JPH0317228A - Continuous fluidized bed type heating furnace - Google Patents

Continuous fluidized bed type heating furnace

Info

Publication number
JPH0317228A
JPH0317228A JP15155189A JP15155189A JPH0317228A JP H0317228 A JPH0317228 A JP H0317228A JP 15155189 A JP15155189 A JP 15155189A JP 15155189 A JP15155189 A JP 15155189A JP H0317228 A JPH0317228 A JP H0317228A
Authority
JP
Japan
Prior art keywords
heating furnace
furnace
fluidized bed
heated
materials
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
JP15155189A
Other languages
Japanese (ja)
Inventor
Masao Hattori
雅夫 服部
Yoshiki Oyabu
大藪 芳樹
Shuichi Kishida
岸田 修一
Akio Hamataka
浜高 昭夫
Tatsu Fukuda
福田 達
Hidemitsu Takenoshita
竹野下 秀満
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.)
JFE Steel Corp
Komatsu Ltd
Toho Gas Co Ltd
Original Assignee
Komatsu Ltd
Kawasaki Steel Corp
Toho Gas 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 Komatsu Ltd, Kawasaki Steel Corp, Toho Gas Co Ltd filed Critical Komatsu Ltd
Priority to JP15155189A priority Critical patent/JPH0317228A/en
Publication of JPH0317228A publication Critical patent/JPH0317228A/en
Pending legal-status Critical Current

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  • Heat Treatments In General, Especially Conveying And Cooling (AREA)

Abstract

PURPOSE:To efficiently heat materials to be heated and to prevent the generation of skid marks by providing means tor sending the exhaust gas used in the fluidized bed heating furnace to an adjacent preheating furnace and changing the positions of the materials to be heated in this heating furnace. CONSTITUTION:The preheating furnace 1 is installed adjacently via a heat insulating wall 9 to the wall surface on one side of the fluidized bed heating furnace 2 and the materials 5 to be heated are continuously charged from the preheating furnace 1 via a ventilation hole 10 into the heating furnace 2. The materials 5 are successively transported in a direction E by stationary walking beams 6A and movable walking beams 6B in the beating furnace 2 and are subjected to the heating treatment by burners 42 provided at several points. The hot gas of the heating furnace 2 flows in a direction H at this time and enters the preheating furnace 1 via the ventilation hole 10 to preheat the materials 5. A pusher 33 is provided, via an insertion hole 22, on the side wall surface 21 of the heating furnace 2, which surface faces the side wall surface 9 adjacent to the preheating furnace 1 so that the materials 5 can be changed in position by slightly pushing the material in a direction P. The thermal efficiency is improved in this way and the generation of the skid marks in the materials 5 is prevented.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は,鋼材その他の金属材料からなる被加熱材を連
続的にかつ熱効率よく加熱処理できる.連続流動層式加
熱炉に関する. 〔従来技術〕 従来,ウォーキングビームを備えた流動層加熱炉として
は.第4図及び第5図に示すごとく,断熱壁9と.燃料
供給管8と,該燃籾供給管8を連結した流動床加熱装置
7と.該流動床加熱装置7に並設されたウオーキングビ
ーム6A,6Bとよりなるものが知られている. 上記燃料供給管8は,上記流動床加熱装置7の下方に配
管され,また該流動床jJn熱装置7は被加熱材5の搬
送方向に沿って配設されている.また、燃料供給管8は
,炉の長手方向に沿って複数本並列されている. また.上記ウォーキングビーム6A,6Bは,被加熱材
5の搬送方向に沿って上記流動床加熱装置7と併設され
ている。
[Detailed Description of the Invention] [Industrial Application Field] The present invention can heat-treat materials made of steel or other metal materials continuously and thermally efficiently. Concerning continuous fluidized bed heating furnace. [Prior art] Conventionally, a fluidized bed heating furnace equipped with a walking beam. As shown in FIGS. 4 and 5, the insulation wall 9. A fuel supply pipe 8, a fluidized bed heating device 7 to which the fuel supply pipe 8 is connected. A device comprising walking beams 6A and 6B installed in parallel with the fluidized bed heating device 7 is known. The fuel supply pipe 8 is arranged below the fluidized bed heating device 7, and the fluidized bed heating device 7 is arranged along the conveyance direction of the material to be heated 5. Further, a plurality of fuel supply pipes 8 are arranged in parallel along the longitudinal direction of the furnace. Also. The walking beams 6A, 6B are installed along with the fluidized bed heating device 7 along the conveyance direction of the material to be heated 5.

