JP2921381B2 - Electric furnace with rotating pre-tropics - Google Patents
Electric furnace with rotating pre-tropicsInfo
- Publication number
- JP2921381B2 JP2921381B2 JP35544293A JP35544293A JP2921381B2 JP 2921381 B2 JP2921381 B2 JP 2921381B2 JP 35544293 A JP35544293 A JP 35544293A JP 35544293 A JP35544293 A JP 35544293A JP 2921381 B2 JP2921381 B2 JP 2921381B2
- Authority
- JP
- Japan
- Prior art keywords
- discharge
- electric furnace
- zone
- melted
- rotating
- 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.)
- Expired - Fee Related
Links
Landscapes
- Furnace Details (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は被溶解物の回転予熱帯
を備えた電気炉に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electric furnace provided with a rotating pre-tropical zone for a material to be melted.
【0002】[0002]
【従来の技術】電気炉における被溶解物の予熱には、従
来、例えば図7に示すような装置が用いられてきた。図
7において鋼屑等の被溶解物8は装入用コンベア21に
より予熱帯20に運ばれ、電気炉本体1内での溶解、精
錬に際して電気炉本体1より発生する高温の排ガスで予
熱される。予熱された鋼屑等の被溶解物8はコンベア2
1により予熱帯20から電気炉本体1に排出される。
尚、図7において、1aは排ガス排出口、4は排ガス吸
引用ファンである。 2. Description of the Related Art Preheating of an object to be melted in an electric furnace is not easy.
Heretofore, for example, an apparatus as shown in FIG. 7 has been used. The lysate 8 such as steel scrap 7 is conveyed to the preheating zone 20 by instrumentation necessity conveyor 21, dissolved in an electric furnace main assembly 1 is preheated with hot exhaust gas generated from an electric furnace body 1 during refining . The material 8 to be melted, such as preheated steel chips, is
1 discharges from the pre-tropical zone 20 to the electric furnace main body 1.
In FIG. 7, reference numeral 1a denotes an exhaust gas outlet, and 4 denotes an exhaust gas suction port.
I'm a quote fan.
【0003】[0003]
【発明が解決しようとする課題】ところで、図7の装置
ではコンベア21で被溶解物8を予熱帯20内に運ぶた
め、予熱帯20内での被溶解物8の詰まり防止から、被
溶解物8の充填率を低くしなければならなかった。従っ
て、予熱帯20の天井壁と被溶解物8の表層面とにはか
なりの隙間ができ、ここを高温の排ガスが通過するの
で、被溶解物8との熱交換の効率が50%程度と低く、
被溶解物8の充分な予熱効果が得られなかった。本発明
はこのような事情に鑑みなされたもので、その目的は、
電気炉本体から発生する排ガスにより被溶解物を効率良
く予熱することのできる電気炉を提供することである。 In the apparatus shown in FIG. 7, the conveyed material 8 is conveyed into the pre-tropical zone 20 by the conveyor 21, so that the clogging of the dissolved object 8 in the pre-tropical zone 20 is prevented. 8 had to be reduced. Follow
The ceiling wall of the pre-tropical zone 20 and the surface of the material 8
There are gaps where high-temperature exhaust gas passes
Thus, the efficiency of heat exchange with the material to be melted 8 is as low as about 50%,
A sufficient preheating effect of the material to be melted 8 was not obtained. The present invention
Has been made in view of these circumstances, and its purpose is to
Efficient removal of substances to be dissolved by exhaust gas generated from the electric furnace body
An object of the present invention is to provide an electric furnace which can be preheated.
