JPH0441621A - Continuous heat treatment for steel strip - Google Patents

Continuous heat treatment for steel strip

Info

Publication number
JPH0441621A
JPH0441621A JP14741190A JP14741190A JPH0441621A JP H0441621 A JPH0441621 A JP H0441621A JP 14741190 A JP14741190 A JP 14741190A JP 14741190 A JP14741190 A JP 14741190A JP H0441621 A JPH0441621 A JP H0441621A
Authority
JP
Japan
Prior art keywords
furnace
direct
combustion
steel strip
exhaust gas
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
Application number
JP14741190A
Other languages
Japanese (ja)
Inventor
Junichi Hayashi
林 順一
Atsushi Suzuki
淳 鈴木
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 JP14741190A priority Critical patent/JPH0441621A/en
Publication of JPH0441621A publication Critical patent/JPH0441621A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To improve thermal efficiency in continuous heat treatment and to reduce equipment costs by burning unburnt gas in a combustion exhaust gas from a direct-fire heating furnace by blowing preheated combustion air from an auxiliary burner into a preheating furnace in a position lying to the outlet side of the preheating furnace. CONSTITUTION:A fuel (coke-oven gas) is subjected to incomplete combustion at 0.8 air ratio by means of a nonoxidizing combustion burner in a direct-fire heating furnace 3 to apply direct-fire heating to a steel strip S, and a combustion exhaust gas (a) generated in the direct-fire heating furnace 3 is allowed to flow into a preheating furnace 2. The unburnt gas in the combustion exhaust gas (a) is burned by means of combustion air blown from a burner 11 in the position lying to the outlet side of the preheating furnace 2, and the steel strip S is preheated by means of a gaseous mixture (b) of the combustion exhaust gas (a) from direct-fire heating furnace 3 and the combustion exhaust gas from the unburnt gas. By this method, the oxidation of the steel strip S can be prevented, and the high quality steel strip S can be obtained.

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は鋼帯の連続熱処理方法に関する。[Detailed description of the invention] [Industrial application field] This invention relates to a continuous heat treatment method for steel strip.

この発明は、冷延深絞り鋼板、ステンレス鋼板の連続焼
鈍ライン、電磁鋼板の熱処理ライン、連続熱処理を含む
溶融めっきラインなどに利用される。
The present invention is utilized in continuous annealing lines for cold-rolled deep-drawn steel sheets, stainless steel sheets, heat treatment lines for electrical steel sheets, hot-dip plating lines including continuous heat treatment, and the like.

[従来の技術] 鋼帯の連続熱処理設備では、ラジアントチューブによる
間接加熱炉に代えて直火加熱炉を備えたものがある。直
火加熱炉は、走行する鋼帯の表面に向かうバーナー群を
備えており、バーナーからの燃焼炎により鋼帯を直接加
熱する。また、バーナーとして無酸化燃焼バーナーか用
いられている。無酸化燃焼バーナーは、燃焼炎により鋼
帯を直接加熱するとともに、酸化スケールの生成を防止
し、さらにはすてに生成した酸化スケールを退元してス
ケール量を減少する。
[Prior Art] Some continuous heat treatment equipment for steel strips is equipped with a direct heating furnace instead of an indirect heating furnace using a radiant tube. A direct-fire heating furnace is equipped with a group of burners directed toward the surface of a running steel strip, and directly heats the steel strip with combustion flame from the burners. Also, a non-oxidizing combustion burner is used as a burner. The non-oxidizing combustion burner directly heats the steel strip with a combustion flame, prevents the formation of oxide scale, and further reduces the amount of scale by receding the oxide scale that has already been generated.

