JP2000282137A - Soaking method and soaking furnace - Google Patents

Soaking method and soaking furnace

Info

Publication number
JP2000282137A
JP2000282137A JP11086599A JP8659999A JP2000282137A JP 2000282137 A JP2000282137 A JP 2000282137A JP 11086599 A JP11086599 A JP 11086599A JP 8659999 A JP8659999 A JP 8659999A JP 2000282137 A JP2000282137 A JP 2000282137A
Authority
JP
Japan
Prior art keywords
burner
furnace body
furnace
main burner
combustion
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
JP11086599A
Other languages
Japanese (ja)
Inventor
Fujio Komaki
藤男 小牧
Ikuo Sugie
郁夫 杉江
Yoshinori Matsuo
吉則 松尾
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co 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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP11086599A priority Critical patent/JP2000282137A/en
Publication of JP2000282137A publication Critical patent/JP2000282137A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To improve the heating quality of a steel ingot and also the treating capacity by selecting an optimum heating operation according to the kind of the steel ingot. SOLUTION: In the front part at an one side in the longitudinal direction of a furnace body 32, one set of main burner 34 is disposed at almost center position in the width direction. In the rear part at the other side in the longitudinal direction of the furnace body 32, two sets of auxiliary burners 36 are disposed so as to be mutually apart in the width direction. Each combustion capacity in both auxiliary burners 36, is set to <=1/2 of the combustion capacity in the main burner 34, and two sets of the auxiliary burners 36 and one set of the main burner 34 are constituted so as to have the relation of a pair in a regenerator burner system. In the case of charging plural steel ingots 14 in the vertically laying state in the furnace, only the main burner 34 is used to heat the steel ingot group, and in the case of charging plural steel ingots 14 in the horizontally laying state in the furnace, the main burner 34 and the auxiliary burners 36 are alternately used to heat the steel ingot group.

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】この発明は、リジェネレイテ
ィブバーナ燃焼システム(以下「リジェネバーナシステ
ム」と称す)を選択して鋼塊を加熱し得る均熱方法および
均熱炉に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a soaking method and a soaking furnace capable of selecting a regenerative burner combustion system (hereinafter referred to as "regenerative burner system") to heat a steel ingot.

【0002】[0002]

【従来の技術】溶鋼を鋳型に鋳入して製造したスラブ、
ビレット等の鋼塊を、鋳型から取出した後に圧延するに
際し、その前工程として、該鋼塊の内部と外部との温度
を均一に近付けるための均熱作業がある。この均熱作業
に用いられる均熱炉は、図5に示す如く、炉体10にお
ける長手方向一方の前部に1基のバーナ12が配置され
ており、炉体10内部の幅方向に対向する左右の内部側
壁面に複数の鋼塊14を長手方向に所定間隔離間して立
て掛けた状態(縦置き状態)で装入し、前記バーナ12を
燃焼することで各鋼塊14を加熱するよう構成されてい
る。
2. Description of the Related Art A slab manufactured by casting molten steel into a mold,
When a steel ingot such as a billet is taken out of a mold and then rolled, as a pre-process, there is a heat equalizing operation for making the temperature between the inside and the outside of the steel ingot close to uniform. As shown in FIG. 5, the heat equalizing furnace used for this heat equalizing operation has a single burner 12 disposed at one front portion in the longitudinal direction of the furnace body 10 and faces the width direction inside the furnace body 10. A configuration in which a plurality of steel ingots 14 are loaded on the left and right inner side wall surfaces in a state where the plurality of steel ingots 14 are placed upright at a predetermined interval in the longitudinal direction (vertical installation state), and the burners 12 are burned to heat each steel ingot 14 Have been.

【0003】前記均熱炉では、バーナ12の火炎が鋼塊
14に直接当たらないように、図5(a),(b)に示すよ
うに、左右の鋼塊群列の間(幅方向の略中央)で、かつ鋼
塊14の上端より上方にバーナ12が配置される。しか
し、このように炉体10の前部に1基のバーナ12を配
置した構成では、炉内の前後および上下での温度差が大
きく、炭素鋼等のように圧延加工性の良好な種類の鋼塊
14を加熱する場合は問題ないが、JIS SUS 30
3やJIS SKD 11等のような圧延加工性の難しい
種類の鋼塊14を加熱する場合は、不均一な加熱により
後工程での圧延に支障を来す問題を生ずる。従って、圧
延加工性の難しい鋼塊14を加熱する際には、図5に示
すように12本の鋼塊14が炉体10の内部に装入され
ている場合では、バーナ12から離間する後部側の6本
の鋼塊14を取出した後に、残りの6本の鋼塊14を後
部に移動して再び加熱する工程を繰返す極めて煩雑な作
業を行なっていた。
In the above soaking furnace, as shown in FIGS. 5 (a) and 5 (b), the flame of the burner 12 does not directly hit the steel ingot 14, as shown in FIGS. The burner 12 is disposed substantially at the center and above the upper end of the steel ingot 14. However, in the configuration in which one burner 12 is disposed in the front part of the furnace body 10 as described above, the temperature difference between the front and rear and up and down in the furnace is large, and a kind of a type having good rolling workability such as carbon steel is used. There is no problem when heating the steel ingot 14, but JIS SUS 30
In the case of heating a steel ingot 14 that is difficult to roll, such as No. 3 or JIS SKD 11, there is a problem that uneven heating may hinder the rolling in the subsequent process. Therefore, when heating the steel ingot 14 that is difficult to be rolled, when the twelve steel ingots 14 are charged inside the furnace body 10 as shown in FIG. After taking out the six ingots 14 on the side, an extremely complicated operation of repeating the process of moving the remaining six ingots 14 to the rear and heating again was performed.

