JPS62155488A - Regulator for quantity of heat transfer of heating furnace - Google Patents

Regulator for quantity of heat transfer of heating furnace

Info

Publication number
JPS62155488A
JPS62155488A JP29934885A JP29934885A JPS62155488A JP S62155488 A JPS62155488 A JP S62155488A JP 29934885 A JP29934885 A JP 29934885A JP 29934885 A JP29934885 A JP 29934885A JP S62155488 A JPS62155488 A JP S62155488A
Authority
JP
Japan
Prior art keywords
furnace
heating furnace
zone
nose
nose portion
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
JP29934885A
Other languages
Japanese (ja)
Inventor
中塚 満
竹村 眞宣
勇司 田中
哲朗 北村
下里 比佐志
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP29934885A priority Critical patent/JPS62155488A/en
Publication of JPS62155488A publication Critical patent/JPS62155488A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 ;1蛮業上の利用分野〕 本発明は、加熱炉の伝熱量調整装置に関し、特二二ノー
ズ部での被加熱材への排ガス下流側及び上流側からの伝
熱量を均一化できるようにした伝熱量調整装置に関する
[Detailed description of the invention]; 1. Field of industrial application] The present invention relates to a heat transfer amount adjusting device for a heating furnace, and relates to a device for adjusting the amount of heat transfer in a heating furnace. The present invention relates to a heat transfer amount adjusting device that can equalize the amount of heat.

〔従来の技(ネi〕[Traditional technique (nei)]

−Cに、加熱炉は炉本体を長手方向に予熱帯1加熱帯及
び均熱帯に分割するとともに、茶器に多数のバーナを配
設し、茶器ごとに温度側1111を行うようにしでいる
。そして各帯の境界部分には、炉内の高さ寸法を他の部
分より小さくしてなるノース部が形成されており、この
ノーズ部は、各帯筋の温度制御刊を隣接する・11″F
からの影響をあまり受−することなく独立して行うため
、及びバーナを炉)[畠方向、つまり排ガスの流れ方向
と直交する線上にδいて炉長方向に向けて配設するため
に設けられている。
-C, the heating furnace has a furnace main body divided into a preheating zone, a heating zone, and a soaking zone in the longitudinal direction, and a large number of burners are arranged on the tea utensils, so that the temperature side 1111 is performed for each tea utensil. A north part is formed at the boundary between each band, and the height inside the furnace is smaller than other parts. F
The burner is installed so that it can be operated independently without being affected by the ing.

ところで、上記茶器ごとの温度制御においては、一般に
上流側帯はど炉温を高く設定するようにしており、従っ
て各帯の境界部、つまりト記ノーズ部における被加執材
への伝熱量は、上流側からの量が下流側からの星より大
きくなる。そのため、被加熱材は上流側が下流側より高
温になり、特にビレットのように小断面のものでは上流
側に凸状に湾曲し易い。その結果、従来、ビレットが搬
送中に転倒したり、ビレット間隔が変化するトラッキン
グエラーか生したりして抽出作業に支障が生しろ等、加
軌炉の安定操業が困難となって生産性が低下するという
問題があった。
By the way, in the above-mentioned temperature control for each tea utensil, the furnace temperature of the upstream side zone is generally set high, so the amount of heat transferred to the workpiece at the boundary between each zone, that is, the nose section, is as follows: The amount from the upstream side is larger than the star from the downstream side. Therefore, the upstream side of the material to be heated becomes hotter than the downstream side, and in particular, a material with a small cross section such as a billet tends to curve into a convex shape toward the upstream side. As a result, in the past, billets would topple over during transportation, or tracking errors would occur due to changes in billet spacing, which would hinder extraction operations, making stable operation of the processing furnace difficult and reducing productivity. There was a problem with the decline.

そごで、従来の加熱炉では、このようなビレ。In the conventional heating furnace, this kind of fin.