【0004】[0004]
【課題を解決するための手段及び作用】Means and Action for Solving the Problems
上記課題を解決Solving the above issues
するための本発明によるアーク式電気炉は、電気炉本体The electric arc furnace according to the present invention for performing
の排ガス排出口と排ガス吸引用ファンとの間に、被溶解Between the exhaust gas outlet of exhaust gas and the fan for exhaust gas suction
物を予熱する予熱帯を備えた電気炉において、前記予熱An electric furnace having a pre-tropical zone for pre-heating an object;
帯が、電気炉本体の排ガス排出口に開口する排出帯と、A discharge band, which is open to an exhaust gas discharge port of the electric furnace body,
この排出帯と接合し、中心を軸として回転自在な回転筒Rotating cylinder that is rotatable about the center by joining this discharge zone
と、この回転筒と接合し、被溶解物の流れ方向の上流側And this rotary cylinder, and the upstream side in the flow direction of the material to be melted
に被溶解物の装入口を有する装入帯とからなり、前記回And a charging zone having a charging port for the material to be melted therein.
転筒が被溶解物の装入口側を上部として水平面に対してThe rolling cylinder is on the horizontal surface with the inlet side of the melt
傾斜しており、回転筒が回転することで、回転筒内に被It is inclined, and the rotating cylinder rotates,
溶解物が充填されることを特徴とするものである。そしIt is characterized by being filled with a melt. Soshi
て、前記排出帯には、被溶解物を電気炉本体内に排出すIn the discharge zone, the material to be melted is discharged into the electric furnace body.
るために、コンベアやプッシャー等の独立した排出機構Independent discharge mechanism such as conveyor and pusher for
を設けることが好ましい。Is preferably provided.
【0005】以下、本発明を実施例に対応する図1、図
2によって説明する。電気炉本体1の排ガス排出口1a
と排ガス吸引用ファン4との間に、被溶解物8を予熱す
る予熱帯Aを備えた電気炉において、予熱帯Aは、被溶
解物8の装入口6側を上部として水平面に対して傾斜
し、かつ中心を軸として回転自在な回転筒3と、一方を
電気炉本体1と接合し、他方を回転筒3に接合する排出
帯2と、被溶解物8の流れの上流側に被溶解物8の装入
口6を有し、回転筒3と接する装入帯5とよりなってい
る。 Hereinafter, the present invention will be described with reference to FIGS. 1 and 2 corresponding to an embodiment. Flue gas exhaust outlet 1a of the electric furnace body 1
An electric furnace having a pre-tropical zone A for preheating the material to be melted 8 between the gas and the exhaust gas suction fan 4 , the pre-tropical zone A is inclined with respect to a horizontal plane with the charging port 6 side of the material to be melted 8 as an upper portion. and, and a rotatable rotary cylinder 3 to the center as an axis, and joined to the electric furnace body 1 one, and a discharge zone 2 for joining the other to the rotary cylinder 3, the dissolution on the upstream side of the flow of the melt 8 It has a charging port 6 for the object 8 and a charging band 5 in contact with the rotary cylinder 3.
【0006】装入口6より装入用コンベア9で装入され
た被溶解物8は自重で回転筒3に入る。この回転筒3は
中心を軸として回転している。被溶解物8は回転筒3内
でその回転に伴って上部に持ち上げらながら回転筒3内
に下流に移動しながら充填される。図2はこの充填され
ていく状況を示したもので、以下に記載する機構で充填
される。回転筒3が回転すると、回転筒3と被溶解物8
又は被溶解物8同士の間の摩擦により、被溶解物8は上
方に持ち上げられる。上方に持ち上げられた被溶解物8
は回転筒3が傾斜していることにより、当初の場所より
排出帯2側に落下する。被溶解物8が落下する場所に空
間があればそこに落下し、これを繰り返すことで、被溶
解物8は前方の排出帯2側に運ばれ、そして排出帯2に
落下し堆積する。更に回転筒3を回転しつつ被溶解物8
を回転筒3に装入することにより、排出帯2に落下し堆
積した被溶解物8は山盛り状になり、回転筒3から排出
される被溶解物8は堰き止められ、排出帯2への排出速
度が遅くなり、回転筒3内に被溶解物8が充填されてい
く。The material to be melted 8 charged by the charging conveyor 9 from the charging inlet 6 enters the rotary cylinder 3 by its own weight. The rotary cylinder 3 rotates around the center as an axis. The to-be-dissolved substance 8 is filled in the rotary cylinder 3 while moving upward in the rotary cylinder 3 while being lifted upward with its rotation. FIG. 2 shows this filling situation, and the filling is performed by the mechanism described below. When the rotating cylinder 3 rotates, the rotating cylinder 3 and the material to be melted 8 are rotated.
