JP2011225939A - Continuous heating furnace - Google Patents

Continuous heating furnace Download PDF

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JP2011225939A
JP2011225939A JP2010097212A JP2010097212A JP2011225939A JP 2011225939 A JP2011225939 A JP 2011225939A JP 2010097212 A JP2010097212 A JP 2010097212A JP 2010097212 A JP2010097212 A JP 2010097212A JP 2011225939 A JP2011225939 A JP 2011225939A
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furnace
regenerative
continuous heating
burners
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Toyohiko Morita
豊彦 森田
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Nippon Steel Engineering Co Ltd
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Nippon Steel Engineering Co Ltd
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PROBLEM TO BE SOLVED: To provide a continuous heating furnace which is provided with regenerative burners arranged on both side walls of an upper zone and a lower zone of a preheating area and a heating area, and roof burners or axial-flow burners in an upper zone of a soaking area, and which is capable of inhibiting black smoke from blowing out from clearances of an extracting door of the continuous heating furnace.SOLUTION: The continuous heating furnace is provided with a charging door 21 for charging a billet in one side of the furnace body, an extracting door 22 for extracting the billet in another side, regenerative burners arranged on both side walls in a preheating area 5 and heating areas 6 and 7, roof burners 17a arranged in a ceiling portion of a soaking area 8, and regenerative burners arranged in both side walls of a lower zone 10 of the soaking area 8, wherein a partition wall 23 crossing the furnace body and having a height lower than a walking beam is erected on a hearth between the regenerative burner 27b located nearest the extraction side among the regenerative burners in the lower zone of the soaking area 8 and the regenerative burner 28b adjacent thereto.

Description

本発明は、スラブ、ビレットなどの鋼片を連続的に加熱する連続式加熱炉に関する。   The present invention relates to a continuous heating furnace that continuously heats steel pieces such as slabs and billets.

スラブ、ビレットなどの鋼片を連続的に加熱する連続式加熱炉として、リジェネバーナ(蓄熱式バーナ)を備えた連続式加熱炉が利用されている。以下に図を用いて連続式加熱炉について説明する。   As a continuous heating furnace for continuously heating steel pieces such as slabs and billets, a continuous heating furnace equipped with a regenerative burner (thermal storage burner) is used. The continuous heating furnace will be described below with reference to the drawings.

図4は蓄熱式バーナを備えた従来の連続式加熱炉の断面図、図5は図4に示す連続式加熱炉の上部ゾーンの平面図、図6は図4に示す連続式加熱炉の下部ゾーンの平面図、図7(a)は図4に示す炉の予熱帯及び加熱帯の断面図、図7(b)は図4に示す炉の均熱帯の断面図をそれぞれ示す。   4 is a sectional view of a conventional continuous heating furnace equipped with a regenerative burner, FIG. 5 is a plan view of an upper zone of the continuous heating furnace shown in FIG. 4, and FIG. 6 is a lower portion of the continuous heating furnace shown in FIG. FIG. 7 (a) is a sectional view of the pre-tropical zone and heating zone of the furnace shown in FIG. 4, and FIG. 7 (b) is a sectional view of the soaking zone of the furnace shown in FIG.

連続式加熱炉の炉体1の予熱帯5、加熱帯A6、加熱帯B7の上部ゾーン9及び下部ゾーン10の両側壁には対向して対となるリジェネバーナ11a,11b〜16a,16bが配置され、均熱帯8の下部ゾーン10にはリジェネバーナ18a,18bが配置されている。上部ゾーン9の炉体の天井部には、後工程の圧延による品質向上を目的として鋼片の長手方向(炉幅方向)の加熱温度に傾斜を持たせる等の理由によりルーフバーナ17a、17bが配置されている。上部ゾーン9及び下部ゾーン10には各帯5〜8の境界に各帯5〜8を仕切る仕切り壁19が設けられている。   Regenerative burners 11a, 11b to 16a, 16b, which are opposed to each other, are arranged on both side walls of the pre-tropical zone 5, the heating zone A6, and the upper zone 9 and the lower zone 10 of the heating zone B7 of the furnace 1 of the continuous heating furnace. Regenerative burners 18 a and 18 b are arranged in the lower zone 10 of the soaking zone 8. Roof burners 17a and 17b are arranged on the ceiling of the furnace body in the upper zone 9 for the purpose of increasing the heating temperature in the longitudinal direction (furnace width direction) of the steel slab for the purpose of improving quality by rolling in the subsequent process. Has been. The upper zone 9 and the lower zone 10 are provided with partition walls 19 that partition the bands 5 to 8 at the boundaries of the bands 5 to 8.