【0004】ここで、前述した従来の均熱炉では、バー
ナによる燃焼効率が低く、エネルギーロスが大きかっ
た。そこで、リジェネバーナシステムによる均熱方法が
提案されている。これは、蓄熱体を有する2本のバーナ
を一対とし、燃料、空気、排ガスの切替弁、熱焼用空気
ブロワ、排気ファンおよびそれらを制御する制御装置等
で構成される。このシステムでは、一方のバーナが燃焼
しているときは、他方のバーナから燃焼排ガスを排気し
て蓄熱体を加熱する。次にこの一対のバーナの燃焼と排
気とを切替えることにより、蓄熱体に蓄熱された熱量を
燃焼用空気で回収し、燃焼室内に還元する。そして、こ
の切替えを数10秒〜数分の短周期で繰返すことで、燃
焼用空気を高い温度まで予熱し、高効率で廃熱回収をし
ながら燃焼させるシステムである。
Here, in the above-mentioned conventional soaking furnace, the combustion efficiency by the burner is low and the energy loss is large. Therefore, a soaking method using a regenerative burner system has been proposed. This is a pair of two burners each having a heat storage body, and is configured by a switching valve for fuel, air, and exhaust gas, an air blower for thermal firing, an exhaust fan, and a control device for controlling them. In this system, when one burner is burning, the combustion exhaust gas is exhausted from the other burner to heat the regenerator. Next, by switching between combustion and exhaust of the pair of burners, the amount of heat stored in the heat storage body is recovered by the combustion air and returned to the combustion chamber. By repeating this switching in a short cycle of several tens of seconds to several minutes, the combustion air is preheated to a high temperature, and the combustion is performed while recovering waste heat with high efficiency.

【0005】前記リジェネバーナシステムを用いる均熱
炉のバーナの配置については、例えば図6に示す構成が
考えられる。すなわち、炉体10の前部に第1バーナ1
6と第3バーナ20とを幅方向に離間して配置すると共
に、炉体10の後部に第2バーナ18と第4バーナ22
とを幅方向に離間して配置し、前後に対向する第1バー
ナ16と第2バーナ18および第3バーナ20と第4バ
ーナ22とを対として構成する。また4基のバーナ1
6,18,20,22の燃焼容量は、同一に設定される。
そして、第1バーナ16と第4バーナ22の燃焼中に
は、対をなす第2バーナ18と第3バーナ20から燃焼
排ガスを排気して蓄熱体を加熱するよう運転され、第2
バーナ18と第3バーナ20の燃焼中には、対をなす第
1バーナ16と第4バーナ22から燃焼排ガスを排気し
て蓄熱体を加熱する運転が行なわれる。
The arrangement of burners in a soaking furnace using the regenerating burner system may be, for example, as shown in FIG. That is, the first burner 1 is provided at the front of the furnace body 10.
6 and the third burner 20 are spaced apart in the width direction, and the second burner 18 and the fourth burner 22
Are arranged apart in the width direction, and the first burner 16 and the second burner 18 and the third burner 20 and the fourth burner 22 facing each other are formed as a pair. 4 burners 1
The combustion capacities of 6, 18, 20, and 22 are set to be the same.
During the combustion of the first burner 16 and the fourth burner 22, the operation is performed to exhaust the combustion exhaust gas from the paired second burner 18 and the third burner 20 to heat the regenerator,
During the combustion of the burner 18 and the third burner 20, an operation of heating the regenerator by exhausting the combustion exhaust gas from the paired first burner 16 and fourth burner 22 is performed.