直火加熱炉て発生した燃焼排ガスは、直火加熱炉の入側
に接続された予熱炉に導く。予熱炉において燃焼排ガス
により鋼帯を予熱し、排ガスによる熱損失を低減するよ
うにしている。また、上記無酸化燃焼バーナーを備えた
直火加熱炉では、空気比0.7〜0.95で燃料を燃焼
するので、直火加熱炉からの燃焼排ガスには一酸化炭素
、水素などの多量の未燃分か含まれている。未燃分を含
む燃焼排ガスをそのまま炉外に排出すると熱損失の増大
を招くので、従来では炉外に排出するまでに未燃分を燃
焼させ、その燃焼熱を鋼帯の予熱に利用している。
The combustion exhaust gas generated in the direct-fired heating furnace is led to a preheating furnace connected to the inlet side of the direct-fired heating furnace. The steel strip is preheated by combustion exhaust gas in the preheating furnace to reduce heat loss due to the exhaust gas. In addition, in a direct-fired heating furnace equipped with the above-mentioned non-oxidizing combustion burner, fuel is combusted at an air ratio of 0.7 to 0.95, so the combustion exhaust gas from the direct-fired heating furnace contains large amounts of carbon monoxide, hydrogen, etc. Contains unburned matter. Discharging combustion exhaust gas containing unburned matter directly outside the furnace will result in increased heat loss, so conventionally the unburned matter is combusted before being discharged outside the furnace, and the combustion heat is used to preheat the steel strip. There is.

このように燃焼排カス中の未燃分を燃焼させる技術とし
て、たとえば特公昭53−39848号公報で開示され
た技術かある。
As a technique for burning the unburned content in the combustion waste in this manner, there is, for example, the technique disclosed in Japanese Patent Publication No. 53-39848.

特公昭53−39848号公報で開示された連続焼鈍炉
では、予熱炉に空気ノズルを備えアフターバーニング室
を設けている。直火炉からの燃焼排ガスに含まれる多量
の未燃分を、アフターバーニング室で過剰空気により完
全燃焼させて予熱炉に内に供給する。
In the continuous annealing furnace disclosed in Japanese Patent Publication No. 53-39848, a preheating furnace is equipped with an air nozzle and an afterburning chamber. A large amount of unburned gas contained in the combustion exhaust gas from the direct-fired furnace is completely combusted with excess air in the afterburning chamber and then supplied to the preheating furnace.

[発明が解決しようとするB題] 連続熱処理設備では、操業条件によって直火加熱炉のバ
ーナー負荷が低減されることがある。このような場合、
直火加熱炉の燃焼排ガスは温度が低下し、未燃分の着火
温度以下となることがある。未燃分が燃焼しないと、熱
損失の増大を招く。また、未燃分燃焼用の空気中の酸素
が残存することとなり、その残存酸素により鋼帯が予熱
炉中で急速に酸化される。鋼帯が酸化されると、その酸
化スケールかハースロールに付着して板疵発生の原因と
なりたり、あるいはめフき密着性の低下を招くという問
題がある。
[Problem B to be Solved by the Invention] In continuous heat treatment equipment, the burner load of the direct-fired heating furnace may be reduced depending on the operating conditions. In such a case,
The temperature of the combustion exhaust gas from a direct-fired heating furnace may drop to below the ignition temperature of unburned gas. If unburned matter is not combusted, heat loss will increase. Further, oxygen in the air for burning unburned matter remains, and the remaining oxygen rapidly oxidizes the steel strip in the preheating furnace. When the steel strip is oxidized, there is a problem in that the oxidized scale adheres to the hearth roll, causing defects in the plate, or causing a decrease in surface adhesion.

そこで、この発明は直火加熱炉からの燃焼排ガスに含ま
れる未燃分を予熱炉において確実に燃焼することができ
る鋼帯の連続熱処理方法を提供しようとするものである
SUMMARY OF THE INVENTION Therefore, the present invention aims to provide a method for continuous heat treatment of steel strips, in which unburned components contained in combustion exhaust gas from a direct-fired heating furnace can be reliably combusted in a preheating furnace.

