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JP2776183B2 - Combustion control method for steel heating furnace - Google Patents
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JP2776183B2 - Combustion control method for steel heating furnace - Google Patents

Combustion control method for steel heating furnace

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Publication number
JP2776183B2
JP2776183B2 JP5004862A JP486293A JP2776183B2 JP 2776183 B2 JP2776183 B2 JP 2776183B2 JP 5004862 A JP5004862 A JP 5004862A JP 486293 A JP486293 A JP 486293A JP 2776183 B2 JP2776183 B2 JP 2776183B2
Authority
JP
Japan
Prior art keywords
zone
combustion
heating furnace
flue
combustion air
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 - Fee Related
Application number
JP5004862A
Other languages
Japanese (ja)
Other versions
JPH06212248A (en
Inventor
光博 山本
健一 山本
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
Sumitomo Metal Industries Ltd
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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP5004862A priority Critical patent/JP2776183B2/en
Publication of JPH06212248A publication Critical patent/JPH06212248A/en
Application granted granted Critical
Publication of JP2776183B2 publication Critical patent/JP2776183B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、鋼材加熱炉、特に鍛接
管用鋼帯加熱炉の燃焼制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for controlling the combustion of a steel heating furnace, in particular, a steel strip heating furnace for forging pipes.

【0002】[0002]

【従来の技術】一般に、鋼材は帯鋼であろうが形鋼であ
ろうが、加工前には所定温度に加熱して、いわゆる変形
抵抗を少なくすることが行われている。そのために鋼材
加熱炉が用いられる。しかしながら、通常、かかる加熱
炉におけるバーナーの燃焼は、空気比1.1 〜1.2 で燃焼
させている。そのため、燃焼ガスの雰囲気は過剰酸素を
含む酸化性雰囲気となっている。その結果、被加熱材は
酸化性雰囲気にさらされながら加熱されることになり、
スケールの発生量が多くなり、これによる歩留低下が多
かった。
2. Description of the Related Art Generally, whether a steel material is a strip steel or a shaped steel, it is heated to a predetermined temperature before processing to reduce so-called deformation resistance. For this purpose, a steel heating furnace is used. However, the combustion of the burner in such a heating furnace is usually performed at an air ratio of 1.1 to 1.2. Therefore, the atmosphere of the combustion gas is an oxidizing atmosphere containing excess oxygen. As a result, the material to be heated is heated while being exposed to the oxidizing atmosphere,
The amount of scale generated increased, and the resulting reduction in yield was large.

【0003】従来にあっても、かかる問題点を解決する
方法として、特開昭60- 215716号公報において開示され
るように、二層雰囲気による加熱炉の燃焼方法が提案さ
れている。この方法は、被加熱材を囲む領域を空気比1.
0 未満で燃焼させ、この領域の燃焼で発生した未燃ガス
分をその外側の領域で燃焼させることにより、鋼材の加
熱時に発生するスケールを抑制しようとするものであ
る。いわゆるスケールロスの低減である。
[0003] Also in the conventional, as a method to solve such a problem, JP 60 - as disclosed in 215716 and JP-combustion method of the heating furnace has been proposed by two layers atmosphere. In this method, the area surrounding the material to be heated has an air ratio of 1.
By burning at less than 0 and burning the unburned gas generated in the combustion in this region in a region outside the region, it is intended to suppress the scale generated when the steel material is heated. This is the so-called reduction of scale loss.

【0004】しかしながら、この二層雰囲気による燃焼
方法では、燃焼帯域を二層にきちんと区分けして形成す
ることが困難な場合がある。例えば、鍛接管用鋼板の加
熱炉( 以下、単に鍛接管加熱炉という) では、加熱ゾー
ンの下流にオフテークと呼ばれる煙道部が複数個設置さ
れているが、加熱炉内排ガスの流速がこの部分で大きく
なるため、被加熱材の周囲の無酸化雰囲気を乱し、この
位置でスケールが発生する。また、鍛接管加熱炉のバー
ナーは約300 本もあり、この全数を二層雰囲気形成用に
変更する必要があり、非常に大きな設備費用を必要とす
る。
[0004] However, in the combustion method using the two-layer atmosphere, it may be difficult to form the combustion zone in two layers. For example, in a steel forging pipe heating furnace (hereinafter simply referred to as a forging pipe heating furnace), a plurality of flue sections called off-takes are installed downstream of the heating zone. Since the size becomes large, the non-oxidizing atmosphere around the material to be heated is disturbed, and scale is generated at this position. In addition, there are about 300 burners in the forging tube heating furnace, and it is necessary to change all the burners to form a two-layer atmosphere, which requires very large equipment costs.