【0006】[0006]

【発明が解決しようとする課題】前記リジェネバーナシ
ステムを用いる均熱炉では、炉体10の内部前後の温度
を略均一にすることができるから、図6(b)に示すよう
に、複数の鋼塊14を炉体10の炉床24上に長手方向
に所定間隔で横倒し状態(横置き状態)で装入すること
で、該鋼塊14の均一な加熱が可能となる。すなわち、
圧延加工性の難しい種類の鋼塊14を加熱する場合には
好適である。しかし、複数の鋼塊14を横置き状態で装
入する場合は、一度に処理し得る鋼塊14の数が少な
く、炉内温度の均一度が要求されない圧延加工性の良好
な種類の鋼塊14を加熱する場合の処理能力が低下する
欠点がある。なお、図6に示すバーナ配置の均熱炉に、
圧延加工性の良好な種類の鋼塊14を縦置き状態で装入
した場合は、各バーナ16,18,20,22が側壁に近
接して配置されているためにその火炎が鋼塊14に直接
当ってしまい、部分的なオーバーヒートを来す問題があ
り、縦置き状態での装入は採用できない。
In the soaking furnace using the regenerative burner system, since the temperature before and after the inside of the furnace body 10 can be made substantially uniform, as shown in FIG. By loading the steel ingot 14 on the hearth 24 of the furnace body 10 at a predetermined interval in the longitudinal direction in a state of being laid down (sideways), the steel ingot 14 can be uniformly heated. That is,
This is suitable for heating a steel ingot 14 of a type that is difficult to roll. However, when a plurality of steel ingots 14 are charged in a horizontal state, the number of steel ingots 14 that can be processed at one time is small, and a type of steel ingot with good rolling workability that does not require uniformity of furnace temperature is required. There is a disadvantage that the processing capacity when heating 14 is reduced. In addition, in the soaking furnace of the burner arrangement shown in FIG.
When a steel ingot 14 of a type having good rolling workability is charged in a vertical state, the flame is applied to the ingot 14 because the burners 16, 18, 20, and 22 are arranged close to the side walls. There is a problem that it hits directly and causes partial overheating, so charging in a vertical position cannot be adopted.

【0007】[0007]

【発明の目的】この発明は、前述した従来の技術に内在
している前記課題に鑑み、これを好適に解決するべく提
案されたものであって、鋼塊の種類に応じて最適な加熱
運転を選択して、鋼塊の加熱品質を向上し得ると共に処
理能力を向上させ得る均熱方法および均熱炉を提供する
ことを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems inherent in the prior art, and has been proposed in order to solve the problem in a suitable manner. It is an object of the present invention to provide a soaking method and a soaking furnace capable of improving the heating quality of a steel ingot and improving the processing capacity.

【0008】[0008]

【課題を解決するための手段】前述した課題を解決し、
所期の目的を好適に達成するため、本発明に係る均熱方
法は、炉体の内部に、その長手方向に離間して複数の鋼
塊を装入し、これら鋼塊群をリジェネレイティブバーナ
燃焼システムを用いて加熱可能な均熱方法であって、前
記炉体内部の幅方向に対向する両側壁面に沿って複数の
鋼塊を縦置き状態で装入した場合は、炉体の長手方向一
方で鋼塊群に火炎が直接当たらない位置に配置した主バ
ーナのみを燃焼して鋼塊群を加熱し、前記炉体内の炉床
上に横置き状態で複数の鋼塊を装入した場合は、前記主
バーナより燃焼容量が小さく、炉体の長手方向他方で幅
方向に離間して配置した複数の副バーナと、主バーナと
を交互に燃焼して鋼塊群を加熱することを特徴とする。
[MEANS FOR SOLVING THE PROBLEMS]
In order to appropriately achieve the intended purpose, the heat equalizing method according to the present invention comprises charging a plurality of steel ingots inside a furnace body in the longitudinal direction with a distance therebetween, and regenerating these steel ingot groups. A method of equalizing heat that can be heated using a burner combustion system, wherein a plurality of steel ingots are charged vertically along both side walls facing the width direction inside the furnace body. In the case where a plurality of steel ingots are charged in a horizontal state on the hearth in the furnace, by burning only the main burner arranged in a position where the flame does not directly hit the steel ingot in the direction and heating the steel ingot. Is characterized in that the combustion capacity is smaller than that of the main burner, and a plurality of sub-burners arranged in the width direction at the other end in the longitudinal direction of the furnace body and the main burner are alternately burned to heat the steel ingot group. And

【0009】前述した課題を解決し、所期の目的を好適
に達成するため、本願の別の発明に係る均熱炉は、炉体
の内部に、その長手方向に離間して複数の鋼塊を装入
し、これら鋼塊群をリジェネレイティブバーナ燃焼シス
テムを用いて加熱可能な均熱炉であって、 前記炉体の
長手方向に対向する一方の側に配置された主バーナと、
前記炉体の長手方向に対向する他方の側に幅方向に離間
して配置され、前記主バーナより燃焼容量が小さい複数
の副バーナと、前記鋼塊の炉体内部への装入状態に応じ
て、前記主バーナおよび副バーナの燃焼・燃焼停止を制
御する制御装置とから構成したことを特徴とする。
[0009] In order to solve the above-mentioned problems and appropriately achieve the intended purpose, a soaking furnace according to another invention of the present application includes a plurality of steel ingots spaced apart in a longitudinal direction inside a furnace body. A soaking furnace capable of heating these ingot groups using a regenerative burner combustion system, and a main burner disposed on one side of the furnace body facing the longitudinal direction,
A plurality of sub-burners, which are arranged in the width direction on the other side opposite to the longitudinal direction of the furnace body and have a smaller combustion capacity than the main burner, and according to a state of charging the steel ingot into the furnace body. And a control device for controlling combustion and stop of the main burner and the sub burner.