Alternatively, the material to be melted 8 is lifted upward due to friction between the materials to be melted 8. Dissolved material 8 lifted upward
Because the rotary cylinder 3 is inclined, it falls from the initial position to the discharge zone 2 side. If there is a space in the place where the melt 8 falls, if there is a space, the melt 8 is carried to the front discharge zone 2 side by repeating this, and drops and deposits on the discharge zone 2. Further, while rotating the rotary cylinder 3,
Is loaded into the rotary cylinder 3, the melted material 8 that has fallen and accumulated in the discharge zone 2 forms a heap, and the melted material 8 discharged from the rotary cylinder 3 is blocked, and The discharge speed becomes slower, and the to-be-dissolved substance 8 fills the rotary cylinder 3.
【0007】充填された被溶解物8は電気炉本体1内で
の溶解、精錬で発生する高温の排ガスと排ガスの二次燃
焼の火炎で予熱され、電気炉本体1に排出される。この
電気炉本体1への排出方法は回転筒3を回転すること、
又は回転筒3の回転によらず独立した排出機構を排出帯
2に設けることにより達成される。独立した排出機構を
設置することで、回転筒3内における被溶解物8の充填
と、電気炉本体1への被溶解物8の排出とを独立して行
うことができる。 [0007] the lysate was filled 8 dissolved in an electric furnace main assembly 1, is preheated in the secondary combustion of the flame of the high-temperature exhaust gas and the exhaust gas generated in the smelting, it is discharged into an electric furnace body 1. This discharge method to the electric furnace body 1 includes rotating the rotary cylinder 3,
Alternatively, this is achieved by providing an independent discharge mechanism in the discharge band 2 irrespective of the rotation of the rotary cylinder 3. Independent discharge mechanism
By installing, the filling of the to-be-dissolved substance 8 in the rotating cylinder 3
And discharge of the material 8 to be melted into the electric furnace main body 1 independently.
I can.
【0008】回転筒3内にラセン状の溝、又は突起物等
を設けることにより、回転による充填効率が向上し、こ
れらを設置することも有効である。By providing spiral grooves or projections in the rotary cylinder 3, the filling efficiency by rotation is improved, and it is also effective to install them.
【0009】[0009]
【実施例】(実施例1) 図1は本発明の一実施例を示す縦断面図である。予熱体
Aは、中心を軸として回転自在の回転筒3と、一方を電
気炉本体1の側壁の排ガス排出口1aと接し、もう一方
を回転筒3と接する排出帯2と、被溶解物8の流れの上
流側には被溶解物の装入口6を有し、回転筒3と接する
装入帯5とからなっている。更に、装入帯5より分岐し
て煙道7が設けられ、煙道7には電気炉本体1から発生
する高温の廃ガスを吸引する排ガス吸引用ファン4が設
けられている。予熱帯Aの主体を構成する回転筒3は、
装入口6側を上部にして水平面に対して10度傾斜して
設置されている。回転筒3は外径3m、長さ20mで、
回転数は最大5rpmである。(Embodiment 1) FIG. 1 is a longitudinal sectional view showing one embodiment of the present invention. Preheating body
A is a rotating cylinder 3 rotatably around an axis, one of them in contact with the exhaust gas outlet 1a of the side wall of the electric furnace body 1, a discharge zone 2 which is in contact with the rotating cylinder 3 and the other, of the lysate 8 on the upstream side of the flow it consists has a spout 6 of the lysate, the rotating cylinder 3 in contact SoIritai 5. Furthermore , branch off from charging zone 5
Flue 7 is provided Te, the flue 7 exhaust gas suction fan 4 for sucking the hot waste gas generated from the electric furnace body 1 is eclipsed set <br/>. Rotating cylinder 3 constituting the main body of the preheating zone A is
It is installed at an angle of 10 degrees with respect to the horizontal plane with the inlet 6 side as the upper part. The rotating cylinder 3 has an outer diameter of 3 m and a length of 20 m.