【0005】この問題点を解決する方法として、実開平
3−45949 号公報に開示する方法が提案されている。こ
の方法は、鍛接管加熱炉の燃焼ゾーンの炉高をオフテー
クへ近づくほど高くすることにより、炉内排ガスの流速
を遅くして、鋼材周囲の無酸化雰囲気の乱れを防止する
方法である。しかし、この方法は炉体を改造する必要が
あるため、前記と同様に設備費が非常に高価になるとい
う欠点がある。
As a method for solving this problem, a method disclosed in Japanese Utility Model Laid-Open No. 3-45949 has been proposed. In this method, the furnace height in the combustion zone of the forging tube heating furnace is increased toward the off-take, so that the flow rate of the exhaust gas in the furnace is reduced to prevent disturbance of the non-oxidizing atmosphere around the steel material. However, this method has a drawback in that the equipment cost is extremely high as described above because the furnace body needs to be modified.

【0006】[0006]

【発明が解決しようとする課題】ここに、本発明の目的
は、設備費をそれほどかけずに、鍛接管加熱炉などの鋼
材加熱炉の加熱時に発生するスケールロスを20〜30%抑
制できる鋼材加熱炉の加熱方法を提供することである。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a steel material capable of suppressing a scale loss generated during heating of a steel material heating furnace such as a forged pipe heating furnace by 20 to 30% without incurring much equipment cost. It is to provide a heating method of a heating furnace.

【0007】[0007]

【課題を解決するための手段】本発明者等は、かかる目
的を達成すべく、種々検討を重ね、加熱帯での空気比1.
0 未満での燃焼の有利性に着目し、それによる無酸化雰
囲気の安定的形成をはかる燃焼制御方式を見い出し、本
発明を完成した。
Means for Solving the Problems The present inventors have conducted various studies in order to achieve the object, and have found that the air ratio in the heating zone is 1.
Focusing on the advantage of combustion at less than 0, a combustion control system for stably forming a non-oxidizing atmosphere thereby has been completed, and the present invention has been completed.

【0008】よって、本発明の要旨とするところは、
熱帯と、この予熱帯の下流に配置されるとともに連設さ
れた複数の燃焼ゾーンを有する加熱帯と、複数の燃焼ゾ
ーンと予熱帯とをそれぞれ連通状態で接続する複数の煙
道部とを備える鋼材の加熱炉の燃焼制御方法であって
燃焼ゾーンでの燃焼を空気比1.0未満で行い、生じた
未燃ガスを完全燃焼するに要する量の二次燃焼空気を複
数の煙道部毎に計算し、計算した量の二次燃焼空気を複
数の煙道部それぞれに供給することを特徴とする、鋼材
加熱炉の燃焼制御方法である。
[0008] Thus, it is an aspect of the present invention, the pre
Tropical and downstream of this pre-tropical zone
Heating zone having a plurality of combustion zones,
Smoke that connects the cloud and the tropics in communication
And a combustion control method for a steel heating furnace comprising a road section ,
Combustion in the combustion zone is performed at an air ratio of less than 1.0, and the amount of secondary combustion air required to completely combust the generated unburned gas is combined.
Calculated for each of the number of flue sections, and duplicated the calculated amount of secondary combustion air.
A combustion control method for a steel material heating furnace, characterized in that the supply is supplied to each of a number of flue sections.

【0009】特に、鋼材として鍛接管用鋼板を加熱する
場合に、前記予熱帯は前記燃焼ゾーンの上方に設けら
れ、少なくとも一部垂直に延設された煙道部によって連
結され、前記二次燃焼空気は、この垂直煙道部で予熱帯
に向けて斜め上方に投入する。
[0009] In particular, when heating a steel plate for a forged pipe as a steel material, the pre-tropical zone is provided above the combustion zone and is connected at least partially by a vertically extending flue portion, and the secondary combustion air is provided. Will be injected diagonally upward into the pre-tropical zone in this vertical flue.