しかして5上記流動層加熱炉においては,上記被加熱材
5はウオーキングビーム6A.,6Bのうち可動ビーム
6Bの作動により.搬送される.また,上記流動床加熱
装置7には,上記燃料供給管8を介して燃料ガスが供給
される.そして,この燃料ガスの燃焼熱により上記被加
熱材5はウォーヰングビーム6上で加熱されながら,加
熱もしくは焼鈍等の熱処理が行われる。
Therefore, in the fluidized bed heating furnace 5, the material to be heated 5 is connected to the walking beam 6A. , 6B due to the operation of the movable beam 6B. Transported. Furthermore, fuel gas is supplied to the fluidized bed heating device 7 via the fuel supply pipe 8. Then, the material to be heated 5 is heated on the walking beam 6 by the combustion heat of the fuel gas, and heat treatment such as heating or annealing is performed.

〔解決すべき問題点] しかしながら.上記従来の加熱炉においては7次の問題
点がある. 即ち,上記炉においては.破加熱材5は流動床加熱装置
7からのガス燃焼による輻射熱と該輻射熱の断熱壁9か
らの反射熱によって加熱される.そのため.被加熱材5
はウォーキングビーム6の上面6lと当接している部分
(第6図)を除き,上記輻射熱によって周囲から直接加
熱される。しかし,ウォーキングビーム6と当接してい
る被加熱材5の下面5lには輻射熱が直接当たらないた
め5強く加熱されない.その結果,この下面5lには.
第6図に示すごとく,スキッドマーク55と称する加熱
ムラを生じ,被加熱材の商品価値を低下させる. また.上記従来の炉においては,排ガスはガス排気筒9
lより放出され.排ガスのエネルギーは十分活用されて
いない。
[Problems to be solved] However. The above conventional heating furnace has the following 7 problems. That is, in the above furnace. The heating material 5 is heated by the radiant heat from the fluidized bed heating device 7 due to gas combustion and the reflected heat of the radiant heat from the heat insulating wall 9. Therefore. Heated material 5
is heated directly from the surroundings by the radiant heat, except for the portion that is in contact with the upper surface 6l of the walking beam 6 (FIG. 6). However, since the radiant heat does not directly hit the lower surface 5l of the heated material 5 that is in contact with the walking beam 6, it is not heated strongly. As a result, this lower surface 5l.
As shown in Figure 6, heating unevenness called skid marks 55 occurs, reducing the commercial value of the heated material. Also. In the above conventional furnace, the exhaust gas is
Released from l. The energy of exhaust gas is not fully utilized.

本発明は,かかる従来の間理点に鑑みてなされたもので
.被加熱材5のスキンドマークを解消し,かつ被加熱材
5を連続的に効率よく加熱処理できる,連Vt?JL動
層式加熱炉を提供しようとするものである. (課題の解決手段) 本発明は.予熱炉と.ウォーキングビームを備えた流動
層加熱炉とからなる加熱炉であって,上記予熱炉と流動
層加熱炉は,少なくともl側壁面において当接した状態
で隣接し,両炉においては被加熱材の搬送方向と対向す
る方向に熱ガス流を送ると共に.上記予熱炉内に送る熱
ガスは上記流動層加悲炉において使用した排ガスであっ
て,また該流動層加熱炉には上記被加熱材が上記ウォー
キングビームの上面と当接する位置を転換するための位
置変換装置を配設したことを特徴とする連続流動層式加
熱炉にある. 本発明において.上記予熱炉は.iJ!L動層加熱炉に
被加熱材を挿入する前に.予め被加熱材を一定温度に加
熱しておくための炉である。
The present invention has been made in view of such conventional logic points. A continuous Vt? that eliminates skin marks on the heated material 5 and allows continuous and efficient heat treatment of the heated material 5. This project aims to provide a JL fluidized bed heating furnace. (Means for solving the problem) The present invention is as follows. Preheating furnace. A heating furnace consisting of a fluidized bed heating furnace equipped with a walking beam, the preheating furnace and the fluidized bed heating furnace are adjacent to each other with at least one side wall surface in contact with each other, and in both furnaces, the material to be heated is transported. As well as sending a stream of hot gas in the opposite direction. The hot gas sent into the preheating furnace is the exhaust gas used in the fluidized bed heating furnace. This continuous fluidized bed heating furnace is characterized by being equipped with a position changing device. In the present invention. The above preheating furnace is. iJ! L Before inserting the material to be heated into the moving bed heating furnace. This is a furnace for preheating the material to be heated to a constant temperature.