鋼片3は装入扉21を開いて炉内に装入され、図7に示すウォーキングビーム4で炉内を順次予熱帯5、加熱帯A6、加熱帯B7、均熱帯8へと搬送中に加熱され、抽出扉22を開いて系外に搬出される。前記バーナから燃焼・排出された排ガスは煙道2から系外へ排出される。   The steel slab 3 is inserted into the furnace by opening the charging door 21, and is being conveyed to the pre-tropical zone 5, the heating zone A 6, the heating zone B 7, and the soaking zone 8 by the walking beam 4 shown in FIG. Heated, the extraction door 22 is opened and carried out of the system. The exhaust gas combusted and discharged from the burner is discharged from the flue 2 to the outside of the system.

図8は他の構造を有する従来の連続式加熱炉の断面図であり、図9は図8に示す炉の上部ゾーンの平面図である。この連続式加熱炉と図4〜図7で示した従来の連続式加熱炉との構成の相違は均熱帯の上部ゾーンの天井部にルーフバーナの代わりに軸流バーナ20a、20bを配設した点であり、他の構成は同じである。   FIG. 8 is a cross-sectional view of a conventional continuous heating furnace having another structure, and FIG. 9 is a plan view of the upper zone of the furnace shown in FIG. The difference between the configuration of this continuous heating furnace and the conventional continuous heating furnace shown in FIGS. 4 to 7 is that axial flow burners 20a and 20b are arranged in place of the roof burner at the ceiling of the soaking zone. The other configurations are the same.

ところで、前記従来の両加熱炉に配設されているリジェネバーナは低NOx化のため、燃焼空気と燃料の投入口を離して緩慢燃焼させる形式が一般的になっている。このような燃焼空気と燃料の投入口を離したリジェネバーナを使用した場合、最も抽出側(抽出扉側)に配置されたリジェネバーナにおいて、抽出扉22側に抽出前壁24が存在するためバーナから炉内へ吹き込んだ燃焼空気と燃料ガスが抽出前壁24側へ吸い寄せられ、抽出前壁24に沿って緩慢燃焼をしながら炉巾方向へ流れる。一方、加熱炉の抽出扉22部分を完全にシールすることは不可能であるため炉内圧力をプラス圧として抽出扉22部分からの外気侵入を防止しており、抽出扉22付近の炉内排ガスは常に抽出扉22部分の隙間から炉外へ排出されるが、緩慢燃焼による未燃の燃料が図10に示すように抽出前壁24に沿ったガス流れ25となり、その一部が抽出扉22部分の隙間から黒煙となって吹き出し、環境を汚染するという問題がある。   By the way, in order to reduce NOx, the regenerative burner disposed in the conventional both heating furnaces is generally in the form of slow combustion with the combustion air and fuel inlets separated. When such a regenerative burner with the combustion air and fuel inlets separated is used, in the regenerative burner arranged on the most extraction side (extraction door side), the extraction front wall 24 exists on the extraction door 22 side, so the burner Combustion air and fuel gas blown into the furnace are sucked toward the extraction front wall 24 and flow in the furnace width direction while slowly burning along the extraction front wall 24. On the other hand, since it is impossible to completely seal the extraction door 22 portion of the heating furnace, the pressure inside the furnace is set to a positive pressure to prevent intrusion of outside air from the extraction door 22 portion, and the exhaust gas in the furnace near the extraction door 22 is prevented. Is always discharged out of the furnace through the gap of the extraction door 22 portion, but unburned fuel due to slow combustion becomes a gas flow 25 along the extraction front wall 24 as shown in FIG. There is a problem that black smoke is blown out from the gap between the parts and pollutes the environment.