The rotation speed is up to 5 rpm.
【0010】装入口6より装入された被溶解物8は自重
で回転筒3に入る。この回転筒3は図示されていない回
転機構により回転される。回転により被溶解物8は回転
筒3内に天井部まで充填される。充填された被溶解物8
は電気炉本体1内での溶解、精錬で発生する高温の排ガ
スと排ガスの二次燃焼の火炎で効率よく予熱され、電気
炉本体1に排出される。この排出は回転筒3を回転する
ことによって達成され、本実施例における被溶解物8の
電気炉本体1への排出速度は、回転筒3の回転数を変え
ることで0〜5Ton/分に制御可能であった。The material to be melted 8 charged through the charging port 6 enters the rotary cylinder 3 by its own weight. The rotating cylinder 3 is rotated by a rotating mechanism (not shown). The object 8 to be melted is filled into the rotary cylinder 3 to the ceiling by rotation. Dissolved substance 8 filled
Is efficiently preheated by high-temperature exhaust gas generated by melting and refining in the electric furnace main body 1 and a flame of secondary combustion of the exhaust gas, and is discharged to the electric furnace main body 1. This discharge is achieved by rotating the rotary cylinder 3, and the discharge speed of the melt 8 to the electric furnace main body 1 in this embodiment is controlled to 0 to 5 Ton / min by changing the rotation speed of the rotary cylinder 3. It was possible.
【0011】図3には回転筒3内の被溶解物8の平均充
填率と被溶解物8の昇温速度の関係を示す。被溶解物8
の平均充填率を100、95、90、85、80%と変
え被溶解物8の温度を連続的に測定した。この場合平均
充填率を一定に保つために回転筒3は回転していない。
図3の横軸は被溶解物8の回転筒3内での平均の充填率
を示し、縦軸は被溶解物8の平均充填率を100%とし
たときのある一定時間での被溶解物8の昇温速度を1と
したときの比昇温速度を示しており、この比昇温速度が
大きい程、昇温が速くつまり予熱効率がよいこととな
る。この図より被溶解物8の平均充填率が85〜80%
以下となると、平均充填率が100%のときと比べて昇
温速度が半分以下となり、又、被溶解物8の平均充填率
が90%以上あると十分な予熱効率が得られることが分
かった。又、回転した場合は回転による温度の均一化で
予熱効率の向上も加わり、更に予熱効率は向上する。FIG. 3 shows the relationship between the average filling rate of the melt 8 in the rotary cylinder 3 and the rate of temperature rise of the melt 8. Dissolved material 8
Was changed to 100, 95, 90, 85, and 80%, and the temperature of the material to be dissolved 8 was continuously measured. In this case, the rotating cylinder 3 is not rotating in order to keep the average filling rate constant.
The horizontal axis in FIG. 3 shows the average filling rate of the substance 8 in the rotating cylinder 3, and the vertical axis shows the substance filling at a certain time when the average filling rate of the substance 8 is 100%. The figure shows the specific heating rate when the heating rate of 8 is set to 1, and the higher the specific heating rate, the faster the heating, that is, the better the preheating efficiency. According to this figure, the average filling rate of the material to be dissolved 8 is 85 to 80%.
Becomes less, heating rate and the average fill factor as compared with the case of 100% is less than half, also correspondingly be sufficient preheating efficiency can be obtained when the average filling factor of the melt 8 is not less than 90%
It was . In the case of rotation, the preheating efficiency is further improved by making the temperature uniform by the rotation, and the preheating efficiency is further improved.