【0010】[0010]

【作用】次に、添付図面を参照して本発明の作用につい
てさらに具体的に説明する。図1は、本発明において使
用する鍛接管加熱炉の概略説明図であり、図2はそのA
−Aの矢視図であり、そして図3は同じく図2のB−B
の矢視図である。
Next, the operation of the present invention will be described more specifically with reference to the accompanying drawings. FIG. 1 is a schematic explanatory view of a forged pipe heating furnace used in the present invention, and FIG.
-A, and FIG. 3 is also BB of FIG.
FIG.

【0011】図中、帯鋼1は矢印の方向へ進入し、予熱
帯3へ入り炉端でUターンして予熱炉入口から一度炉外
へ出て、今度は加熱帯2へ導入され、約1200℃程度に加
熱された後、炉外へ出て製管機によりパイプ状に成形さ
れ、同時に接合端部を圧接されてパイプとなる。
In the figure, the steel strip 1 enters in the direction of the arrow, enters the pre-tropical zone 3, makes a U-turn at the furnace end, exits the furnace once from the preheating furnace inlet, and is then introduced into the heating zone 2 for about 1200 After being heated to about ° C., it goes out of the furnace and is formed into a pipe shape by a pipe-making machine, and at the same time, the joining ends are pressed into a pipe.

【0012】加熱帯2は約300 本程度のバーナ5が加熱
帯を構成する燃焼ゾーンIないしIVの両側壁に設置され
ており、通常、これにより炉温度は1300〜1350℃に設定
されている。各加熱ゾーンからの排ガスは煙道部4を経
て予熱帯3に導入されるので、帯鋼1は常温で予熱帯に
入り、約500 〜600 ℃で加熱帯に入ることになる。
In the heating zone 2, about 300 burners 5 are installed on both side walls of the combustion zones I to IV constituting the heating zone, and usually the furnace temperature is set to 1300 to 1350 ° C. . Since the exhaust gas from each heating zone is introduced into the pre-tropical zone 3 through the flue section 4, the steel strip 1 enters the pre-tropical zone at room temperature and enters the heating zone at about 500 to 600 ° C.

【0013】ここで、加熱帯でのスケールロスを抑制す
るためには、被加熱材の周囲雰囲気を無酸化状態にする
ことが有効であることが知られており、本発明にあって
も、燃料配管6と燃焼空気配管7の流量を空気比1.0 以
下になるように調整して燃焼させる。このとき、加熱帯
2内が、O2=0%、CO>0%の雰囲気となり、非酸化雰
囲気が形成され帯鋼1のスケール発生が抑制される。
Here, it is known that it is effective to make the surrounding atmosphere of the material to be heated non-oxidizing in order to suppress the scale loss in the heating zone. Combustion is performed by adjusting the flow rates of the fuel pipe 6 and the combustion air pipe 7 so that the air ratio becomes 1.0 or less. At this time, the inside of the heating zone 2 becomes an atmosphere of O 2 = 0% and CO> 0%, a non-oxidizing atmosphere is formed, and the generation of scale of the steel strip 1 is suppressed.

【0014】一方、加熱帯2で発生した未燃ガスは、こ
のまま排出すると安全上の問題があるばかりでなく燃料
原単位の悪化ともなるので、二次燃焼空気配管8から空
気を煙道部に投入し、未燃ガスを完全燃焼させる。この
ように、未燃ガスは二次燃焼空気の投入により完全に燃
焼し、排ガスの温度が上昇するがその下流のレキュペレ
ータ10により顕熱を回収されて、炉外へ放出される。
On the other hand, if the unburned gas generated in the heating zone 2 is discharged as it is, not only will there be a safety problem but also the fuel consumption rate will be deteriorated. Therefore, the air is discharged from the secondary combustion air pipe 8 to the flue section. And burn the unburned gas completely. As described above, the unburned gas is completely burned by the injection of the secondary combustion air, and the temperature of the exhaust gas rises. However, the sensible heat is recovered by the recuperator 10 downstream of the exhaust gas, and is discharged outside the furnace.