【0010】[0010]

【発明の実施の形態】次に、本発明に係る均熱方法およ
び均熱炉につき、好適な実施例を挙げて、添付図面を参
照しながら以下説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred embodiment of a soaking method and a soaking furnace according to the present invention will be described below with reference to the accompanying drawings.

【0011】図1は、実施例に係る均熱炉の概略構成を
示すものであって、該均熱炉30の炉体32には、その
長手方向(前後方向)一方の側(前部)に、1基の主バーナ
34が幅方向の略中央位置に配置されている。また炉体
32の長手方向の他方の側(後部)に、2基の副バーナ3
6,36が、幅方向の略中央を挟んで幅方向に離間して
配置される。両副バーナ36,36の燃焼容量は、主バ
ーナ34の燃焼容量の約1/2以下に夫々設定されて、
2基の副バーナ36,36と1基の主バーナ34とが、
リジェネバーナシステムにおける対の関係となるよう構
成されている。そして、主バーナ34を燃焼していると
きには、両副バーナ36,36の燃焼を停止したもとで
燃焼排ガスにより副蓄熱体76,76(後述)を加熱し、
両副バーナ36,36を燃焼しているときには、主バー
ナ34の燃焼を停止したもとで燃焼排ガスにより主蓄熱
体74(後述)を加熱する運転を行ない得るよう制御され
る。なお、前記鋼塊14は、その種類に応じて横置き状
態(図1参照)と縦置き状態(図2)との何れかが選択され
て前記炉体32の内部に装入される。
FIG. 1 shows a schematic configuration of a heat equalizing furnace according to an embodiment. A furnace body 32 of the heat equalizing furnace 30 has one side (front part) in a longitudinal direction (front-rear direction) thereof. In addition, one main burner 34 is arranged at a substantially central position in the width direction. Further, two sub-burners 3 are provided on the other side (rear part) of the furnace body 32 in the longitudinal direction.
6, 36 are spaced apart in the width direction with the approximate center in the width direction interposed therebetween. The combustion capacity of each of the sub-burners 36, 36 is set to about 1/2 or less of the combustion capacity of the main burner 34, respectively.
The two sub-burners 36, 36 and one main burner 34
It is configured to have a pair relationship in the regenerative burner system. When the main burner 34 is burning, the sub-heat storage bodies 76, 76 (described later) are heated by the combustion exhaust gas while stopping the combustion of the two sub-burners 36, 36,
When the two sub-burners 36, 36 are burning, control is performed so that the main heat storage 74 (described later) can be heated by the combustion exhaust gas while the combustion of the main burner 34 is stopped. The steel ingot 14 is placed in the furnace body 32 by selecting one of a horizontal state (see FIG. 1) and a vertical state (FIG. 2) according to its type.

【0012】また前記主バーナ34は、図2(a)に示す
如く、炉体32内部の幅方向に対向する両側壁面に沿っ
て縦置き状態で装入した両鋼塊群列の間に火炎が臨む位
置に位置決めされると共に、前記3基のバーナ34,3
6,36の配置高さ位置は、図2(b)に示す如く、前記
縦置き状態で装入された鋼塊群の上端より上方に位置
し、各バーナ34,36,36の火炎が鋼塊群に直接当た
らないようになっている。なお、前記主バーナ34の燃
焼容量は、該主バーナ34を単独で燃焼することで、炉
体32の内部に装入された複数の鋼塊14を、従来と同
等程度の効率で加熱し得る値に設定される。
As shown in FIG. 2 (a), the main burner 34 has a flame between the two steel ingot groups that are vertically installed along both side walls facing the width direction inside the furnace body 32. And the three burners 34, 3
As shown in FIG. 2 (b), the arrangement height positions of the cylinders 6, 36 are located above the upper end of the group of steel ingots charged in the vertical position, and the flame of each burner 34, 36, 36 It does not hit the mass directly. The combustion capacity of the main burner 34 is such that by burning the main burner 34 alone, the plurality of steel ingots 14 charged inside the furnace body 32 can be heated with the same level of efficiency as in the past. Set to value.