トの曲がり、転倒事故を防止するために、各帯間の炉内
温度の差を少なくするようにした操業を行う場合が多い
。このような方法によれば、上記ノーズ部における被加
熱材への上流側がらと下流側からとの伝2Hの差が少な
くなり、従ってビレットの曲がり、転倒事故を防止でき
、合わせてビレット下面のスキッドボタン付近のスキッ
ドマークを改善することもできる。
In order to prevent accidents such as bending and tipping over, operations are often carried out to reduce the difference in temperature inside the furnace between each zone. According to such a method, the difference in the transmission 2H between the upstream side and the downstream side of the material to be heated at the nose portion is reduced, and therefore billet bending and falling accidents can be prevented, and the bottom surface of the billet can be prevented. Skid marks near the skid button can also be improved.

3発明が解決しようとする問題点〕 ところが、上記従来方法では、下流側帯の炉温を高くし
て各帯間の温度差を少なくするのであるから、必然的に
下流側帯の燃焼量を必要以上に大きくすることとなり、
その分燃焼排ガス量が増大し、しかも排ガスの炉尻温度
が高くなり、結局上記従来の加熱炉では排ガス損失が増
大して燃料原単位を悪化させる問題がある。
3. Problems to be Solved by the Invention] However, in the above conventional method, since the furnace temperature in the downstream zone is increased to reduce the temperature difference between each zone, it is inevitable that the combustion amount in the downstream zone will be increased more than necessary. It will be enlarged to
The amount of combustion exhaust gas increases accordingly, and the temperature of the exhaust gas at the bottom of the furnace increases.As a result, in the conventional heating furnace, the exhaust gas loss increases and the fuel consumption rate deteriorates.

本発明はこのような従来の問題点を解消するためになさ
れたもので、ノーズ部における被加熱材の下流側及び上
流側からの伝熱量を均一化して、被加熱材の加熱品質を
向上できるとともに、曲がりを防止して操業の安定性を
向上でき、かつ燃で4原車位を向上できる加熱炉の伝熱
量調整装置を提供することを目的としている。
The present invention has been made to solve these conventional problems, and can improve the heating quality of the heated material by equalizing the amount of heat transferred from the downstream and upstream sides of the heated material at the nose part. Another object of the present invention is to provide a heat transfer amount adjusting device for a heating furnace that can prevent bending, improve operational stability, and increase fuel consumption by 4 degrees.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、各温度制御帯の境界にノーズ部が形成された
加熱炉において、このノーズ部の入口部の少なくとも上
部に、耐熱性及び通気性の高い板状の輻射部材を、炉幅
方向に、かつ排ガスの流れと略直交するように配設した
ことを特徴とする伝熱量調整装置である。
The present invention provides a heating furnace in which a nose portion is formed at the boundary of each temperature control zone, and a plate-shaped radiant member with high heat resistance and air permeability is provided at least above the inlet portion of the nose portion in the width direction of the furnace. , and is arranged so as to be substantially perpendicular to the flow of exhaust gas.

ここで、本発明における輻射部材の耐熱性は、該輻射部
材を設置する温度制御帯の設定温度によって適宜決定さ
れるものであり、また通気性は炉圧制御に支障のない程
度であればよく、例えばセラミックを用いてハニカム状
あるいは綿状の板状体に成形焼成することにより実現で
きる。
Here, the heat resistance of the radiant member in the present invention is appropriately determined by the set temperature of the temperature control zone in which the radiant member is installed, and the air permeability may be at a level that does not interfere with furnace pressure control. This can be realized, for example, by molding and firing ceramic into a honeycomb-like or cotton-like plate-like body.

:作用〕 本発明に係る伝熱量調整装置では、上流側帯からの高温
の燃焼排ガスによって輻射部材が加熱され、該部材から
の輻射熱により、被加熱材へのノーズ部下流側からの伝
熱量が増大し、これにより下流側からの伝熱量と上流側
からの伝熱量とが均一化され、その結果被加熱材が均一
に温度上昇して加執品質が向トするとともに、曲がりを
防止して操業が安定化し、さらに、下流側帯のが温を必
要以上に高くする必要がないので、排ガス損失がσ友少
して燃I4原単位が向上する。
: Effect] In the heat transfer amount adjusting device according to the present invention, the radiant member is heated by the high temperature combustion exhaust gas from the upstream side zone, and the amount of heat transferred from the downstream side of the nose portion to the heated material is increased by the radiant heat from the member. As a result, the amount of heat transferred from the downstream side and the amount of heat transferred from the upstream side are equalized, and as a result, the temperature of the heated material rises uniformly, improving the cutting quality and preventing bending during operation. Furthermore, since there is no need to raise the temperature of the downstream zone more than necessary, the exhaust gas loss is reduced by σ, and the fuel consumption rate is improved.