【0015】空気比1.0未満とする一次燃焼空気量お
よび未燃ガスを完全燃焼させる二次燃焼空気計算量は、
各流量計6−2、7−2、8−2からのデータに基づい
て演算器9によって演算され、所定の電気信号に変えて
各調節弁6−1、7−1、8−1を作動させる。なお、
図1では図示を省略しているが、二次燃焼空気流量調節
弁8−1および二次燃焼空気流量計8−2を備える二次
燃焼空気配管8は、全ての煙道部4に設けられている。
The amount of primary combustion air that makes the air ratio less than 1.0 and the amount of secondary combustion air that completely burns unburned gas are:
It is calculated by the calculator 9 based on the data from each of the flow meters 6-2, 7-2 and 8-2, and the control valves 6-1, 7-1 and 8-1 are operated by changing to predetermined electric signals. Let it. In addition,
Although not shown in FIG. 1, the secondary combustion air flow rate is adjusted.
Secondary equipped with valve 8-1 and secondary combustion air flow meter 8-2
The combustion air pipes 8 are provided in all the flue sections 4.

【0016】例えば、二次燃焼空気配管から投入する空
気量Qb は演算器9により次の式で計算され、流量調整
弁8-1 により流量を制御される。 Qbn ={(4.9〜5.1)×Qfn−Qan}×Cn Qb : 二次燃焼空気流量 Qf : 燃料流量 Qa : 燃焼空気流量 C : 補正係数 各記号の添字n : 各燃焼ゾーンの区分 図2は燃焼ゾーンの下流に設けた煙道部とそれに続く予
熱帯の連結の様子を示すもので、図3は少なくとも一部
垂直に延設された煙道部において二次燃焼空気を投入す
るノズル8-3 の配置を示す。
[0016] For example, the air quantity Q b to be introduced from the secondary combustion air pipe is calculated by the arithmetic unit 9 by the following equation, it is controlling the flow rate by the flow rate regulating valve 8-1. Q b n = {(4.9~5.1) × Q f n-Q a n} × Cn Q b: secondary combustion air flow rate Q f: the fuel flow rate Q a: combustion air flow C: subscript correction factor each symbol n: Fig. 2 shows the flue section provided downstream of the combustion zone and the connection of the pre-tropical zone, and Fig. 3 shows at least a part of the flue section extending vertically. The arrangement of the nozzle 8-3 for supplying combustion air is shown.

【0017】ここで、本発明者らは、このような状態で
二次燃焼空気を投入する場合における二次燃焼空気を投
入する位置や、投入する角度について流体モデル実験や
実際の加熱炉を使って試験を行い、二次燃焼空気と未燃
ガスの混合が最適となるための条件を検討した結果、次
のような知見を得た。
Here, the present inventors use a fluid model experiment or an actual heating furnace to determine the position and angle at which the secondary combustion air is injected when the secondary combustion air is injected in such a state. The following knowledge was obtained as a result of examining conditions for optimizing the mixing of the secondary combustion air and the unburned gas.

【0018】図2および図3に示すように、二次燃焼空
気Qb を投入するノズル8-3 は、煙道部4の予熱炉側垂
直部4-1 の周壁の適宜位置に上向きに設置することが望
ましく、その角度θは水平方向より上向きに30〜60°程
度が適しており、ノズルの設置数は煙道部1箇所につ
き、3〜5本に分割するのが望ましい。これは以下の理
由による。
As shown in FIGS. 2 and 3, the nozzles 8-3 to inject secondary combustion air Q b, upwardly disposed at an appropriate position of the peripheral wall of the preheating furnace side vertical portion 4-1 of the flue section 4 The angle θ is preferably about 30 to 60 ° upward from the horizontal direction, and the number of installed nozzles is preferably divided into 3 to 5 nozzles per flue portion. This is for the following reason.

