JPS61217527A - Operating method for soaking pit burnt unidirectionally at upper part - Google Patents
Operating method for soaking pit burnt unidirectionally at upper partInfo
- Publication number
- JPS61217527A JPS61217527A JP5701685A JP5701685A JPS61217527A JP S61217527 A JPS61217527 A JP S61217527A JP 5701685 A JP5701685 A JP 5701685A JP 5701685 A JP5701685 A JP 5701685A JP S61217527 A JPS61217527 A JP S61217527A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- gas
- combustion
- heating
- heated
- 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
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、連続鋳造鋳片等を圧延温度に加熱するのに
使用される上部一方向焚均熱炉の操業方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention This invention relates to a method of operating an upper one-way firing soaking furnace used for heating continuously cast slabs to rolling temperature.
従来技術とその問題点
上部一方向焚均熱炉は、炉体の側壁上部にバーナが取付
けられ、下部に燃焼排ガスを排出する排煙口が設けられ
、炉内に被加熱材を一段3〜4木ずつ4〜5段に積み重
ねて加熱するものであるが、構造上の特性により焼き上
がり後の被加熱材の温度は最上段が最高で、最下段の排
煙口側が最低となり、通常60〜120℃の温度差が生
じる。Conventional technology and its problems In the upper one-way soaking furnace, a burner is attached to the upper side wall of the furnace body, a smoke exhaust port is provided at the lower part to discharge combustion exhaust gas, and the material to be heated is placed in the furnace in one stage. It is heated by stacking 4 pieces of wood in 4 to 5 tiers, but due to its structural characteristics, the temperature of the heated materials after baking is highest on the top tier and lowest on the smoke exhaust side of the bottom tier, and is usually heated to 60°C. A temperature difference of ~120°C occurs.
このような炉内の偏熱が起こる理由は、炉内のガス流れ
が第5図に破線で示されるようKなっているためで、バ
ーナ(2)に近い位置はどガス温度が高く、離れるにし
たがって被加熱材CM)あるいは炉壁(1)に熱を奪わ
れ、排煙口(3)の近くの位置ではガス温度が最も低く
なっているからである。The reason why such uneven heating occurs in the furnace is that the gas flow in the furnace is set at K as shown by the broken line in Figure 5. This is because heat is taken away by the material to be heated (CM) or the furnace wall (1), and the gas temperature is lowest near the smoke exhaust port (3).
このような均熱炉における材料の加熱温度は、連続鋳造
鋳片(以下「CC7’ルーム」と称する)の場合、炉内
最下段の排煙口近傍のCCプルームの温度が圧延に必要
な温度になるように決定されている。従って、炉内偏熱
が大きい捏上段のCCプμmムは高い温度に加熱される
ことにカリ、熱効率の悪化を招くとともに圧延の温度条
件にも差ができることKなり、好ましくない。さらに、
燃料原単位も高くつく。In the case of continuously cast slabs (hereinafter referred to as "CC7'room"), the heating temperature of the material in such a soaking furnace is such that the temperature of the CC plume near the smoke exhaust port at the lowest stage in the furnace is the temperature required for rolling. It has been decided that it will be. Therefore, the CC pump in the upper stage of kneading, which has a large uneven heat in the furnace, is heated to a high temperature, which leads to deterioration of thermal efficiency and creates a difference in rolling temperature conditions, which is not preferable. moreover,
The fuel consumption rate is also high.
そこで、従来より炉内偏熱を減少する方法として、例え
ば温度の低い位置に補助バーナを設ける方法、あるいは
高温燃焼排ガスの一部を炉内に再循環させる方法(特願
昭59−128807 )、また炉内圧力を燃焼途中か
ら低下させる方法(特願昭59−225488 )等が
提案されているが、いずれも排ガスとして大気放散され
る熱量が多く、加熱効率が悪化するという問題があり、
燃料使用量を大幅に節約できなかった。Therefore, conventional methods for reducing the uneven heat in the furnace include, for example, installing an auxiliary burner at a low temperature position, or recirculating a part of the high-temperature combustion exhaust gas into the furnace (Japanese Patent Application No. 128807/1982). In addition, methods have been proposed in which the pressure inside the furnace is lowered mid-combustion (Japanese Patent Application No. 59-225488), but all of these methods have the problem that a large amount of heat is dissipated into the atmosphere as exhaust gas, resulting in poor heating efficiency.
It was not possible to significantly reduce fuel consumption.