前述の抽出扉22からの黒煙吹き出し防止技術が特許文献1に開示されている。特許文献1には、均熱帯の上部ゾーンの炉体の両側壁にリジェネバーナが対向配設された連続式加熱炉において、炉内の排ガス流れを改善し、前記未燃の燃料が抽出扉の隙間から吹き出すのを防ぐ方法が示されている。   Patent Document 1 discloses a technique for preventing black smoke from the extraction door 22 described above. In Patent Document 1, in a continuous heating furnace in which a regenerative burner is opposed to both sides of a furnace body in a soaking zone in the upper zone, the exhaust gas flow in the furnace is improved, and the unburned fuel flows into the extraction door. It shows how to prevent blowing out of the gap.

特開2008−240133号公報JP 2008-240133 A

しかしながら、前記特許文献1に記載されている技術では、本発明が対象としている均熱帯の上部ゾーンの天井部にルーフバーナ又は軸流バーナを配設し、下部ゾーンにのみリジェネバーナを使用している前記従来の連続式加熱炉の炉内の排ガス流れを改善することができないため、前記のとおり未燃の燃料が抽出扉の隙間から黒煙となって吹き出して環境を汚染するという問題を解決することができない。   However, in the technique described in Patent Document 1, a roof burner or an axial flow burner is disposed on the ceiling of the soaking zone, which is the subject of the present invention, and a regeneration burner is used only in the lower zone. Since the exhaust gas flow in the furnace of the conventional continuous heating furnace cannot be improved, as described above, the problem that unburned fuel blows out as black smoke from the gap of the extraction door and pollutes the environment is solved. I can't.

そこで、本発明は、予熱帯、加熱帯の上部ゾーン及び下部ゾーンの両側壁にジェネバーナを配置し、均熱帯の上部ゾーンにルーフバーナ又は軸流バーナを配設してなる連続式加熱炉において、抽出扉の隙間から黒煙が吹き出すのを抑制することが可能な連続式加熱炉を提供するものである。   Accordingly, the present invention provides a continuous heating furnace in which a gene burner is arranged on both side walls of the pre-tropical zone, the upper zone and the lower zone of the heating zone, and a roof burner or an axial flow burner is arranged in the upper zone of the soaking zone. The present invention provides a continuous heating furnace capable of suppressing black smoke from blowing out from a gap between doors.

本発明は、予熱帯、加熱帯及び均熱帯が鋼片の搬送方向に順次配置された炉体の一端に鋼片の装入扉を有するとともに他端に鋼片の抽出扉を有し、予熱帯及び加熱帯のそれぞれの上部ゾーン及び下部ゾーンの両側壁に対向して対となる複数のリジェネバーナが配置され、均熱帯の上部ゾーンの天井部にルーフバーナ又は軸流バーナが配置され、均熱帯の下部ゾーンの両側壁に対向して対となる複数のリジェネバーナが配置されている連続式加熱炉において、均熱帯の下部ゾーンに配置された前記複数のリジェネバーナのうち、最も抽出側に位置する一対のリジェネバーナとこのリジェネバーナと隣接する一対のリジェネバーナとの間に、炉体を横断し且つ高さがウォーキングビームより低い仕切り壁を炉床上に立設したことを特徴とする。   The present invention has a billet loading door at one end of a furnace body in which the pre-tropical zone, heating zone and soaking zone are sequentially arranged in the billet conveyance direction, and a billet extraction door at the other end. A pair of regenerative burners are arranged opposite to both side walls of the upper zone and lower zone of the tropical zone and the heating zone, and a roof burner or an axial flow burner is placed on the ceiling of the upper zone of the tropical zone. In a continuous heating furnace in which a plurality of regenerative burners that are paired facing both side walls of the lower zone are arranged, among the plurality of regenerative burners arranged in the lower zone of the soaking zone, it is located on the most extraction side A partition wall that crosses the furnace body and has a height lower than that of the walking beam is erected on the hearth between the pair of regenerative burners and the pair of adjacent regenerative burners.