【0019】まず、二次燃焼空気の投入位置としては、
加熱炉内の定期炉修時に加熱炉上蓋を開放する作業に支
障をきたさないことを考慮すれば、煙道部4の炉長方向
壁面にノズルを設置する必要がある。
First, as the position for charging the secondary combustion air,
Considering that it does not hinder the work of opening the heating furnace upper lid during regular furnace repair in the heating furnace, it is necessary to install a nozzle on the wall of the flue section 4 in the furnace length direction.

【0020】煙道部の垂直部4-1 のドライブサイド、つ
まり予熱帯側を向いた壁面からの二次燃焼空気投入とワ
ークサイド、つまり予熱帯側と反対側の壁面からの二次
燃焼空気投入との状況を流体モデル実験でみてみると、
ワークサイドから投入した場合は、投入空気は加熱帯2
より流れてくる排ガス流れとうまく混合せず、分流した
まま煙道部の上部へ流れ、煙道部のコーナー部に滞留す
ることがわかった。しかし、煙道部のドライブサイドか
ら上方斜め方向に二次燃焼空気を投入した場合には、空
気が排ガスと十分に混合することができる。これは排ガ
スの流れ方向と煙道形状の特性であると考えられる。
The secondary combustion air is injected from the drive side of the vertical section 4-1 of the flue section, ie, the wall facing the pre-tropical side, and the secondary combustion air is injected from the work side, ie, the wall opposite to the pre-tropical side. Looking at the situation with the introduction in the fluid model experiment,
When thrown in from the work side, the injected air is heated zone 2
It was found that they did not mix well with the more flowing exhaust gas, but flowed to the upper part of the flue with a split flow and stayed at the corner of the flue. However, when the secondary combustion air is injected obliquely upward from the drive side of the flue, the air can be sufficiently mixed with the exhaust gas. This is considered to be a characteristic of the flow direction of the exhaust gas and the shape of the flue.

【0021】二次燃焼空気の投入ノズル8-3 の角度は、
下向きや水平では加熱炉からくる排ガスの流れを遮断す
ることになり、加熱炉の炉内圧が上昇するので、ノズル
角度は上向きがよく、各種角度を変えて実験した結果、
上向き30〜60°の角度が二次燃焼空気と加熱炉排ガスと
の混合に最適であることがわかった。
The angle of the secondary combustion air injection nozzle 8-3 is
In the downward and horizontal directions, the flow of exhaust gas coming from the heating furnace is cut off, and the furnace pressure in the heating furnace increases.
An upward angle of 30-60 ° was found to be optimal for mixing the secondary combustion air with the furnace exhaust gas.

【0022】また、二次燃焼空気ノズルの本数について
も実験を実施したところ、細管に分割するほど混合性が
よいことがわかったが、設置工事費用も考慮すると3〜
5本程度の分割が適当と考えられる。この流体モデル実
験によって得た知見は、実際の鋼材加熱炉に適用して排
ガス組成分析や炉内圧力測定により、その妥当性を確認
した。
Experiments were also carried out on the number of secondary combustion air nozzles. As a result, it was found that the smaller the number of secondary combustion air nozzles, the better the mixing performance.
It is considered that about five divisions are appropriate. The knowledge obtained by this fluid model experiment was applied to an actual steel heating furnace, and its validity was confirmed by exhaust gas composition analysis and furnace pressure measurement.

【0023】以上述べたように加熱炉での低空気比燃焼
と煙道部での未燃ガス二次燃焼により、鍛接管加熱炉で
のスケール発生を安価な手段でもってしかも容易に抑制
することができる。次に、本発明にかかる鋼材加熱炉の
燃焼制御方法が実際にすぐれた作用を発揮することを実
施例によって説明する。
As described above, the low-air ratio combustion in the heating furnace and the unburned gas secondary combustion in the flue section make it possible to easily and easily suppress the generation of scale in the forging tube heating furnace by using inexpensive means. Can be. Next, an example will be described in which the method for controlling combustion of a steel heating furnace according to the present invention exerts an actually excellent function.