[課題を解決するための手段] この発明の鋼帯の連続熱処理方法は、予熱炉および予熱
炉の出側に接続された直火加熱炉を備えた熱処理設備に
より鋼帯を連続熱処理するに際し、予熱炉の出側寄りの
位置で補助バーナーから燃焼用空気を炉内に吹き込んで
直火加熱炉からの燃焼排ガス中の未燃分を燃焼させる方
法において、燃焼用空気を予熱して炉内に吹き込む。
[Means for Solving the Problems] The method for continuous heat treatment of a steel strip of the present invention includes the following steps: In this method, combustion air is blown into the furnace from an auxiliary burner near the exit side of the preheating furnace to burn unburned content in the combustion exhaust gas from the direct-fired heating furnace. Infuse.

燃焼排ガス中の未燃分の燃焼により発生した熱を鋼帯の
予熱に有効に利用するために、予熱炉の出側寄りで未燃
分を燃焼する。燃焼用空気の予熱方法は特に限られるも
のではないが、予熱炉からの排ガスにより予熱する方法
は連続熱処理の熱効率の向上および設備の低額化を図る
ことがてきる。予熱温度は、300℃以上程度であるが
、400℃以上か好ましい。燃焼用空気は鋼帯面に平行
方向に吹き込むことが望ましい。燃焼用空気を鋼帯面に
平行方向に吹き込むと、燃焼用空気による鋼帯の酸化を
防ぐとともに、補助バーナーからの燃焼炎により鋼帯面
を直接加熱しない。直接加熱すると、鋼帯は必要以上に
高温に予熱される虞れがある。バーナーは燃焼排ガス中
に過剰空気比で燃焼させることにより未燃分を燃焼させ
るものであるが、バーナーの消火を防ぎ、燃焼を確実に
維持するために少量の燃料をバーナーに供給する。バー
ナーに供給する燃料として、コークス炉ガス、軽油など
が用いられる。空気量は直火加熱炉で生しる未燃ガスの
燃焼に必要な量だけ供給する。
In order to effectively utilize the heat generated by the combustion of unburned components in the combustion exhaust gas for preheating the steel strip, the unburned components are combusted near the exit side of the preheating furnace. Although the method of preheating the combustion air is not particularly limited, a method of preheating using exhaust gas from a preheating furnace can improve the thermal efficiency of continuous heat treatment and reduce the cost of equipment. The preheating temperature is approximately 300°C or higher, preferably 400°C or higher. It is desirable that the combustion air be blown in parallel to the steel strip surface. Blowing combustion air parallel to the steel strip surface prevents the steel strip from being oxidized by the combustion air, and also prevents the steel strip surface from being directly heated by the combustion flame from the auxiliary burner. Direct heating may cause the steel strip to be preheated to a higher temperature than necessary. The burner combusts unburned substances by burning the combustion exhaust gas at an excess air ratio, but in order to prevent the burner from extinguishing and to reliably maintain combustion, a small amount of fuel is supplied to the burner. Coke oven gas, light oil, etc. are used as fuel to be supplied to the burner. The amount of air supplied is the amount necessary for combustion of the unburned gas produced in the direct-fired heating furnace.

直火加熱炉は、竪型あるいは横型であってもよい。The direct-fired heating furnace may be vertical or horizontal.

[作用コ 直火加熱炉からの燃焼排ガス中に含まれる未燃分は、バ
ーナーて吹き込まわた燃焼用空気により燃焼する。直火
加熱炉からの燃焼排ガスの温度か下っても、燃焼用空気
は予熱されているので、未燃分の着火温度は維持され、
消火することはない。
[Operation: The unburned components contained in the combustion exhaust gas from the direct-fired heating furnace are combusted by the combustion air blown through the burner. Even if the temperature of the combustion exhaust gas from the direct-fired heating furnace drops, the combustion air is preheated, so the ignition temperature of the unburned components is maintained.
There is no extinguishing.

[実施例コ 第1図はこの発明の方法を実施する連続熱処理設備を併
設した溶融めっき設備の概略構成図である。
[Example 1] FIG. 1 is a schematic diagram of a hot-dip plating facility equipped with a continuous heat treatment facility for carrying out the method of the present invention.