また.上記ウォーキングビームは,例えば偏心カムによ
る作動で上下駆動する移動ビームと.これに交互に配設
された固定ビームとの上で,被加熱物を間歇的に移動さ
せるための装置である(第2図参照). また,上記流動層加熱炉は.燃料供給管と.該燃料供給
管を連結し,また断熱壁によって囲まれたia床加熱部
と,該流動床加熱部に沿って被加熱材の搬送方向に並設
した上記ウオーキングビームとよりなる.そして,該炉
は,被加熱材の加熱もしくは焼鈍等を行なうための熱処
理炉である.また.上記少なくとも1側璧面とは.上記
予熱炉と流動層加熱炉との1つの側壁,即ち最小限1つ
の側壁面において.その一部又は全部の面という意味で
ある. また.上記被加熱材としては,鋼材.その他の金属材料
からなるビレット,ブルーム,スラブパイプ 棒状物等
がある. また,上記位置変換装置とは.上記ウォーキングビーム
の上面と当接する被加熱材の下面の位置を転換するため
の装置である.例えば該.ウォーキングビーム上で被加
熱材を,その長手方向に移動するためのプンシャー,該
被加熱材に一定の回動(例えば90度)を与えるための
回転装置等である。
Also. The walking beam mentioned above is a moving beam that is driven up and down by, for example, an eccentric cam. This is a device for intermittently moving the object to be heated on the fixed beams arranged alternately (see Figure 2). In addition, the fluidized bed heating furnace mentioned above. Fuel supply pipe. It consists of an ia bed heating section to which the fuel supply pipes are connected and surrounded by a heat insulating wall, and the above-mentioned walking beams arranged in parallel in the conveyance direction of the material to be heated along the fluidized bed heating section. The furnace is a heat treatment furnace for heating or annealing the material to be heated. Also. What does the above-mentioned at least one side wall mean? At one side wall of the preheating furnace and the fluidized bed heating furnace, that is, at least one side wall surface. It means part or all of it. Also. The above heated material is steel. There are billets, blooms, slab pipes, rods, etc. made of other metal materials. Also, what is the above position conversion device? This is a device for changing the position of the bottom surface of the heated material that comes into contact with the top surface of the walking beam. For example, These include a puncher for moving the material to be heated in its longitudinal direction on the walking beam, a rotating device for giving a certain degree of rotation (for example, 90 degrees) to the material to be heated, and the like.

〔作用及び効果〕[Action and effect]

本発明にかかる加熱炉においては,予熱炉と流動層加熱
炉は,少なくとも1側壁面において当接した状態で隣接
している。そのため,両炉の断熱壁から熱が放熱頃失す
る面積を減少させることができる.したがって,木熱処
理炉により放熱用失を低減し,省エネルギ品を図ること
ができる。
In the heating furnace according to the present invention, the preheating furnace and the fluidized bed heating furnace are adjacent to each other so as to be in contact with each other on at least one side wall surface. Therefore, the area where heat is lost during heat radiation from the insulated walls of both furnaces can be reduced. Therefore, the wood heat treatment furnace can reduce heat loss and produce energy-saving products.

また.上記両炉においては.被):U熱材の搬送方向と
対向する方向に熱ガスを流すので.加熱処理の熱効率に
優れる。さらに,上記予熱炉に送る加熱処理用の熱ガス
は,上記流動層加熱炉において使用した排ガスである。
Also. In both of the above furnaces. ): U Because the hot gas flows in the direction opposite to the direction in which the heated material is transported. Excellent thermal efficiency in heat treatment. Furthermore, the hot gas for heat treatment sent to the preheating furnace is the exhaust gas used in the fluidized bed heating furnace.

そのため,熱効率が一段と向上し.省エネルギーをより
図ることができる。
Therefore, thermal efficiency is further improved. Energy saving can be further achieved.