〔実施例] 以下、本発明の実施例を図について説明する。〔Example] Hereinafter, embodiments of the present invention will be described with reference to the drawings.

第1図及び第2図は本発明の一実施例による加熱炉の伝
熱量調整装置を説明するためのものである。該伝熱量調
整装置が配設された加熱炉の全体構成を示す第2図にお
いて、1はウオーキングビーム型ビレット連続加熱炉で
あり、これは主として、炉本体2と、アップティク型煙
道3と、ビレ7ト装入、抽出装置4と、ビレット炉内搬
送装置5とから構成されている。
FIG. 1 and FIG. 2 are for explaining a heat transfer amount adjusting device for a heating furnace according to an embodiment of the present invention. In FIG. 2 showing the overall configuration of a heating furnace in which the heat transfer amount adjusting device is installed, 1 is a walking beam type billet continuous heating furnace, which mainly consists of a furnace body 2, an uptick type flue 3, , a billet charging and extraction device 4, and a billet in-furnace conveying device 5.

上記炉本体2は、予熱帯7.加熱帯8.均熱帯9とから
構成されている。茶釜の境界部にはその炉内高さが他の
部分より低いノーズ部15.16が形成され、この各ノ
ーズ部15.16は天井壁を下方に凹設してなる上部ノ
ーズ部15a、16aと、床壁を上方に凹設してなる下
部ノーズ部15b、16bとからなり、各ノーズ部の縦
壁であるバーナ壁には多数のバーナ6が炉幅方向に配設
されている。
The furnace main body 2 has a preheating zone 7. Heating zone8. It consists of 9 soaking zones. Nose portions 15.16 are formed at the boundaries of the tea kettle, and the height inside the furnace is lower than the other portions, and each of these nose portions 15.16 is formed by recessing the ceiling wall downward into upper nose portions 15a, 16a. and lower nose parts 15b and 16b formed by recessing the floor wall upwards, and a large number of burners 6 are arranged in the furnace width direction on the burner wall which is the vertical wall of each nose part.

また、上記ビレ7ト炉内搬送装置5は、偏心輪式ウオー
キングビーム型のもので、王として炉内に固定された固
定ビーム10と、炉内で矩形運動をする移動ビーム11
と、該移動ビーム11を炉外にて支持し、駆動するフレ
ーム12と、該フレ−ム12を上下動させる偏心輪装置
13及び前後V」させるシリンダ装置14から構成され
ており、上記固定ビーム10.移動ビーム11の上面は
炉本体2の高さ方向略中央に位置している。
The billet in-furnace transfer device 5 is of an eccentric walking beam type, and includes a fixed beam 10 fixed in the furnace as a king, and a moving beam 11 that moves rectangularly in the furnace.
The frame 12 supports and drives the movable beam 11 outside the furnace, an eccentric wheel device 13 that moves the frame 12 up and down, and a cylinder device 14 that moves the frame 12 back and forth. 10. The upper surface of the moving beam 11 is located approximately at the center of the furnace body 2 in the height direction.

そして上記各上、下部ノーズ部15a、15b。and the respective upper and lower nose portions 15a, 15b.