また、本発明は、前記構成において、前記最も抽出側に位置する一対のリジェネバーナと仕切り壁との炉体長手方向の間隔を、前記一対のリジェネバーナと抽出前壁との炉体長手方向との間隔より短くしたり、前記仕切り壁の抽出側の立設面にコーティング材を塗布したりすることを特徴とする。   Further, according to the present invention, in the above configuration, the furnace body longitudinal direction between the pair of regenerative burners located on the most extraction side and the partition wall in the furnace body longitudinal direction between the pair of regenerative burners and the extraction front wall Or a coating material is applied to the standing surface on the extraction side of the partition wall.

本発明は、均熱帯の下部ゾーンの炉体の両側壁に配置されたリジェネバーナのうち、最も抽出側に位置する一対のリジェネバーナから吹き込まれた燃料ガスと燃焼空気を炉床から立設された仕切り壁に沿って流すことによって、燃焼空気と燃料ガスが炉内で燃焼を完了するのに必要な時間が確保され、燃焼空気と燃料ガスを炉内で完全に燃焼させることができるので、抽出扉の隙間から燃焼途中の未燃分が黒煙となって吹き出すことを防止することができる。   In the present invention, the fuel gas and the combustion air blown from the pair of regenerative burners located on the most extraction side among the regenerative burners arranged on both side walls of the furnace body in the lower zone of the soaking zone are erected from the hearth. By flowing along the partition wall, the time required for the combustion air and fuel gas to complete combustion in the furnace is secured, and the combustion air and fuel gas can be completely burned in the furnace. It is possible to prevent the unburned portion in the middle of combustion from being blown out as black smoke from the gap of the extraction door.

本発明の仕切り壁を配設した連続式加熱炉の断面図である。It is sectional drawing of the continuous heating furnace which arrange | positioned the partition wall of this invention. 図1に示す下部ゾーンの平面図である。It is a top view of the lower zone shown in FIG. 図2に示す下部ゾーンの均熱帯の部分拡大図である。FIG. 3 is a partially enlarged view of a soaking zone in the lower zone shown in FIG. 2. 均熱帯の上部ゾーンにルーフバーナを配設した従来の連続式加熱炉の断面図である。It is sectional drawing of the conventional continuous heating furnace which arrange | positioned the roof burner in the soaking zone upper zone. 図4に示す炉の上部ゾーンの平面図である。FIG. 5 is a plan view of the upper zone of the furnace shown in FIG. 4. 図4に示す炉の上部ゾーンの平面図である。FIG. 5 is a plan view of the upper zone of the furnace shown in FIG. 4. (a)は図4に示す炉の予熱帯、(b)は均熱帯の断面図である。(A) is the pre-tropical zone of the furnace shown in FIG. 4, (b) is a cross-sectional view of the soaking zone. 均熱帯の上部ゾーンに軸流バーナを配設した従来の連続式加熱炉の断面図である。It is sectional drawing of the conventional continuous heating furnace which arrange | positioned the axial-flow burner in the soaking zone upper zone. 図8に示す炉の上部ゾーンの平面図である。It is a top view of the upper zone of the furnace shown in FIG. 図4または図8に示す下部ゾーンの均熱帯の部分拡大図である。FIG. 9 is a partially enlarged view of a soaking zone in the lower zone shown in FIG. 4 or FIG. 8.

図面を参照しつつ、本発明の実施の形態につき説明する。   Embodiments of the present invention will be described with reference to the drawings.