第1図に示すように、連続熱処理膜@iは予熱炉2、直
火加熱炉3、均熱炉4、徐冷炉5および急冷炉6とから
なっている。溶融めっき設備8は連続熱処理設備1に続
いて設けられている。直火加熱炉3には、無酸化燃焼バ
ーナー群 (図示しない)か直火加熱帯3aに設けられ
ている。バーナー11は、第2図に示すように予熱炉2
の出側寄りに、鋼帯Sの両面側に配置され、炉側壁に取
り付けられている。予熱炉2の入側に空気予熱器13が
配置されている。空気予熱器13の出側は、配管15を
介して上記バーナー11に接続されている。
As shown in FIG. 1, the continuous heat-treated film @i consists of a preheating furnace 2, a direct heating furnace 3, a soaking furnace 4, a slow cooling furnace 5, and a rapid cooling furnace 6. Hot-dip plating equipment 8 is provided following continuous heat treatment equipment 1 . The direct-fired heating furnace 3 is provided with a group of non-oxidizing combustion burners (not shown) or in the direct-fired heating zone 3a. The burner 11 is connected to a preheating furnace 2 as shown in FIG.
They are placed on both sides of the steel strip S near the exit side of the steel strip S, and are attached to the furnace side wall. An air preheater 13 is arranged on the inlet side of the preheating furnace 2. The outlet side of the air preheater 13 is connected to the burner 11 via a pipe 15.

上記直火加熱炉3において、無酸化燃焼バーナーにより
空気比0.8で燃料 (コークス炉ガス)が不完全燃焼
され、鋼帯Sは直火加熱される。直火加熱炉3には予熱
炉2に向かうドラフトが加えられているので、直火加熱
炉3で発生した燃焼排ガスaは予熱炉2に流れ込む。予
熱炉2の出側寄りで、バーナー11から吹き込まれた燃
焼用空気によって燃焼排ガスa中の未燃分は燃焼される
。直火加熱炉3からの燃焼排ガスaおよび未燃分の燃焼
排ガスの混合ガスbによって、鋼帯Sは予熱される。混
合ガスbは空気予熱器13に導かれ燃焼用空気を加熱し
たのち、煙突 (図示しない)から排出される。
In the direct-fired heating furnace 3, the fuel (coke oven gas) is incompletely combusted by the non-oxidizing combustion burner at an air ratio of 0.8, and the steel strip S is directly heated. Since the direct-fired heating furnace 3 has a draft directed toward the preheating furnace 2, the combustion exhaust gas a generated in the direct-fired heating furnace 3 flows into the preheating furnace 2. Near the exit side of the preheating furnace 2, unburned components in the combustion exhaust gas a are combusted by combustion air blown from the burner 11. The steel strip S is preheated by the mixed gas b of the combustion exhaust gas a and the unburned combustion exhaust gas from the direct-fired heating furnace 3. The mixed gas b is guided to the air preheater 13, heats combustion air, and then is discharged from a chimney (not shown).

第3図は、予熱空気温度と残存酸素濃度との関係の一例
を示す線図である。第3図から明らかなように、予熱温
度が約400℃以上となると、残存酸素濃度は0%とな
る。
FIG. 3 is a diagram showing an example of the relationship between preheated air temperature and residual oxygen concentration. As is clear from FIG. 3, when the preheating temperature is about 400° C. or higher, the residual oxygen concentration becomes 0%.

[発明の効果] この発明によれば、燃焼用空気は予熱されているので、
直火加熱炉からの燃焼排ガスの温度が下っても、未燃分
の着火温度は維持され、消火することはない。この結果
、連続熱処理設備の熱効率の向上を図ることができる。
[Effect of the invention] According to this invention, since the combustion air is preheated,
Even if the temperature of the combustion exhaust gas from the direct-fired heating furnace drops, the ignition temperature of unburned gas is maintained and the fire will not be extinguished. As a result, it is possible to improve the thermal efficiency of the continuous heat treatment equipment.