また.上記流動層加熱炉においては,位置変換装置を配
設するため,被加熱材はウオーキングビームと当接する
面が転換され,スキノドマークが生ずることはない. したがって.本発明によれば,被加熱材を連続的にかつ
熱効率よく加熱処理できる.連続流動層式加熱炉を提供
することができる. 〔実施例) 本発明の実施例にかかる加熱炉につき,第l図〜第3図
を用いて説明する. 即ち2本例の加熱炉は,第1図及び第2図に示すごとく
.予熱炉1と,ウォーキングビーム6A6Bを備えた流
動層加熱炉2とからなる.そして.上記予熱炉1と流動
層加熱炉2とは該流動層加熱炉2の長平方向の1側壁面
の1部において,上記予熱炉lのl側壁面と当接した状
態で隣接している。また,流動層加熱炉2においては,
被加熱材5の搬送方向Eと対向する方向Hに熱ガス41
を送るよう,バーナー42を,数カ所に設ける.また,
上記バーナー42には,燃料ガス40(空気K1天然ガ
スGの混合ガス)が供給される. また,上記予熱炉lには1上記流動層加熱炉2と隣接す
る断熱壁9のl側壁面に通風穴IOを設ける.該通風穴
10は.該流動層加熱炉2内において使用した排ガスが
送入されるためのものである.また,該通風穴10は5
被加熱材5を予熱炉1より流動層加熱炉2へ連続して搬
送するための通路を兼ねる。
Also. In the above-mentioned fluidized bed heating furnace, since a position changing device is installed, the surface of the material to be heated that comes into contact with the walking beam is changed, and no skid marks occur. therefore. According to the present invention, the material to be heated can be heat-treated continuously and thermally efficiently. A continuous fluidized bed heating furnace can be provided. [Example] A heating furnace according to an example of the present invention will be explained using FIGS. 1 to 3. That is, the heating furnaces of the two examples are as shown in Figures 1 and 2. It consists of a preheating furnace 1 and a fluidized bed heating furnace 2 equipped with a walking beam 6A6B. and. The preheating furnace 1 and the fluidized bed heating furnace 2 are adjacent to each other in a state in which a portion of one side wall surface in the longitudinal direction of the fluidized bed heating furnace 2 is in contact with the l side wall surface of the preheating furnace I. In addition, in the fluidized bed heating furnace 2,
The hot gas 41 is directed in the direction H opposite to the conveying direction E of the material to be heated 5.
Burners 42 are installed at several locations to send the water. Also,
The burner 42 is supplied with a fuel gas 40 (a mixed gas of air K1 and natural gas G). Further, in the preheating furnace 1, a ventilation hole IO is provided on the 1 side wall surface of the heat insulating wall 9 adjacent to the fluidized bed heating furnace 2. The ventilation hole 10 is. This is for feeding the exhaust gas used in the fluidized bed heating furnace 2. In addition, the ventilation hole 10 has 5
It also serves as a passage for continuously conveying the material to be heated 5 from the preheating furnace 1 to the fluidized bed heating furnace 2.

また,上記予熱炉lには,上記通風穴10と対向する断
熱壁9の側壁面に,被加熱材5を流動層加熱炉2内へ送
り出すためのブッシャ−3l及びその挿入穴l1を設け
る。また,該予熱炉1には,該挿入穴11を設けた同一
側壁面における他端部近傍にプッシャー32及びその挿
入穴12を設ける.該挿入穴12は,被加熱材5を予熱
炉1内に投入するためのものである。また,該挿入穴1
2に隣接してυ1ガス排出用の煙突l5を設ける.また
,上記流動層加熱炉2には.上記予熱炉lと隣接する側
壁面と対面する側壁面2lにブノシャー33,挿入穴2
2を設ける。該挿入穴22は位置変換装置としての被加
熱材5をP方向に若干押すためのものである。また,該
流動層加熱炉2には,該挿入穴22と同一側壁面21側
における端部近傍に,被加熱材5の取出し穴23を設け
る。
Further, the preheating furnace 1 is provided with a busher 3l and its insertion hole 11 for feeding the material to be heated 5 into the fluidized bed heating furnace 2 on the side wall surface of the heat insulating wall 9 facing the ventilation hole 10. Further, the preheating furnace 1 is provided with a pusher 32 and its insertion hole 12 near the other end on the same side wall surface where the insertion hole 11 is provided. The insertion hole 12 is for inserting the material to be heated 5 into the preheating furnace 1. In addition, the insertion hole 1
A chimney l5 for discharging the υ1 gas is installed adjacent to the chimney l5. In addition, the fluidized bed heating furnace 2 includes: A bunosher 33 and an insertion hole 2 are provided on the side wall surface 2l facing the side wall surface adjacent to the preheating furnace l.
2 will be provided. The insertion hole 22 is for slightly pushing the heated material 5 as a position changing device in the P direction. Further, the fluidized bed heating furnace 2 is provided with a hole 23 for taking out the material to be heated 5 near the end on the same side wall surface 21 side as the insertion hole 22.