発 明 の 目 的
この発明は、従来の前記問題を解決するためになされた
もので、炉内偏熱をより小さくし、燃料使用量全大幅に
節減できる上部一方向焚均熱炉の操業方法を提案するこ
とを目的とするものである。Purpose of the Invention This invention was made to solve the above-mentioned conventional problems, and provides a method for operating an upper one-way soaking furnace that can further reduce uneven heat in the furnace and significantly reduce the total amount of fuel used. The purpose is to propose the following.
発明の構成
この発明に係る上部一方向焚均熱炉の操業方法は、バー
ナおよび排煙口が設けられている炉体側壁にファンを介
して炉内雰囲気ガス循環ダクトを設け、予め設定した燃
焼パターンで加熱完了後、ただちに排煙口を閉鎖し、前
記ファンにて炉内雰囲気ガスを燃焼ガスの流れと逆方向
に強制循環させることを特徴とするものである。Structure of the Invention The operating method of the upper one-way firing soaking furnace according to the present invention is to provide a furnace atmosphere gas circulation duct via a fan on the side wall of the furnace body where the burner and the smoke exhaust port are provided, and to control the preset combustion. Immediately after completion of heating in the pattern, the smoke exhaust port is closed, and the furnace atmosphere gas is forcibly circulated in the opposite direction to the flow of combustion gas using the fan.
すなわち、この発明方法は非燃焼中に排ガス出口を完全
密閉して、炉内雰囲気ガスを高温部側から低温部側へ強
制的に循環させることによって、炉内温度の均一化をは
かる方法である。That is, the method of this invention aims to equalize the temperature inside the furnace by completely sealing the exhaust gas outlet during non-combustion and forcibly circulating the atmospheric gas in the furnace from the high temperature side to the low temperature side. .
以下、この発明方法を図面全参照しつつ説明する。The method of this invention will be explained below with reference to all the drawings.
第1図はこの発明方法を実施するための装置構成例を示
す概略図、第2図は第1図■−■線上の縦断正面図であ
る。FIG. 1 is a schematic diagram showing an example of the configuration of an apparatus for carrying out the method of the present invention, and FIG. 2 is a longitudinal sectional front view taken along line 1--2 in FIG.
第1図および第2図において、(5)は排煙口(3)e
閉鎖するためのダンパーで、シリンダー(5−1)によ
り開閉される仕組みとなっている。(6) (7)はそ
れぞれ炉内雰囲気ガスの吸込みダクトおよび吐出ダクト
、(8)は炉内雰囲気ガスの循環ファン、(9−1)(
9−2)は炉内温度計、QOは燃焼用バーナ(2)、ダ
ンパー開閉用シリンダー(5−1)、循環ファン(8)
および炉内温度計(9−1)(9−2)に接続され九コ
ンピュータ、αηは煙道である。In Figures 1 and 2, (5) is the smoke exhaust port (3) e
It is a damper for closing, and is opened and closed by a cylinder (5-1). (6) (7) are the suction duct and discharge duct for the furnace atmosphere gas, (8) is the circulation fan for the furnace atmosphere gas, (9-1) (
9-2) is the furnace temperature gauge, QO is the combustion burner (2), damper opening/closing cylinder (5-1), circulation fan (8)
and nine computers connected to the furnace thermometers (9-1) and (9-2), αη is the flue.
上記装置による均熱炉操業方法を説明すると、まずコン
ピュータα0に予め設定されたと一ドパターンに基づい
てバーナ燃料流量、燃焼用空気量が決定され(所定空燃
比に基づ騒て)燃焼が開始され、被加熱材CM)が所定
時間加熱される。バーナ燃焼中、排煙口(3)は全開と
なっておシ、燃焼排ガスは煙道Iより排出される。To explain the method of operating a soaking furnace using the above device, first, the burner fuel flow rate and combustion air amount are determined based on a uniform pattern preset in the computer α0 (based on a predetermined air-fuel ratio), and combustion begins. The heated material CM) is heated for a predetermined period of time. During burner combustion, the smoke exhaust port (3) is fully opened and the combustion exhaust gas is discharged from the flue I.