【0013】図3は、実施例に係る均熱炉30に採用さ
れるリジェネバーナシステムの概略構成を示すものであ
る。図示しない燃料供給源に接続する燃料供給管38か
ら主燃料分岐管40および副燃料分岐管42が分岐し、
主燃料分岐管40が前記主バーナ34に接続されると共
に、副燃料分岐管42が前記副バーナ36,36に接続
され、各分岐管40,42に対応的に介在させた主燃料
切替弁44および副燃料切替弁46を図4に示す制御装
置48で切替制御することで、燃料供給源からの燃料を
主バーナ34または副バーナ36,36に選択的に供給
するよう構成される。またブロワ50に接続する空気供
給管52から、主空気分岐管54および副空気分岐管5
6が分岐し、主空気分岐管54が前記主バーナ34に接
続されると共に、副空気分岐管56が前記副バーナ3
6,36に接続され、各分岐管54,56に対応的に介在
させた主空気切替弁58および副空気切替弁60を制御
装置48で切替制御することで、ブロワ50からの燃焼
用空気を主バーナ34または副バーナ36,36に選択
的に供給するよう構成してある。
FIG. 3 shows a schematic configuration of a regenerative burner system employed in the heat equalizing furnace 30 according to the embodiment. A main fuel branch pipe 40 and a sub fuel branch pipe 42 branch from a fuel supply pipe 38 connected to a fuel supply source (not shown),
A main fuel branch pipe 40 is connected to the main burner 34, and a sub fuel branch pipe 42 is connected to the sub burners 36, 36, and a main fuel switching valve 44 interposed correspondingly to each branch pipe 40, 42. The fuel supply from the fuel supply source is selectively supplied to the main burner 34 or the sub-burners 36 by controlling the switching of the sub-fuel switching valve 46 by the control device 48 shown in FIG. In addition, from the air supply pipe 52 connected to the blower 50, the main air branch pipe 54 and the sub air branch pipe 5 are connected.
6, the main air branch pipe 54 is connected to the main burner 34, and the sub air branch pipe 56 is connected to the sub burner 3
6 and 36, the main air switching valve 58 and the sub air switching valve 60, which are interposed correspondingly in the branch pipes 54 and 56, are switched by the control device 48 so that the combustion air from the blower 50 is controlled. The main burner 34 or the sub burners 36, 36 are selectively supplied.

【0014】更に、前記主バーナ34に接続された主排
気管62と、前記副バーナ36,36に接続された副排
気管64とが、排気ファン66に接続する元排気管68
に共通的に接続されており、排気ファン66を運転した
もとで各排気管62,64に対応的に介在させた主排気
切替弁70および副排気切替弁72を制御装置48で切
替制御することで、主バーナ34または副バーナ36,
36から選択的に燃焼排ガスを排気する構成になってい
る。
Further, a main exhaust pipe 62 connected to the main burner 34 and a sub-exhaust pipe 64 connected to the sub-burners 36, 36 form a main exhaust pipe 68 connected to an exhaust fan 66.
The main exhaust switching valve 70 and the sub-exhaust switching valve 72 interposed correspondingly to the respective exhaust pipes 62 and 64 are switched by the control device 48 while the exhaust fan 66 is operated. That is, the primary burner 34 or the secondary burner 36,
36, the exhaust gas is selectively exhausted.

【0015】前記主バーナ34における前記主空気分岐
管54および主排気管62が接続される給排気部に、セ
ラミックス製のボールやハニカム体等の主蓄熱体74が
配設されると共に、副バーナ36,36における前記副
空気分岐管56および副排気管64が接続される給排気
部に、セラミックス製のボールやハニカム体等の副蓄熱
体76が配設される。そして、各蓄熱体74,76は、
対応する主バーナ34または副バーナ36,36が燃焼
停止した状態で、他方の副バーナ36,36または主バ
ーナ34の燃焼により生ずる燃焼排ガスにより蓄熱され
た熱量を、燃焼用空気で回収して炉内に還元するべく機
能する。
A main heat storage body 74 such as a ceramic ball or a honeycomb body is disposed at a supply / exhaust portion of the main burner 34 to which the main air branch pipe 54 and the main exhaust pipe 62 are connected, and a sub burner. A sub heat storage body 76 such as a ceramic ball or a honeycomb body is disposed in a supply / exhaust portion to which the sub air branch pipe 56 and the sub exhaust pipe 64 are connected. And each heat storage body 74,76
When the corresponding main burner 34 or sub-burner 36, 36 has stopped burning, the amount of heat stored by the combustion exhaust gas generated by the combustion of the other sub-burner 36, 36 or main burner 34 is recovered by combustion air, and It works to return to within.