【0012】従って、本発明は回転筒3内の被溶解物8
の平均充填率を90%以上とすることが可能であり、十
分な予熱効率を得ることができた。Accordingly, the present invention provides a method for dissolving the material 8 in the rotary cylinder 3.
Can be 90% or more, and sufficient preheating efficiency can be obtained.
【0013】(実施例2) 図4は排出機構として、板状のコンベア11を排出帯2
に設けた一実施例を示している。排出帯2の底面上を排
出口1aの方向に褶動可能な板状のコンベア11が配置
されており、その他の構成は実施例1と同一である。(Embodiment 2) FIG. 4 shows a plate-like conveyor 11 as a discharge mechanism ,
1 shows an embodiment provided in FIG. A plate-like conveyor 11 that is slidable on the bottom surface of the discharge zone 2 in the direction of the discharge port 1a is arranged, and other configurations are the same as those of the first embodiment.
【0014】本実施例は実施例1と被溶解物8の予熱完
了までは同じであり、予熱完了後の電気炉本体1への排
出機構が異なっており、予熱され排出帯2に堆積した被
溶解物8は、板状のコンベア11が前後に褶動すること
により、電気炉本体1に排出される。The present embodiment is the same as the first embodiment until the completion of preheating of the material 8 to be melted. The discharge mechanism to the electric furnace main body 1 after the completion of preheating is different. The melt 8 is discharged to the electric furnace main body 1 when the plate-shaped conveyor 11 folds back and forth.
【0015】板状のコンベア11の褶動により回転筒3
の回転に影響無く電気炉本体1への排出が可能で、回転
筒3の回転は被溶解物の回転筒3内への充填のみを制御
すればよく、常に安定した充填率を得ることができた。The rotating cylinder 3 is moved by the sliding of the plate-shaped conveyor 11.
Can be discharged to the electric furnace main body 1 without being affected by the rotation of the rotating furnace 3. The rotation of the rotating barrel 3 only needs to control the filling of the material to be melted into the rotating barrel 3, and a stable filling rate can always be obtained. Was.
【0016】(実施例3) 図5(a)(b)は排出機構として、排出帯2を回転さ
せる装置の一実施例を示す。排出帯2は円筒状であり、
装入口6側を上部にして水平面に対して傾斜して設置さ
れている。又、排出帯2は図示していない回転機構によ
り、軸を中心として両側に90度回転可能の構造となっ
ている。その他の構成は実施例1と同一である。(Embodiment 3) FIGS. 5A and 5B show an embodiment of a device for rotating a discharge band 2 as a discharge mechanism. The discharge zone 2 is cylindrical ,
It is installed at an angle to the horizontal plane with the charging inlet 6 side as the upper part. Further, the discharge zone 2 is configured to be rotatable 90 degrees to both sides about the axis by a rotation mechanism (not shown). Other configurations are the same as those of the first embodiment.
【0017】本実施例は実施例1と被溶解物8の予熱完
了までは同じであり、予熱完了後の電気炉本体1への排
出機構が異なっており、予熱され排出帯2に堆積した被
溶解物8は、排出帯2を軸を中心として両側に90度回
転させ、電気炉本体1に排出される。The present embodiment is the same as the first embodiment until the completion of preheating of the material 8 to be melted, and the discharging mechanism to the electric furnace main body 1 after the completion of preheating is different. The melt 8 is rotated 90 degrees on both sides about the axis of the discharge zone 2 and discharged to the electric furnace main body 1.
【0018】回転筒3の回転に影響無く、排出帯2の回
転により排出が可能で、回転筒3の回転は被溶解物の回
転筒3内への充填のみを制御すればよく、常に安定した
充填率を得ることができた。The discharge can be performed by the rotation of the discharge zone 2 without affecting the rotation of the rotary cylinder 3. The rotation of the rotary cylinder 3 only needs to control the filling of the material to be dissolved into the rotary cylinder 3, and is always stable. A filling factor could be obtained.