また,該流動層加熱炉2には,該取出し穴23と対向す
る側壁面25の端部近傍に.ブッシャ−34及びその挿
入穴24を設ける.該プッシャー34は,熱処理を終わ
った被加熱材を取り出すためのものである. また,該流動層加熱炉2には,第1図及び第2図に示す
ごとく,炉床内においてウォーキングビーム6A,6B
及び流動床加熱部71を配設する.即ち.該ウォーキン
グビームは,固定ビーム6Aと移動ビーム6Bとを交互
に被加熱材5の搬送方向Eに沿って配設する。また,該
固定ビーム6A及び移動ビーム6Bの上面61には被加
熱材載置用の凹部610を設ける。また,該ウオーキン
グビーム6A,6Bの下方においては,分散板73を被
加熱材5の殿送方向に沿って配設する.また,該流動床
加熱部7lとウォーキングビーム6A,6Bが隣接する
部分にはサンドシール72を配設する。即ち.上記分散
板73の端部において.立設した凹状の溝壁にウォーキ
ングビーム6Bより垂設したシール板を嵌拝する。なお
.上記予熱炉1においては,該流動層加熱炉2と同様に
ウォーキングビーム6A,6Bを配設する。
Further, in the fluidized bed heating furnace 2, there is a hole near the end of the side wall surface 25 facing the takeout hole 23. A busher 34 and its insertion hole 24 are provided. The pusher 34 is for taking out the material to be heated after the heat treatment. The fluidized bed heating furnace 2 also includes walking beams 6A and 6B in the hearth, as shown in FIGS. 1 and 2.
and a fluidized bed heating section 71. That is. The walking beam has fixed beams 6A and moving beams 6B arranged alternately along the conveyance direction E of the material to be heated 5. Further, a recess 610 for placing a heated material is provided on the upper surface 61 of the fixed beam 6A and the movable beam 6B. Further, below the walking beams 6A and 6B, a dispersion plate 73 is arranged along the direction in which the material to be heated 5 is fed. Furthermore, a sand seal 72 is provided at a portion where the fluidized bed heating section 7l and the walking beams 6A, 6B are adjacent to each other. That is. At the end of the dispersion plate 73. A seal plate hanging down from the walking beam 6B is fitted into the upright concave groove wall. In addition. In the preheating furnace 1, walking beams 6A and 6B are provided similarly to the fluidized bed heating furnace 2.

本例の加熱炉は,上記のごとく構威されているので,次
の作用効果を有する. 即ち.本例の加熱炉においては,予熱炉1と流動層加熱
炉2とは1側壁面において当接した状態で隣接している
ので1両炉の断熱壁9から放熱損失する面積が滅少する
。そのため.省熱エネルギーを図ることができる。
Since the heating furnace of this example is constructed as described above, it has the following effects. That is. In the heating furnace of this example, the preheating furnace 1 and the fluidized bed heating furnace 2 are adjacent to each other with one side wall surface in contact with each other, so that the area for heat radiation loss from the heat insulating wall 9 of both furnaces is reduced. Therefore. It is possible to save heat energy.

また,上記両炉においては,被加熱材5の搬送方向Eと
対向する方向Hに,熱ガス4lを流すので.加熱ガスの
熱効率に優れる。さらに.上記子熱炉lに送る排ガスは
.上記流動層Ull熱炉2において使用した例えば約s
 o o ”c以上のものである。
In addition, in both of the above furnaces, 4 liters of hot gas is flowed in the direction H opposite to the conveying direction E of the material to be heated 5. Excellent thermal efficiency of heating gas. moreover. The exhaust gas sent to the sub-heating furnace I is as follows. For example, about s used in the fluidized bed Ull thermal furnace 2
o o ”c or more.