及び16a、16bの入口側、つまり排ガスGの流れ方
向下流側に、本実施例の伝熱品調整装置である輻射プレ
ート17a、+7b及び18a、18bが排ガスGの流
れ方向と略直交するように、かつ、その上流側表面が、
ノーズ部15.16に位置するビレットWの下流側面と
対向するようその取り付は角度を選択して配設されてい
る。上記各輻射プレート17a、17b、+8a、18
bは、耐熱性の高い、例えばセラミックスを通気性に冨
む形状、例えばハニカム(蜂の巣)状に成形焼成したり
、あるいはセラミックファイバーを綿状に成形焼成した
りしてなる板状体である。そして上側の輻射プレート1
7a、+8aは、幅は炉内幅と略等しく、高さは上部ノ
ーズ部15a、16a下面と被加熱材であるビレットW
との間隔より少し低い板状体であり、下側の輻射プレー
ト17b、18bは、幅は上側のものと等しく、高さは
下部ノーズ部15b、16bの上面と移動ビームIIの
下面との間隔より少し低い板状体である。
And on the inlet side of 16a, 16b, that is, on the downstream side in the flow direction of exhaust gas G, radiation plates 17a, +7b and 18a, 18b, which are the heat transfer product adjusting device of this embodiment, are arranged so as to be substantially perpendicular to the flow direction of exhaust gas G. , and its upstream surface is
The mounting angle is selected so as to face the downstream side of the billet W located at the nose portion 15, 16. Each of the above radiation plates 17a, 17b, +8a, 18
b is a plate-like body formed by molding and firing a highly heat-resistant ceramic into a highly breathable shape, such as a honeycomb shape, or by molding and firing ceramic fiber into a cotton-like shape. And the upper radiation plate 1
7a and +8a have a width approximately equal to the width inside the furnace, and a height between the lower surface of the upper nose portions 15a and 16a and the billet W which is the material to be heated.
The lower radiating plates 17b, 18b have the same width as the upper one, and the height is the distance between the upper surface of the lower nose portions 15b, 16b and the lower surface of the moving beam II. It is a slightly lower plate-like body.

次に本実施例の作用効果について説明する。Next, the effects of this embodiment will be explained.

本実施例装置においては、加熱帯8.均熱帯9のバーナ
6を点火し、予熱帯7のバーナ6を消火して行う、いわ
ゆる省エネルギー運転時において、予熱帯7.加熱帯8
間のノーズ部15での効果が大きいから、この部分につ
いて説明する。
In the device of this embodiment, heating zone 8. During so-called energy-saving operation, in which the burner 6 in the soaking zone 9 is ignited and the burner 6 in the preheating zone 7 is extinguished, the preheating zone 7. heating zone 8
Since the effect at the nose portion 15 in between is large, this portion will be explained.

この省エネルギー運転時には、予熱帯7は加熱帯8に比
べて著しく低温になっているから、従来の加熱炉では、
上述のように、ノーズ部15におけるビレットWへの伝
熱量は、加熱帯8側からの量が予熱帯7側からの量より
著しく多く、従ってビレットWの加熱帯8側部分の温度
が予熱帯7側部分の温度より高くなり、加熱帯8側に凸
状に湾曲してしまう問題があった。
During this energy-saving operation, the temperature of the preheating zone 7 is significantly lower than that of the heating zone 8, so in the conventional heating furnace,
As mentioned above, the amount of heat transferred to the billet W in the nose portion 15 from the heating zone 8 side is significantly larger than that from the preheating zone 7 side, and therefore the temperature of the heating zone 8 side portion of the billet W is lower than that of the heating zone 8 side. There was a problem in that the temperature of the heating zone 7 side became higher than that of the heating zone 8 side, and the heating zone 8 side was curved in a convex shape.

これに対して本実施例では、上、下部ノーズ部15a、
15bの入口部に輻射プレート17a。
On the other hand, in this embodiment, the upper and lower nose portions 15a,
A radiation plate 17a is provided at the inlet of 15b.

17bを配設しているから、これが高温の排ガスGによ
って加熱され、この輻射プレー)17a。
17b, it is heated by the high-temperature exhaust gas G, and this radiation plays) 17a.

17bからの輻射による伝熱量が予熱帯7からの伝%i
に加算され、そのため、加熱帯8からの伝熱量と均一化
され、その結果ビレットWが均一温度になって曲がりが
防止される。
The amount of heat transferred by radiation from 17b is transferred from preheating zone 7%i
Therefore, the amount of heat transferred from the heating zone 8 is equalized, and as a result, the temperature of the billet W becomes uniform and bending is prevented.