【0019】(実施例4) 図6は排出機構として、排出帯2の後部にプッシャー1
2を配置した一実施例を示しており、その他の構成は実
施例1と同一である。(Embodiment 4) FIG. 6 shows a pusher 1 at the rear of the discharge zone 2 as a discharge mechanism.
2 shows an embodiment in which 2 is arranged, and the other configuration is the same as that of the first embodiment.
【0020】本実施例は実施例1と被溶解物8の予熱完
了までは同じであり、予熱完了後の電気炉本体1への排
出機構が異なっている。予熱され排出帯2に堆積した被
溶解物8はプッシャー12で電気炉本体1へ排出され
る。The present embodiment is the same as the first embodiment up to the completion of the preheating of the material 8 to be melted, and the discharging mechanism to the electric furnace body 1 after the completion of the preheating differs. The material 8 to be melted which has been preheated and deposited in the discharge zone 2 is discharged to the electric furnace main body 1 by the pusher 12.
【0021】回転筒3の回転に影響無く、排出帯2の後
部のプッシャー12により排出が可能で、回転筒3の回
転は被溶解物の回転筒3内への充填のみを制御すればよ
く、常に安定した充填率を得ることができた。The discharge can be performed by the pusher 12 at the rear of the discharge zone 2 without affecting the rotation of the rotary cylinder 3, and the rotation of the rotary cylinder 3 may be controlled only by filling the rotary cylinder 3 with the material to be dissolved. A stable filling rate was always obtained.
【0022】[0022]
【発明の効果】以上のように、予熱帯の主体を構成する
回転筒に被溶解物を導入して回転筒を回転させることに
より、被溶解物の充填率を上げ、被溶解物の予熱効率を
著しく向上させることができた。As is evident from the foregoing description, by rotating the rotary cylinder by introducing the lysate into rotary cylinder which constitutes the main body of the preheating zone, increasing the packing ratio of the lysate, the preheating efficiency of the lysate Was significantly improved.
【図1】本発明の第1の一実施例を示す回転予熱帯を備
えた電気炉の縦断面図である。FIG. 1 is a longitudinal sectional view of an electric furnace having a rotating pre-tropical zone according to a first embodiment of the present invention.
【図2】回転筒内に被溶解物が天井部まで充填される様
子を示す概要図である。FIG. 2 is a schematic diagram showing a state in which a substance to be dissolved is filled into a rotating cylinder up to a ceiling.
【図3】第1の実施例における回転筒内の被溶解物の平
均充填率と被溶解物の昇温速度との関係を示すグラフ図
である。FIG. 3 is a graph showing a relationship between an average filling rate of a substance to be dissolved in a rotary cylinder and a rate of temperature rise of the substance to be dissolved in a first embodiment.
【図4】本発明の第2の実施例の排出機構を示す断面図
である。FIG. 4 is a sectional view showing a discharge mechanism according to a second embodiment of the present invention.
【図5】本発明の第3の実施例の排出機構を示し、
(a)は排出機構の断面図で、(b)はX−Y断面の断
面図である。FIG. 5 shows a discharge mechanism according to a third embodiment of the present invention;
(A) is a sectional view of a discharge mechanism, (b) is a cross <br/> view of X-Y cross section.
【図6】本発明の第4の実施例の排出機構を示す断面図
であるFIG. 6 is a sectional view showing a discharge mechanism according to a fourth embodiment of the present invention.
【図7】従来の予熱帯を備えた電気炉例を示す断面図で
ある。FIG. 7 is a cross-sectional view showing an example of a conventional electric furnace having a pre-tropical zone.
