides from steel

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20040106