本実施例1の連続式加熱炉の炉体は、図4〜図7で示したルーフバーナを配設した従来の連続式加熱炉と実質同一である。すなわち、図1に示すとおり、炉体1は、被熱物である鋼材3を搬送・加熱する方向に、4つのゾーンである予熱帯5、加熱帯A6、加熱帯B7、均熱帯8で区分されている。予熱帯5、加熱帯A6、加熱帯B7の上部ゾーン9及び下部ゾーン10の炉体1の側壁に、対向して対となるリジェネバーナ11a,11b〜16a,16bが配設され、均熱帯8の上部ゾーン9の炉体1の天井部には、複数のルーフバーナ17a、17bが配置され、下部ゾーンにはリジェネバーナ18a,18bが配置され、各帯を仕切るため仕切り壁19が設けられる。   The furnace body of the continuous heating furnace of the first embodiment is substantially the same as the conventional continuous heating furnace provided with the roof burner shown in FIGS. That is, as shown in FIG. 1, the furnace body 1 is divided into four zones, a pre-tropical zone 5, a heating zone A 6, a heating zone B 7, and a soaking zone 8, in the direction of conveying and heating the steel material 3 that is the object to be heated. Has been. Regenerative burners 11a, 11b to 16a, 16b, which are opposed to each other, are disposed on the side walls of the furnace zone 1 in the upper zone 9 and the lower zone 10 of the pre-tropical zone 5, heating zone A6, and heating zone B7. A plurality of roof burners 17a and 17b are disposed in the ceiling portion of the furnace body 1 in the upper zone 9, and regenerative burners 18a and 18b are disposed in the lower zone, and a partition wall 19 is provided to partition each band.

鋼片3は、炉体1の一方に設けられている装入扉21から炉内に装入され、炉内を搬送中に加熱・均熱され、炉体1の他方に設けられている抽出扉22から系外に出される。以上は、前記のとおり従来の連続式加熱炉の構成と同じである。   The steel piece 3 is inserted into the furnace from a charging door 21 provided on one side of the furnace body 1, heated and soaked during conveyance in the furnace, and extracted on the other side of the furnace body 1. It is taken out of the system from the door 22. The above is the same as the structure of the conventional continuous heating furnace as described above.

本実施例1では、図1〜図3に示すように、抽出前壁24の近傍には、最も抽出側に位置する一対のリジェネバーナ27a,27bが設けられ、このバーナ27a,27bに隣接して、一対のリジェネバーナ28a,28bが設けられている。   In the first embodiment, as shown in FIGS. 1 to 3, a pair of regenerative burners 27 a and 27 b located closest to the extraction side is provided in the vicinity of the extraction front wall 24, and adjacent to the burners 27 a and 27 b. A pair of regenerative burners 28a and 28b is provided.

最も抽出側のバーナ27a,27bとこのバーナに隣接するバーナ28a,28bの炉体の長手方向の間で、炉床上に炉体1を横断するとともに、高さがウォーキングビーム4より低い仕切り壁23が立設されている。仕切り壁23は、各帯5〜8の仕切り壁19と同様に、例えば、耐火煉瓦を築造することにより構成されている。   A partition wall 23 that crosses the furnace body 1 on the hearth and has a height lower than that of the walking beam 4 between the longitudinal side of the furnace body of the burners 27a and 27b on the most extraction side and the burners 28a and 28b adjacent to the burner. Is erected. The partition wall 23 is configured by, for example, building a refractory brick, similarly to the partition walls 19 of the bands 5 to 8.