また、未燃分燃焼用空気中の残存酸素による鋼帯の酸化
を防止することがてき、高品質の鋼帯を得ることができ
る。
In addition, oxidation of the steel strip due to residual oxygen in the air for combustion of unburned matter can be prevented, and a high-quality steel strip can be obtained.

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

第1図はこの発明の方法を実施する設備の一例を示すも
ので、連続熱処理設備を併設した溶融めっき設備の概略
構成図、第2図は第1図の予熱炉および直火加熱炉を示
す図面、ならびに第3図は予熱空気温度と残存酸素濃度
との関係の一例を示す線図である。 1・・・連続熱処理設備、2・・・予熱炉、3・・・直
火加熱炉、4・・・均熱炉、5・・・徐冷炉、6・・・
急冷炉、8・・・溶融めっき設備、11−・補助バーナ
ー、13・・・レキュブレーター、a・・・直火加熱炉
からの燃焼排ガス、b・・・直火加熱炉からの燃焼排ガ
スと未燃分の燃焼排ガスとの混合ガス、S −・・鋼帯
Figure 1 shows an example of equipment for carrying out the method of the present invention, and is a schematic diagram of a hot-dip plating equipment equipped with continuous heat treatment equipment, and Figure 2 shows the preheating furnace and direct-fired heating furnace of Figure 1. The drawings and FIG. 3 are diagrams showing an example of the relationship between preheated air temperature and residual oxygen concentration. 1... Continuous heat treatment equipment, 2... Preheating furnace, 3... Direct fire heating furnace, 4... Soaking furnace, 5... Slow cooling furnace, 6...
Quenching furnace, 8...Hot-dip plating equipment, 11--Auxiliary burner, 13--Recubator, a...Combustion exhaust gas from the direct-fired heating furnace, b...Combustion exhaust gas from the direct-fired heating furnace and a mixed gas of unburned combustion exhaust gas, S-... steel strip.

Claims (1)

【特許請求の範囲】[Claims] 1、予熱炉および予熱炉の出側に接続された直火加熱炉
を備えた熱処理設備により鋼帯を連続熱処理するに際し
、予熱炉の出側寄りの位置で燃焼用空気を炉内に吹き込
んで直火加熱炉からの燃焼排ガス中の未燃分を燃焼させ
る方法において、前記燃焼用空気を予熱して炉内に吹き
込むことを特徴とする鋼帯の連続熱処理方法。
1. When continuously heat treating steel strips using heat treatment equipment equipped with a preheating furnace and a direct-fired heating furnace connected to the outlet side of the preheating furnace, combustion air is blown into the furnace at a position near the outlet side of the preheating furnace. A continuous heat treatment method for steel strip, which is a method for burning unburned content in combustion exhaust gas from a direct-fired heating furnace, characterized in that the combustion air is preheated and blown into the furnace.
JP14741190A 1990-06-07 1990-06-07 Continuous heat treatment for steel strip Pending JPH0441621A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14741190A JPH0441621A (en) 1990-06-07 1990-06-07 Continuous heat treatment for steel strip

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14741190A JPH0441621A (en) 1990-06-07 1990-06-07 Continuous heat treatment for steel strip

Publications (1)

Publication Number Publication Date
JPH0441621A true JPH0441621A (en) 1992-02-12

Family

ID=15429695

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14741190A Pending JPH0441621A (en) 1990-06-07 1990-06-07 Continuous heat treatment for steel strip

Country Status (1)

Country Link
JP (1) JPH0441621A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100567910B1 (en) * 2001-11-02 2006-04-05 주식회사 포스코 Direct combustion furnace exhaust gas combustion device
JP2014048020A (en) * 2012-09-04 2014-03-17 Chugai Ro Co Ltd Continuous type heating furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100567910B1 (en) * 2001-11-02 2006-04-05 주식회사 포스코 Direct combustion furnace exhaust gas combustion device
JP2014048020A (en) * 2012-09-04 2014-03-17 Chugai Ro Co Ltd Continuous type heating furnace

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