被加熱材(M)の加熱が完了すると、燃焼を停止し、排
煙口(3)t−ダンパー(5)で閉鎖する。排煙口(3
)を全閉すると、ただちに循環ファン(8)t−駆動し
て炉内雰囲気ガスを第1図矢印で示すように燃焼ガスの
流れと逆方向に強制循環させる。この時、炉体側壁(1
)の上部に設は九吸込みダクト(6)より高温の炉内雰
囲気ガスが吸込まれ、炉体側壁下部に設けた吐出ダクト
(7)より炉内に導かれるので、温度の低い排煙口(3
)近傍の雰囲気温度は上昇し始める。When heating of the material to be heated (M) is completed, combustion is stopped and the smoke exhaust port (3) is closed by the T-damper (5). Smoke exhaust port (3
) is fully closed, the circulation fan (8) is immediately driven to forcefully circulate the atmospheric gas in the furnace in the direction opposite to the flow of combustion gas, as shown by the arrow in FIG. At this time, the side wall of the furnace body (1
) is installed in the upper part of the furnace.The high-temperature furnace atmosphere gas is sucked in through the suction duct (6) and guided into the furnace through the discharge duct (7) installed at the lower part of the side wall of the furnace body. 3
) The nearby ambient temperature begins to rise.
従って、この炉内雰囲気ガスの強制循環を続けると、必
然的に炉内の上部(高温)と底部(低温)の温度差がな
くなってくる。そして、炉内温度計(9−2)で測定さ
れる炉内最下段の排煙口近傍の雰囲気温度Vと炉内温度
計(9−1)で測定される炉内最上段の雰囲気温度Xが
V≧Xの関係になった時点で循環ファン(8)を停止し
、被加熱材料(M)を抽出する。Therefore, if this forced circulation of the furnace atmosphere gas continues, the temperature difference between the top (high temperature) and bottom (low temperature) inside the furnace will inevitably disappear. Then, the atmospheric temperature V near the smoke exhaust port at the lowest stage of the furnace measured by the furnace thermometer (9-2) and the atmospheric temperature X at the top stage of the furnace measured by the furnace thermometer (9-1). When V≧X is established, the circulation fan (8) is stopped and the material to be heated (M) is extracted.
なお、循環中の雰囲気ガス中にN、ガスを吹込み、無酸
化雰囲気にして2次スケールの抑制を行なう方法を合せ
て実施することもできる。Note that it is also possible to carry out a method in which secondary scale is suppressed by blowing N gas into the circulating atmospheric gas to create a non-oxidizing atmosphere.
実 施 例
@ 4.4 m +長さ7.5m、高さ4.86mの炉
内寸法を有し、かつ内部混合式低NOxバーナを2基取
付は九均熱炉内に、被加熱材料として表面温度620℃
(装入直前)のCCプ〃−ム16木9重量160トンを
装入し、1220℃の設定温度で10時間加熱後燃焼を
停止し、その直後排煙口をダンパーで全閉し、しかる後
循環ファンを駆動させて吸込みダクトよシ炉内雰囲気ガ
スを吸込み、吐出ダクトより炉内に導入して、炉内雰囲
気ガスの循環全1.5時間実施し念結果を第3図に示す
。また、本実施例における循環時間と炉内最下段の材料
温度の関係(循環流量5500 Nrrl/H)を第4
図に示す。Example @ 4.4 m + 7.5 m in length, 4.86 m in height, and two internal mixing low NOx burners are installed. As surface temperature 620℃
Charge 160 tons of CC plume (immediately before charging) with 9 pieces of 16 wood, and stop combustion after heating at a set temperature of 1220℃ for 10 hours. Immediately after that, completely close the smoke exhaust port with a damper and The post-circulation fan was driven to suck in the furnace atmosphere gas through the suction duct and introduce it into the furnace through the discharge duct, and the furnace atmosphere gas was circulated for a total of 1.5 hours. The experimental results are shown in FIG. In addition, the relationship between the circulation time and the material temperature at the lowest stage in the furnace in this example (circulation flow rate 5500 Nrrl/H) was
As shown in the figure.
第3図より明らかなように、加熱終了時における偏熱8
0℃を40℃前後に約40℃も縮めることができた。特
に、循環流量550ONm’/Hで1.5時間循環した
場合が最大効果となり、燃料節約量は12 X 10”
kcaI2/Tであった。これは、第4図より明らか
なように、炉内雰囲気ガスを循環させることにより炉内
最下段の材料温度を上昇させられたことによる。As is clear from Figure 3, the uneven heat 8 at the end of heating
We were able to reduce the temperature from 0°C to around 40°C by about 40°C. In particular, the maximum effect is achieved when circulating for 1.5 hours at a circulation flow rate of 550 ONm'/H, with a fuel savings of 12 x 10"
It was kcaI2/T. As is clear from FIG. 4, this is because the temperature of the material at the lowest stage in the furnace was raised by circulating the atmosphere gas in the furnace.