【0016】図4に示す制御装置48は、前述したよう
に、前記主燃料切替弁44,副燃料切替弁46,主空気切
替弁58,副空気切替弁60,主排気切替弁70,副排気
切替弁72を開閉制御する。そして、実施例の制御装置
48では、圧延加工性の難しい種類の鋼塊14を加熱す
る場合には、主バーナ34および副バーナ36,36の
燃焼と燃焼停止とを数10秒〜数分間隔で交互に行なう
ように前記各弁の開閉制御を行ない、圧延加工性の良好
な種類の鋼塊14を加熱する場合には、主バーナ34の
みを燃焼するべく各弁の開閉制御を行なうよう設定され
る。
The control device 48 shown in FIG. 4 includes, as described above, the main fuel switching valve 44, sub fuel switching valve 46, main air switching valve 58, sub air switching valve 60, main exhaust switching valve 70, sub exhaust The switching valve 72 is controlled to open and close. Then, in the control device 48 of the embodiment, when heating the steel ingot 14 of a type that is difficult to roll, the combustion of the main burner 34 and the sub-burners 36, 36 and the stop of the combustion are performed at intervals of several tens seconds to several minutes. In order to heat the ingot 14 of a type having good rolling workability, the opening and closing control of each valve is performed so that only the main burner 34 is burned. Is done.

【0017】[0017]

【実施例の作用】次に、前述した実施例に係る均熱炉の
作用につき、均熱方法との関係で説明する。前記均熱炉
30で、圧延加工性の難しい種類の鋼塊14を加熱する
場合は、多数の鋼塊14を、図1(a),(b)に示すよう
に、炉体32の炉床33上に横置き状態で装入する。こ
のときは、前記制御装置48により前記各切替弁44,
46,58,60,70,72が切替制御されて、前記主バ
ーナ34を燃焼した状態で、両副バーナ36,36の燃
焼を停止して副蓄熱体76,76を燃焼排ガスで加熱す
る運転と、両副バーナ36,36を燃焼した状態で、主
バーナ34の燃焼を停止して主蓄熱体74を燃焼排ガス
で加熱する運転とが、数10秒〜数分の間隔で交互に行
なわれるよう繰返される。すなわち、前述したリジェネ
バーナシステムを正規に働かせることで、各バーナ3
4,36,36による燃焼効率の高い加熱が可能で、前記
鋼塊14を高い加熱品質で均一に加熱することができ
る。従って、均熱炉30から取出した鋼塊14を、後工
程で良好に圧延し得る。また前記蓄熱体74,76,76
には、高温の燃焼排ガスと燃焼用空気が短周期で交互に
流れて直接熱交換が行なわれるから、大幅な熱回収効率
の向上が達成でき、省エネルギーとなる。
Next, the operation of the soaking furnace according to the above embodiment will be described in relation to the soaking method. When heating the steel ingot 14 of a type that is difficult to be rolled in the soaking furnace 30, as shown in FIGS. 1A and 1B, a large number of steel ingots 14 are 33 is placed horizontally. At this time, the switching device 44,
The operation in which the switching of 46, 58, 60, 70, 72 is controlled to stop the combustion of both sub-burners 36, 36 and heat the sub-heat storage bodies 76, 76 with the combustion exhaust gas while the main burner 34 is burning. The operation of stopping the combustion of the main burner 34 and heating the main regenerator 74 with the combustion exhaust gas in a state where both sub-burners 36, 36 are burned is performed alternately at intervals of several tens seconds to several minutes. Is repeated as follows. That is, by operating the above-mentioned regenerative burner system properly, each burner 3
4,36,36 enables high heating with high combustion efficiency, and the steel ingot 14 can be heated uniformly with high heating quality. Therefore, the steel ingot 14 taken out from the soaking furnace 30 can be satisfactorily rolled in the subsequent step. The heat storage elements 74, 76, 76
In this case, high-temperature combustion exhaust gas and combustion air alternately flow in a short cycle to perform direct heat exchange, so that a significant improvement in heat recovery efficiency can be achieved, and energy is saved.

【0018】次に、前記均熱炉30で、圧延加工性の良
好な鋼塊14を加熱する場合は、多数の鋼塊14を、図
2に示すように、炉体32の内部両側壁面に沿って縦置
き状態で装入する。このときは、前記制御装置48によ
り前記各切替弁44,46,58,60,70,72が切替
制御されて、前記主バーナ34のみを燃焼して鋼塊14
を加熱する運転が行なわれる。前述したように主バーナ
34は、幅方向の略中央で縦置き状態の鋼塊群の上端よ
り上方に配置されているから、該主バーナ34の火炎が
鋼塊群に直接当たることはなく、部分的なオーバーヒー
トの発生は防止される。
Next, when heating the steel ingot 14 having good rolling workability in the soaking furnace 30, a large number of steel ingots 14 are placed on the inner side wall surfaces of the furnace body 32 as shown in FIG. Along the way, insert it vertically. At this time, the switching valves 44, 46, 58, 60, 70 and 72 are controlled to be switched by the control device 48, so that only the main burner 34 is burned and the steel ingot 14
The operation of heating is performed. As described above, since the main burner 34 is disposed substantially above the upper end of the group of steel ingots in the vertical state at the approximate center in the width direction, the flame of the main burner 34 does not directly hit the group of steel ingots. The occurrence of partial overheating is prevented.