また、加熱帯8は均熱帯9より低温に設定されているか
ら、従来の加熱炉ではノーズ部16におい°ζも上記ノ
ーズ部15における場合と同様の傾向があり、ビレyト
Wの曲がりの問題があったが、本実施例ではこのノーズ
部16においても、輻射プレー1−18a、18bの作
用により伝熱量力9周整され、ビレットの曲がりを防止
できる。
In addition, since the heating zone 8 is set at a lower temperature than the soaking zone 9, in the conventional heating furnace, the temperature at the nose section 16 tends to be similar to that at the nose section 15, and the bending of the belay W is prevented. Although there was a problem, in this embodiment, even in the nose portion 16, the heat transfer force is adjusted by nine rounds by the action of the radiation plays 1-18a and 18b, and the billet can be prevented from bending.

また、この場合、輻射プレート17a、+7b及び18
a、18bは通気性に富んでいるから、この輻射プレー
トが排ガス抵抗となって炉圧に影習を与えることはほと
んどない。
Also, in this case, the radiation plates 17a, +7b and 18
Since portions a and 18b are highly permeable, these radiation plates hardly act as exhaust gas resistance and affect the furnace pressure.

このように、本実施例では、ノーズ部15.及びI6に
輻射プレート17a、17b及び18a。
In this way, in this embodiment, the nose portion 15. and radiant plates 17a, 17b and 18a at I6.

18bを配設したので、ビレットWへの下流側帯からの
伝熱量と上流側帯からの伝熱量とを均一化でき、ビレッ
トWの加熱品質を向上できるとともに、ビレットWの曲
がりを防止して操業の安定性を向上できる。
18b, the amount of heat transferred from the downstream side zone to the billet W and the amount of heat transferred from the upstream side zone to the billet W can be equalized, the heating quality of the billet W can be improved, and the billet W can be prevented from bending to improve operation. Stability can be improved.

また、本実施例では伝熱量の均一化に際し、従来のよう
な下流側帯の燃焼量を必要以上に増大させる必要もなく
、従ってその分排ガス損失を低減して燃料原単位を向上
できる。
Furthermore, in this embodiment, when the amount of heat transfer is made uniform, there is no need to increase the amount of combustion in the downstream side zone more than necessary as in the conventional case, and therefore, the exhaust gas loss can be reduced accordingly and the fuel consumption rate can be improved.

なお、上記実施例では、ノーズ部のト側及び下側の両方
に輻射プレートを配設したが、本発明では、下側の輻射
プレートは必ずしも必要ではなく、少なくとも上側の輻
射プレートを配設すればよい。
In the above embodiment, the radiation plate is provided on both the top side and the bottom side of the nose part, but in the present invention, the lower radiation plate is not necessarily required, and at least the upper radiation plate is provided. Bye.

このようにするのは、燃焼排ガスはビレットWの上側部
分をより多く流れるから、この上側部分に輻射プレート
を配設するのが効果的だからである。
The reason for doing this is that since more combustion exhaust gas flows through the upper part of the billet W, it is effective to arrange the radiation plate in this upper part.

また、上記実施例では、ウオーキングビーム式ビレット
加熱炉の場合について説明したが、本発明は、ウオーキ
ングハース式等の連続式加熱炉において、ビレットに限
らず、スラブ、ブルーム等を加熱する場合にも勿論適用
できる。
Further, in the above embodiment, the case of a walking beam type billet heating furnace was explained, but the present invention is applicable not only to billets but also to heating slabs, blooms, etc. in a continuous type heating furnace such as a walking hearth type. Of course it can be applied.