図3において、下側にあるリジェネバーナ27bが燃焼している場合、燃焼ガスと空気の流れは仕切り壁23に沿った矢印26で示す状態になる。バーナ27bから吹き込まれた燃料ガスと燃焼空気は、炉床から立設された仕切り壁23が存在するため、コアンダ効果により仕切り壁23に沿って流れ、両者が炉内で燃焼を完了するのに必要な時間を確保されて炉内で完全に燃焼する。それにより、抽出扉22の隙間から燃焼途中の未燃分が黒煙となって吹き出すことを防止することができる。   In FIG. 3, when the regenerative burner 27 b on the lower side is burning, the flow of combustion gas and air is in the state indicated by the arrow 26 along the partition wall 23. The fuel gas and the combustion air blown from the burner 27b flow along the partition wall 23 due to the Coanda effect because the partition wall 23 standing from the hearth exists, and both of them complete the combustion in the furnace. The necessary time is ensured and it burns completely in the furnace. Thereby, it can prevent that the unburned part in the middle of combustion turns into black smoke and blows out from the clearance gap of the extraction door 22. FIG.

最も抽出側に位置する一対のリジェネバーナ27a,27bと仕切り壁23との炉体長手方向の間隔を、一対のリジェネバーナ27a,27bと抽出前壁24との炉体長手方向との間隔より短くすることにより、コアンダ効果を更に増加させることが可能となり、抽出扉22の隙間からの未燃の燃料が吹き出すことが確実に防止可能となる。   The distance in the furnace longitudinal direction between the pair of regenerative burners 27a, 27b located on the most extraction side and the partition wall 23 is shorter than the distance between the pair of regenerative burners 27a, 27b and the front wall 24 in the furnace longitudinal direction. By doing so, it becomes possible to further increase the Coanda effect, and it is possible to reliably prevent unburned fuel from blowing out from the gap of the extraction door 22.

さらに、仕切り壁23の抽出側の耐火煉瓦の立設面に、コーティング材を塗布すると、前記コアンダ効果をさらに増加させることが可能となり、抽出扉22の隙間からの未燃の燃料が吹き出すことが確実に防止可能となる。なお、耐火煉瓦に塗布するコーティング材としては、耐熱性のアルミナを主成分とする吹きつけ材等が好ましい。   Furthermore, if a coating material is applied to the standing surface of the refractory brick on the extraction side of the partition wall 23, the Coanda effect can be further increased, and unburned fuel from the gap of the extraction door 22 can be blown out. It can be surely prevented. In addition, as a coating material apply | coated to a refractory brick, the spraying material etc. which have a heat resistant alumina as a main component are preferable.

本実施例2の連続式加熱炉の炉体は、図8で示した軸流バーナを配設した従来の連続式加熱炉と実質同一である。   The furnace body of the continuous heating furnace of Example 2 is substantially the same as the conventional continuous heating furnace provided with the axial flow burner shown in FIG.

図4〜図7で示した実施例1との相違点は、均熱帯の上部ゾーンの天井部にルーフバーナの代わりに軸流バーナが配置されている点のみであり、他の仕切り壁などの構成は、同一である。すなわち、実施例1と同様に、最も抽出側に位置する一対のリジェネバーナと隣接する一対のリジェネバーナとの間の炉床上に、炉体を横断し、高さがウォーキングビームより低い仕切り壁が設けられる。   The only difference from the first embodiment shown in FIGS. 4 to 7 is that an axial flow burner is disposed in place of the roof burner at the ceiling of the upper zone in the soaking zone, and the configuration of other partition walls, etc. Are identical. That is, as in Example 1, a partition wall that crosses the furnace body and has a height lower than that of the walking beam on the hearth between the pair of regenerative burners located on the most extraction side and the adjacent pair of regenerative burners. Provided.

本実施例2においても、実施例1と同様に、仕切り壁により、最も抽出側に位置する一対のリジェネバーナから吹き込まれた燃料ガスと燃焼空気は、仕切り壁に沿って流れ、炉内で燃焼を完了するのに必要な時間を確保されて炉内で完全に燃焼するので、抽出扉の隙間から燃焼途中の未燃分が吹き出すことを防止することができる。   Also in the second embodiment, as in the first embodiment, the fuel gas and the combustion air blown from the pair of regeneration burners located on the most extraction side by the partition wall flow along the partition wall and burn in the furnace. Since the time required to complete the process is ensured and combustion is completely performed in the furnace, it is possible to prevent the unburned part during combustion from being blown out from the gap of the extraction door.