【0024】[0024]

【実施例】本例では図1ないし図3に示す鍛接管加熱炉
を使用して空気比を0.8 〜1.1 まで変化させて鍛接管用
鋼帯を加熱した時のスケールロス測定結果を示す。鋼材
の寸法および加熱条件は下記の通りである。
EXAMPLE In this example, the results of scale loss measurement when the steel strip for forging pipe was heated by using the forging pipe heating furnace shown in FIGS. 1 to 3 and changing the air ratio from 0.8 to 1.1 are shown. The dimensions of the steel and the heating conditions are as follows.

【0025】 加熱材料寸法 : 4.2t × 445W(mm) 〃 速度 : 80 m/min 加熱帯温度 : 1300〜1350℃ 二次燃焼空気投入ノズル: 角度 45度×4本( 燃焼ゾー
ン当たり) 一連の実験の結果をまとめると図4に示すグラフの通り
である。空気比を1.0未満とすると速やかにスケールロ
スの低減が見られ、空気比1.1 の場合を基準に考えて、
空気比0.8 でほぼ20%の低減が実現できた。
Heating material dimensions: 4.2t × 445W (mm) 速度 Speed: 80 m / min Heating zone temperature: 1300-1350 ° C Secondary combustion air injection nozzle: Angle 45 ° x 4 (per combustion zone) The results of are summarized in the graph shown in FIG. When the air ratio is less than 1.0, the scale loss is rapidly reduced, and based on the air ratio of 1.1,
A reduction of almost 20% was achieved with an air ratio of 0.8.

【0026】次に、加熱帯を空気比0.8 で燃焼させた時
の加熱帯内、煙道部、予熱帯内排ガス中のCO%を測定し
た結果を表1に示す。表中の番号は図5に示す測定部位
を示す。これらの結果からも分かるように、本発明によ
れば加熱帯においては非酸化雰囲気が安定して形成され
ており、煙道部から下流、特に予熱帯において初めて未
燃ガスの燃焼が行われていることが分かる。
Next, Table 1 shows the results of measuring the CO% in the exhaust gas in the heating zone, in the flue, and in the pre-tropical zone when the heating zone was burned at an air ratio of 0.8. The numbers in the table indicate the measurement sites shown in FIG. As can be seen from these results, according to the present invention, a non-oxidizing atmosphere is stably formed in the heating zone, and the combustion of unburned gas is performed for the first time downstream from the flue, particularly in the pre-tropical zone. You can see that there is.

【0027】[0027]

【表1】 [Table 1]

【0028】[0028]

【発明の効果】本発明により、安価な設備費で鍛接管加
熱炉で発生するスケールを抑制することができる。
According to the present invention, it is possible to suppress the scale generated in the forged pipe heating furnace at low equipment cost.

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

【図1】本発明において使用する鍛接管加熱炉の概略説
明図である。
FIG. 1 is a schematic explanatory view of a forging tube heating furnace used in the present invention.

【図2】加熱帯と予熱帯とを連結する煙道部の形状、構
造を示す、図1のA−A矢視図である。
FIG. 2 is a view taken in the direction of arrows AA in FIG. 1, showing the shape and structure of a flue section connecting the heating zone and the pre-tropical zone.

【図3】二次燃焼空気投入ノズルの設置態様を示す、図
2のB−B矢視図である。
FIG. 3 is a view taken in the direction of arrows BB in FIG. 2, showing an installation mode of a secondary combustion air injection nozzle.

【図4】本発明の実施例の結果を示すグラフである。FIG. 4 is a graph showing a result of an example of the present invention.

【図5】図4のデータの測定部位の説明図を示す、図2
のC−C矢視図である。
5 shows an explanatory view of a measurement site of the data of FIG. 4, FIG.
FIG.

【符号の説明】[Explanation of symbols]

1: 帯鋼、 2: 加熱帯、 3: 予熱帯、
4: 煙道部、 5: バーナ、 6: 燃料配管、
6−1: 燃料流量調節弁、 6−2: 燃料流
量計、7: 燃焼空気配管、 7−1:
燃焼空気流量調節弁、7−2: 燃料空気流量計、
8: 二次燃焼空気配管、8−1: 二次燃焼空気流
量調節弁、 8−2: 二次燃焼空気流量計、8−3:
二次燃焼空気投入ノズル、 9: 演算器、10: レキュ
ペレータ
1: strip, 2: heated zone, 3: pre-tropical,
4: flue section, 5: burner, 6: fuel pipe,
6-1: fuel flow control valve, 6-2: fuel flow meter, 7: combustion air piping, 7-1:
Combustion air flow control valve, 7-2: fuel air flow meter,
8: Secondary combustion air piping, 8-1: Secondary combustion air flow control valve, 8-2: Secondary combustion air flow meter, 8-3:
Secondary combustion air injection nozzle, 9: arithmetic unit, 10: recuperator