〔発明の効果〕〔Effect of the invention〕

以上のように本発明に係る加熱炉の伝熱量調整装置によ
れば、ノーズ部の入口側の少なくとも上部に、耐払性及
び通気性の良好な輻射部材を配設じたので、被加熱材を
均一に加熱して加熱品質を向りできるとともに、曲がり
を防止して操業の安定性を向上できる効果があり、かつ
燃料原単位を向上できる効果がある。
As described above, according to the heat transfer amount adjusting device for a heating furnace according to the present invention, since the radiant member with good blowout resistance and air permeability is disposed at least in the upper part of the nose portion on the inlet side, the heated material can be heated. It has the effect of uniformly heating and improving heating quality, preventing bending and improving operational stability, and improving fuel consumption.

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

第1図は本発明の−・実施例による加り九炉の伝熱堅調
整装置を示す概略構成図、第2図は上記実施例装置が適
用された加熱炉の全体構成図である。 図において、■は加熱炉、7.8.9はそれぞれ子軌帯
、加熱帯、均熱帯(温度制御■帯)、15゜16はノー
ズ部、15a、+6aは上部ノーズ部、15b、16b
は下部ノーズ部、17a、17b。 18=、+8bは輻射プレート(輻射部材)、Gは燃焼
排ガス、Wはビレット(被加熱材)である。
FIG. 1 is a schematic diagram showing a heat transfer adjustment device for a heating furnace according to an embodiment of the present invention, and FIG. 2 is an overall configuration diagram of a heating furnace to which the device of the above embodiment is applied. In the figure, ■ is a heating furnace, 7, 8, and 9 are respectively a child orbital zone, a heating zone, and a soaking zone (temperature control ■ zone), 15° and 16 are nose parts, 15a, +6a are upper nose parts, 15b, 16b
are lower nose portions, 17a and 17b. 18=, +8b is a radiation plate (radiation member), G is combustion exhaust gas, and W is a billet (heated material).

Claims (2)

【特許請求の範囲】[Claims] (1)長手方向に複数の温度制御帯に分割され、各帯の
境界部分に他の部分より炉内高さの低いノーズ部が形成
され、被加熱材を長手方向に搬送しつつ加熱する連続式
加熱炉において、上記ノーズ部の入口側の少なくとも上
部に、耐熱性及び通気性の高い板状の輻射部材を炉幅方
向に、かつ燃焼排ガスの流れ方向と略直交するように配
設したことを特徴とする加熱炉の伝熱量調整装置。
(1) It is divided into multiple temperature control zones in the longitudinal direction, and a nose section with a lower height inside the furnace than other sections is formed at the boundary of each zone, and the material to be heated is continuously heated while being conveyed in the longitudinal direction. In the type heating furnace, a plate-shaped radiant member with high heat resistance and air permeability is arranged at least in the upper part of the inlet side of the nose part in the width direction of the furnace and substantially perpendicular to the flow direction of the combustion exhaust gas. A heating furnace heat transfer amount adjustment device characterized by:
(2)上記ノーズ部が、天井壁を下方に凹設してなる上
部ノーズ部と、床壁を上方に凹設してなる下部ノーズ部
とからなり、該下部ノーズ部、上部ノーズ部の各々の入
口側に上記輻射部材を配設したことを特徴とする特許請
求の範囲第1項記載の加熱炉の伝熱量調整装置。
(2) The nose portion consists of an upper nose portion formed by recessing the ceiling wall downward and a lower nose portion formed by recessing the floor wall upward, and each of the lower nose portion and the upper nose portion 2. The heat transfer amount adjusting device for a heating furnace according to claim 1, wherein the radiant member is disposed on the inlet side of the heating furnace.
JP29934885A 1985-12-27 1985-12-27 Regulator for quantity of heat transfer of heating furnace Pending JPS62155488A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29934885A JPS62155488A (en) 1985-12-27 1985-12-27 Regulator for quantity of heat transfer of heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29934885A JPS62155488A (en) 1985-12-27 1985-12-27 Regulator for quantity of heat transfer of heating furnace

Publications (1)

Publication Number Publication Date
JPS62155488A true JPS62155488A (en) 1987-07-10

Family

ID=17871385

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29934885A Pending JPS62155488A (en) 1985-12-27 1985-12-27 Regulator for quantity of heat transfer of heating furnace

Country Status (1)

Country Link
JP (1) JPS62155488A (en)

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