1:連続式加熱炉の炉体
2:煙道
3:鋼片
4:ウォーキングビーム
5:予熱帯
6:加熱帯A
7:加熱帯B
8:均熱帯
9:上部ゾーン
10:下部ゾーン
11a,11b〜16a,16b:リジェネバーナ
17a,17b:ルーフバーナ
18a,18b:リジェネバーナ
19:各帯の仕切り壁
20a,20b:軸流バーナ
21:装入扉
22:抽出扉
23:仕切り壁
24:抽出前壁
25:ガスの流れ
26:ガスの流れ
27a,27b:最も抽出側に位置するリジェネバーナ
28a,28b:リジェネバーナ27に隣接するリジェネバーナ
1: Continuous heating furnace body 2: Flue 3: Steel slab
4: Walking beam 5: Pre-tropical
6: Heating zone A
7: Heating zone B
8: Soaking zone 9: Upper zone 10: Lower zone 11a, 11b-16a, 16b: Regenerative burner 17a, 17b: Roof burner
18a, 18b: Regenerative burner 19: Partition wall of each band
20a, 20b: Axial flow burner 21: Loading door 22: Extraction door 23: Partition wall 24: Extraction wall 25: Gas flow 26: Gas flow 27a, 27b: Regenerative burners 28a, 28b located on the most extraction side : Regeneration burner adjacent to regeneration burner 27

Claims (3)

予熱帯、加熱帯及び均熱帯が鋼片の搬送方向に順次配置された炉体の一端に鋼片の装入扉を有するとともに他端に鋼片の抽出扉を有し、予熱帯及び加熱帯のそれぞれの上部ゾーン及び下部ゾーンの両側壁に対向して対となる複数のリジェネバーナが配置され、均熱帯の上部ゾーンの天井部にルーフバーナ又は軸流バーナが配置され、均熱帯の下部ゾーンの両側壁に対向して対となる複数のリジェネバーナが配置されている連続式加熱炉において、
均熱帯の下部ゾーンに配置された前記複数のリジェネバーナのうち、最も抽出側に位置する一対のリジェネバーナとこのリジェネバーナと隣接する一対のリジェネバーナとの間に、炉体を横断し且つ高さがウォーキングビームより低い仕切り壁を炉床上に立設したことを特徴とする連続式加熱炉。
Pre-tropical zone, heating zone and soaking zone are sequentially arranged in the conveying direction of the steel slabs. The furnace body has a billet loading door at one end and a billet extraction door at the other end. A plurality of regenerative burners are arranged opposite to the both side walls of each upper zone and lower zone, and a roof burner or an axial flow burner is placed on the ceiling of the soaking zone. In a continuous heating furnace in which a plurality of regenerative burners that are opposed to both side walls are arranged,
Among the plurality of regenerative burners arranged in the lower tropical zone, between the pair of regenerative burners located closest to the extraction side and the pair of regenerative burners adjacent to the regenerative burner, A continuous heating furnace characterized in that a partition wall lower than the walking beam is installed on the hearth.
前記最も抽出側に位置する一対のリジェネバーナと仕切り壁との炉体長手方向の間隔を、前記一対のリジェネバーナと抽出前壁との炉体長手方向との間隔より短くすることを特徴とする請求項1に記載の連続式加熱炉。   The distance between the pair of regenerative burners located on the most extraction side and the partition wall in the longitudinal direction of the furnace body is shorter than the distance between the pair of regenerative burners and the front wall of the extraction body in the longitudinal direction of the furnace body. The continuous heating furnace according to claim 1. 前記仕切り壁の抽出側の立設面にコーティング材を塗布したことを特徴とする請求項1又は2に記載の連続式加熱炉。   The continuous heating furnace according to claim 1 or 2, wherein a coating material is applied to a standing surface on the extraction side of the partition wall.
JP2010097212A 2010-04-20 2010-04-20 Continuous heating furnace Withdrawn JP2011225939A (en)

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