【0019】すなわち、実施例の均熱炉30では、鋼塊
14の種類に応じた炉体32の内部への装入状態(縦置
き状態、横置き状態)に応じて主バーナ34および副バ
ーナ36,36の燃焼・燃焼停止を制御装置48で制御
することで、圧延加工性の難しい種類の鋼塊14におい
ては均一に加熱して加熱品質を向上させ得ると共に、圧
延加工性の良好な種類の鋼塊14においては一度に多く
を処理することができて処理能力を向上し得る。
That is, in the heat equalizing furnace 30 of the embodiment, the main burner 34 and the sub-burner according to the charging state (vertical state, horizontal state) in the furnace body 32 according to the type of the steel ingot 14. By controlling the combustion / suspension of 36, 36 by the control device 48, the ingot 14 of a type difficult to be rolled can be uniformly heated to improve the heating quality, and the type of steel ingot having good rollability can be improved. In the steel ingot 14, a large amount can be processed at a time, and the processing capacity can be improved.

【0020】なお、実施例で説明した均熱方法および均
熱炉の技術は、加熱炉や熱処理炉等にも応用可能であ
る。
The techniques of the soaking method and the soaking furnace described in the embodiments can be applied to a heating furnace, a heat treatment furnace and the like.

【0021】[0021]

【発明の効果】以上説明した如く、本発明に係る均熱方
法および均熱炉では、種類の異なる鋼塊の炉体内部への
装入状態に応じて複数のバーナの燃焼・燃焼停止を制御
して、最適な条件での加熱処理を行ない得る。例えば、
圧延加工性の難しい種類の鋼塊については、主バーナと
副バーナとを交互に燃焼させてリジェネバーナシステム
を正規に働かせることで、鋼塊を均一に加熱して加熱品
質を向上することができる。また、圧延加工性の良好な
種類の鋼塊を加熱する場合には、オーバーヒートを生ず
ることなく一度に多くの鋼塊を縦置き状態で炉体内部に
装入することができ、処理能力を向上し得る。
As described above, in the heat equalizing method and the heat equalizing furnace according to the present invention, the control of the burning / stopping of the plurality of burners in accordance with the state of charging different types of steel ingots into the furnace body. Thus, heat treatment under optimal conditions can be performed. For example,
For ingots of a type that are difficult to roll, it is possible to heat the ingot uniformly and improve the heating quality by firing the primary and secondary burners alternately and operating the regenerative burner system properly. . In addition, when heating ingots of a type with good rolling workability, many ingots can be loaded into the furnace vertically at the same time without overheating, improving the processing capacity. I can do it.

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

【図1】本発明の好適な実施例に係る均熱炉を圧延加工
性の難しい鋼塊を加熱する場合で示す概略構成図であ
る。
FIG. 1 is a schematic configuration diagram showing a case where a steel ingot having difficulty in rolling workability is heated in a heat equalizing furnace according to a preferred embodiment of the present invention.

【図2】実施例に係る均熱炉を圧延加工性の良好な鋼塊
を加熱する場合で示す概略構成図である。
FIG. 2 is a schematic configuration diagram illustrating a soaking furnace according to an example in which a steel ingot having good rolling workability is heated.

【図3】実施例に係る均熱炉に採用されるリジェネバー
ナシステムの概略構成図である。
FIG. 3 is a schematic configuration diagram of a regenerative burner system employed in the soaking furnace according to the embodiment.

【図4】実施例に係る均熱炉の制御ブロック図である。FIG. 4 is a control block diagram of the soaking furnace according to the embodiment.

【図5】従来の技術に係る均熱炉の概略構成図である。FIG. 5 is a schematic configuration diagram of a soaking furnace according to a conventional technique.

【図6】リジェネバーナシステムを採用した従来の技術
に係る均熱炉の概略構成図である。
FIG. 6 is a schematic configuration diagram of a soaking furnace according to a conventional technique employing a regenerative burner system.