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) C21D 1/00 - 11/00 105──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 6 , DB name) C21D 1/00-11/00 105

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 予熱帯と、当該予熱帯の下流に配置され
るとともに連設された複数の燃焼ゾーンを有する加熱帯
と、複数の前記燃焼ゾーンと前記予熱帯とをそれぞれ連
通状態で接続する複数の煙道部とを備える鋼材の加熱炉
の燃焼制御方法であって、前記燃焼ゾーンでの燃焼を空
気比1.0未満で行い、生じた未燃ガスを完全燃焼する
に要する量の二次燃焼空気を複数の前記煙道部毎に計算
し、計算した量の前記二次燃焼空気を複数の前記煙道部
それぞれに供給することを特徴とする、鋼材加熱炉の燃
焼制御方法。
Claims: 1. A pre-tropical zone, wherein the pre-tropical zone is located downstream of the pre-tropical zone.
Zone with multiple combustion zones connected and connected
And a plurality of said combustion zones and said pre-
Steel heating furnace with a plurality of flue sections connected in a continuous manner
The combustion control method of the above, wherein the combustion in the combustion zone is performed at an air ratio of less than 1.0, the amount of secondary combustion air required to completely combust the generated unburned gas is discharged to each of the plurality of flue sections. Calculation
And transferring the calculated amount of the secondary combustion air to the plurality of flue sections.
A combustion control method for a steel material heating furnace, characterized in that it is supplied to each of them.
【請求項2】 前記鋼材は鍛接管用鋼帯であって、前記
予熱帯は前記燃焼ゾーンの上方に設けられ、少なくとも
一部垂直に延設された煙道部によって連結され、前記二
次燃焼空気は、この垂直煙道部で予熱帯に向けて斜め上
方に投入することを特徴とする請求項1記載の鋼材加熱
炉の燃焼制御方法。
2. The secondary combustion air, wherein the steel material is a steel strip for a forged pipe, wherein the pre-tropical zone is provided above the combustion zone, and is connected at least partially by a vertically extending flue portion. 2. The combustion control method for a steel heating furnace according to claim 1, wherein the fuel is injected obliquely upward toward the pre-tropical zone in the vertical flue section.
JP5004862A 1993-01-14 1993-01-14 Combustion control method for steel heating furnace Expired - Fee Related JP2776183B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5004862A JP2776183B2 (en) 1993-01-14 1993-01-14 Combustion control method for steel heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5004862A JP2776183B2 (en) 1993-01-14 1993-01-14 Combustion control method for steel heating furnace

Publications (2)

Publication Number Publication Date
JPH06212248A JPH06212248A (en) 1994-08-02
JP2776183B2 true JP2776183B2 (en) 1998-07-16

Family

ID=11595490

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5004862A Expired - Fee Related JP2776183B2 (en) 1993-01-14 1993-01-14 Combustion control method for steel heating furnace

Country Status (1)

Country Link
JP (1) JP2776183B2 (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2643199B2 (en) * 1976-09-23 1978-07-13 Siemens Ag, 1000 Berlin Und 8000 Muenchen Method for the pictorial representation of a diffraction image in a transmission scanning particle beam microscope
JPS54128440A (en) * 1978-03-30 1979-10-05 Sumitomo Metal Ind Ltd Directly firing type non-oxidation furnace
JPS5617968A (en) * 1979-07-24 1981-02-20 Matsushita Electric Works Ltd Manufacture of glass fiber reinforced cement product
JPS6345324A (en) * 1986-08-11 1988-02-26 Mitsubishi Heavy Ind Ltd Heating of metallic strip

Also Published As

Publication number Publication date
JPH06212248A (en) 1994-08-02

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