そのため,熱効率が一層向上し,省エネルギーを達威す
ることができる. また,上記流動層加熱炉2においては位置変換装置とし
てのブノシャ−33を配設しているため被加熱材5とウ
ォーキングビームの上面61と当接する部分を変更する
ことができる.それ故.被加熱材5にはスキッドマーク
が生ずることがない.したがって,本例によれば,被加
熱材5を連続的にかつ熱効率よく加熱処理でき,かつス
キッドマークを生ずることがない.連続流動層式加熱炉
を提供することができる.
Therefore, thermal efficiency is further improved and energy savings can be achieved. Furthermore, since the fluidized bed heating furnace 2 is provided with a bunosher 33 as a position changing device, the portion where the material to be heated 5 contacts the upper surface 61 of the walking beam can be changed. Therefore. Skid marks do not occur on the heated material 5. Therefore, according to this example, the material to be heated 5 can be heated continuously and thermally efficiently, and skid marks are not generated. A continuous fluidized bed heating furnace can be provided.

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

第1図〜第3図は本発明の実施例にかかる加熱炉を示し
.第1図はその斜視図.第2図は流動層加熱炉の一部切
欠斜視図,第3図はサンドシール部の一部拡大斜視図,
第4図〜第6図は従来の流動層加熱炉を示し,第4図は
その側面断面図,第5図はその正面断面図,第6図はス
キッドマーク形底部の説明図である. 2・・・流動層加熱炉, 31〜34・ ・・フ゛・冫シャー 40・・・燃料ガス 4l・・・熱ガス, 42・・・バーナー 5・・・被加熱材, 55・・・スキッドマーク 6A  6B・・・ウォーキングビーム7・・・流動床
加熱部 8・・・燃料供給管, 9・・・断熱壁,
1 to 3 show a heating furnace according to an embodiment of the present invention. Figure 1 is a perspective view. Figure 2 is a partially cutaway perspective view of the fluidized bed heating furnace, Figure 3 is a partially enlarged perspective view of the sand seal section,
Figures 4 to 6 show a conventional fluidized bed heating furnace, with Figure 4 being a side sectional view, Figure 5 being a front sectional view, and Figure 6 being an explanatory view of the skid mark shaped bottom. 2... Fluidized bed heating furnace, 31-34... Film shear 40... Fuel gas 4 liters... Hot gas, 42... Burner 5... Material to be heated, 55... Skid Mark 6A 6B...Walking beam 7...Fluidized bed heating section 8...Fuel supply pipe, 9...Insulating wall,

Claims (1)

【特許請求の範囲】[Claims] 予熱炉と、ウォーキングビームを備えた流動層加熱炉と
からなる加熱炉であって、上記予熱炉と流動層加熱炉は
、少なくとも1側壁面において当接した状態で隣接し、
両炉においては被加熱材の搬送方向と対向する方向に熱
ガス流を送ると共に、上記予熱炉内に送る熱ガスは上記
流動層加熱炉において使用した排ガスであって、また該
流動層加熱炉には上記被加熱材が上記ウォーキングビー
ムの上面と当接する位置を転換するための位置変換装置
を配設したことを特徴とする連続流動層式加熱炉。
A heating furnace consisting of a preheating furnace and a fluidized bed heating furnace equipped with a walking beam, wherein the preheating furnace and the fluidized bed heating furnace are adjacent to each other in contact with each other on at least one side wall surface,
In both furnaces, a hot gas flow is sent in a direction opposite to the conveying direction of the material to be heated, and the hot gas sent into the preheating furnace is the exhaust gas used in the fluidized bed heating furnace, and the hot gas is the exhaust gas used in the fluidized bed heating furnace. The continuous fluidized bed heating furnace is characterized in that a position changing device for changing the position where the material to be heated comes into contact with the upper surface of the walking beam is provided.
JP15155189A 1989-06-14 1989-06-14 Continuous fluidized bed type heating furnace Pending JPH0317228A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15155189A JPH0317228A (en) 1989-06-14 1989-06-14 Continuous fluidized bed type heating furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15155189A JPH0317228A (en) 1989-06-14 1989-06-14 Continuous fluidized bed type heating furnace

Publications (1)

Publication Number Publication Date
JPH0317228A true JPH0317228A (en) 1991-01-25

Family

ID=15520996

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15155189A Pending JPH0317228A (en) 1989-06-14 1989-06-14 Continuous fluidized bed type heating furnace

Country Status (1)

Country Link
JP (1) JPH0317228A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020114268A1 (en) * 2018-12-04 2020-06-11 苏州中门子工业炉科技有限公司 Dual-station waste heat utilization and automatic production line for bearing steel wire coil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020114268A1 (en) * 2018-12-04 2020-06-11 苏州中门子工业炉科技有限公司 Dual-station waste heat utilization and automatic production line for bearing steel wire coil

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