【符号の説明】 14 鋼塊 32 炉体 33 炉床 34 主バーナ 36 副バーナ 48 制御装置[Description of Signs] 14 Steel Ingot 32 Furnace Body 33 Hearth 34 Main Burner 36 Secondary Burner 48 Controller

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 炉体(32)の内部に、その長手方向に離間
して複数の鋼塊(14)を装入し、これら鋼塊群をリジェネ
レイティブバーナ燃焼システムを用いて加熱可能な均熱
方法であって、前記炉体(32)内部の幅方向に対向する両
側壁面に沿って複数の鋼塊(14)を縦置き状態で装入した
場合は、炉体(32)の長手方向一方で鋼塊群に火炎が直接
当たらない位置に配置した主バーナ(34)のみを燃焼して
鋼塊群を加熱し、前記炉体(32)内の炉床(33)上に横置き
状態で複数の鋼塊(14)を装入した場合は、前記主バーナ
(34)より燃焼容量が小さく、炉体(32)の長手方向他方で
幅方向に離間して配置した複数の副バーナ(36,36)と、
主バーナ(34)とを交互に燃焼して鋼塊群を加熱すること
を特徴とする均熱方法。
1. A plurality of steel ingots (14) are charged into a furnace body (32) at a distance in a longitudinal direction thereof, and the steel ingots can be heated using a regenerative burner combustion system. In the soaking method, when a plurality of steel ingots (14) are charged in a vertically placed state along both side walls facing in the width direction inside the furnace body (32), the length of the furnace body (32) is increased. Only the main burner (34) arranged at a position where the flame does not directly hit the steel ingot in the direction is heated to heat the steel ingot, and placed horizontally on the hearth (33) in the furnace body (32). When a plurality of steel ingots (14) are charged in the condition,
(34) a plurality of sub-burners (36, 36) having a combustion capacity smaller than that of the furnace body (32) and spaced apart in the width direction at the other longitudinal direction of the furnace body (32)
A soaking method characterized by heating a group of ingots by alternately burning a main burner (34).
【請求項2】 炉体(32)の内部に、その長手方向に離間
して複数の鋼塊(14)を装入し、これら鋼塊群をリジェネ
レイティブバーナ燃焼システムを用いて加熱可能な均熱
炉であって、前記炉体(32)の長手方向に対向する一方の
側に配置された主バーナ(34)と、前記炉体(32)の長手方
向に対向する他方の側に幅方向に離間して配置され、前
記主バーナ(34)より燃焼容量が小さい複数の副バーナ(3
6,36)と、前記鋼塊(14)の炉体(32)内部への装入状態に
応じて、前記主バーナ(34)および副バーナ(36,36)の燃
焼・燃焼停止を制御する制御装置(48)とから構成したこ
とを特徴とする均熱炉。
2. A plurality of steel ingots (14) are charged into a furnace body (32) at a distance in a longitudinal direction thereof, and these steel ingots can be heated using a regenerative burner combustion system. A soaking furnace, a main burner (34) disposed on one side of the furnace body (32) facing the longitudinal direction, and a width on the other side facing the longitudinal direction of the furnace body (32). A plurality of sub-burners (3) having a combustion capacity smaller than that of the main burner (34).
6, 36), and controls the combustion / stop of combustion of the main burner (34) and the sub-burner (36, 36) according to the state of charging the steel ingot (14) into the furnace body (32). A soaking furnace characterized by comprising a control device (48).
【請求項3】 前記副バーナ(36)は2基であって、各副
バーナ(36)の燃焼容量は主バーナ(34)の燃焼容量の約1
/2以下に設定されている請求項2記載の均熱炉。
3. The combustion capacity of each sub-burner (36) is about one of the combustion capacity of the main burner (34).
The heat equalizing furnace according to claim 2, wherein the temperature is set to not more than / 2.
【請求項4】 前記主バーナ(34)は、前記炉体(32)内部
の幅方向に対向する両側壁面に沿って縦置き状態で装入
した両鋼塊群列の間に火炎が臨む位置に配置されている
請求項2または3記載の均熱炉。
4. The main burner (34) is located at a position where a flame faces between two steel ingot groups that are vertically inserted along both side walls facing the width direction inside the furnace body (32). The heat equalizing furnace according to claim 2 or 3, wherein
JP11086599A 1999-03-29 1999-03-29 Soaking method and soaking furnace Pending JP2000282137A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11086599A JP2000282137A (en) 1999-03-29 1999-03-29 Soaking method and soaking furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11086599A JP2000282137A (en) 1999-03-29 1999-03-29 Soaking method and soaking furnace

Publications (1)

Publication Number Publication Date
JP2000282137A true JP2000282137A (en) 2000-10-10

Family

ID=13891487

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11086599A Pending JP2000282137A (en) 1999-03-29 1999-03-29 Soaking method and soaking furnace

Country Status (1)

Country Link
JP (1) JP2000282137A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019138528A (en) * 2018-02-09 2019-08-22 大同特殊鋼株式会社 Heating furnace and method for heating metal material

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019138528A (en) * 2018-02-09 2019-08-22 大同特殊鋼株式会社 Heating furnace and method for heating metal material
JP7062989B2 (en) 2018-02-09 2022-05-09 大同特殊鋼株式会社 Heating furnace and heating method for metal materials

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