発明の効果
上記の実施例からも明らかなごとく、この発明方法によ
れば、加熱完了後に炉内雰囲気ガスを燃焼ガスの流れと
逆方向に強制循環させるだけで炉内最低温度を上昇させ
ることができるので、その最低温度が上昇した分設定温
度を低くすることが可能となり、燃料使用量を大幅に節
約できる。また、この偏熱を少なくするための炉内雰囲
気ガスの循環は、非燃焼中に排煙口を閉鎖して行なうた
め加熱効率が低下することもない。Effects of the Invention As is clear from the above embodiments, according to the method of the present invention, the minimum temperature in the furnace can be increased simply by forcing the atmosphere gas in the furnace to circulate in the opposite direction to the flow of combustion gas after heating is completed. Therefore, it is possible to lower the set temperature by the amount that the minimum temperature has increased, and the amount of fuel used can be significantly reduced. Further, since the circulation of the furnace atmosphere gas to reduce this uneven heat is carried out by closing the smoke exhaust port during non-combustion, the heating efficiency does not decrease.
第1図はこの発明方法を5!施するための装置構成例を
示す概略図、第2図は第1図ll−Tl線上の概略正面
図、第3図はこの発明の実施例における循環流量と偏熱
および燃料節約量の関係を示す図、第4図は同上実施例
における循環時間と材料温度の関係を示す図、第5図は
上部一方向焚均熱炉のガス流の状態を示す概略図である
。
1・・・側壁、2・・・バーナ、3・・・排煙口、5・
・・ダンパー、6・・・吸込みダクト、7・・・吐出ダ
クト、8・・・循環ファン、9−1.9−2・・・温度
計、10・・・コンピュータ、11・・・煙道、M・・
・被加熱材。
出願人 住友金属工業株式会社
第1図
第2図
第3図
循環流Q (Nd/H)
循環時間(Hr)Figure 1 shows the method of this invention in 5! FIG. 2 is a schematic front view taken along the line ll-Tl in FIG. FIG. 4 is a diagram showing the relationship between circulation time and material temperature in the same example as above, and FIG. 5 is a schematic diagram showing the state of gas flow in the upper one-way firing soaking furnace. 1... Side wall, 2... Burner, 3... Smoke exhaust port, 5...
Damper, 6 Suction duct, 7 Discharge duct, 8 Circulation fan, 9-1.9-2 Thermometer, 10 Computer, 11 Flue ,M...
・Heated material. Applicant: Sumitomo Metal Industries, Ltd. Figure 1 Figure 2 Figure 3 Circulating flow Q (Nd/H) Circulating time (Hr)
Claims (1)
上部一方向焚均熱炉の操業方法において、炉体側壁にフ
ァンを介して炉内雰囲気ガス循環ダクトを設け、予め設
定した燃焼パターンで加熱完了直後排煙口を閉鎖し、前
記ファンにて炉内雰囲気ガスを燃焼ガスの流れと逆方向
に強制循環させることを特徴とする上部一方向焚均熱炉
の操業方法。In the operating method of an upper one-way firing soaking furnace, which has a burner in the upper part of the furnace side wall and a smoke exhaust port in the lower part, a furnace atmosphere gas circulation duct is installed on the furnace side wall through a fan, and a preset A method for operating an upper one-way soaking furnace, characterized in that the smoke exhaust port is closed immediately after heating is completed in a combustion pattern, and the atmosphere gas in the furnace is forcedly circulated in the opposite direction to the flow of combustion gas using the fan.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5701685A JPS61217527A (en) | 1985-03-20 | 1985-03-20 | Operating method for soaking pit burnt unidirectionally at upper part |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5701685A JPS61217527A (en) | 1985-03-20 | 1985-03-20 | Operating method for soaking pit burnt unidirectionally at upper part |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61217527A true JPS61217527A (en) | 1986-09-27 |
Family
ID=13043636
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5701685A Pending JPS61217527A (en) | 1985-03-20 | 1985-03-20 | Operating method for soaking pit burnt unidirectionally at upper part |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61217527A (en) |
-
1985
- 1985-03-20 JP JP5701685A patent/JPS61217527A/en active Pending
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