1 電気炉本体 1a 排ガス排出口 2 排出帯 A 予熱帯 3 回転筒 4 排ガス吸引用ファン 5 装入帯 6 装入口 7 煙道 8 被溶解物 9 装入用コンベア 10 排出用コンベア 11 排出用プッシャーDESCRIPTION OF SYMBOLS 1 Electric furnace main body 1a Exhaust gas discharge port 2 Discharge zone A Preliminary tropical zone 3 Rotary cylinder 4 Exhaust gas suction fan 5 Charging zone 6 Charging inlet 7 Flue 8 Melted material 9 Conveyor for charging 10 Conveyor for discharging 11 Pusher for discharging
Claims (5)
用ファンとの間に、被溶解物を予熱する予熱帯を備えた
電気炉において、前記予熱帯が、電気炉本体の排ガス排
出口に開口する排出帯と、この排出帯と接合し、中心を
軸として回転自在な回転筒と、この回転筒と接合し、被
溶解物の流れ方向の上流側に被溶解物の装入口を有する
装入帯とからなり、前記回転筒が被溶解物の装入口側を
上部として水平面に対して傾斜しており、回転筒が回転
することで、回転筒内に被溶解物が充填されることを特
徴とする回転予熱帯を備えた電気炉。To 1. A between the flue gas discharge outlet of the electric furnace body and the exhaust gas suction fan, in an electric furnace having a preheating zone for preheating the lysate, the preheating zone, the electric furnace body waste gas a discharge zone which is open to the scan discharge <br/> outlet, joined to the discharge zone, a rotatable rotary cylinder as the axis center, joined to the rotating cylinder, upstream of the flow direction of the melt to be to have a spout of the lysates
The rotating cylinder is inclined with respect to a horizontal plane with the charging inlet side of the material to be melted as an upper portion, and the rotating cylinder rotates.
An electric furnace equipped with a rotating pre-tropical zone , wherein the rotating cylinder is filled with a substance to be melted .
する排出機構を設けたことを特徴とする請求項1に記載
の回転予熱帯を備えた電気炉。2. The electric furnace according to claim 1 , wherein a discharge mechanism is provided in the discharge zone to discharge the material to be melted into the electric furnace main body.
向に褶動自在に設けられた板状のコンベアであることを
特徴とする請求項2に記載の回転予熱帯を備えた電気
炉。3. The electric device with a rotating pre-tropical zone according to claim 2 , wherein the discharge mechanism is a plate-shaped conveyor provided on the bottom surface of the discharge band so as to be slidable toward the discharge port. Furnace.
回転可能に設けられた排出帯であることを特徴とする請
求項2に記載の回転予熱帯を備えた電気炉。4. The discharge mechanism is 90 ° on both sides about the axis.
3. The electric furnace with a rotating pre-tropical zone according to claim 2 , wherein the rotatable discharge zone is provided.
たプッシャーであることを特徴とする請求項2に記載の
回転予熱帯を備えた電気炉。5. The electric furnace according to claim 2 , wherein the discharge mechanism is a pusher attached to a rear part of the discharge zone.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP35544293A JP2921381B2 (en) | 1993-12-30 | 1993-12-30 | Electric furnace with rotating pre-tropics |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP35544293A JP2921381B2 (en) | 1993-12-30 | 1993-12-30 | Electric furnace with rotating pre-tropics |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07198274A JPH07198274A (en) | 1995-08-01 |
| JP2921381B2 true JP2921381B2 (en) | 1999-07-19 |
Family
ID=18443981
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP35544293A Expired - Fee Related JP2921381B2 (en) | 1993-12-30 | 1993-12-30 | Electric furnace with rotating pre-tropics |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2921381B2 (en) |
-
1993
- 1993-12-30 JP JP35544293A patent/JP2921381B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07198274A (en) | 1995-08-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1091871C (en) | Apparatus for preheating and supplying scraps | |
| JPH0413296B2 (en) | ||
| CN1902329A (en) | Method for pre-heating, transforming and melting a metal charge and relative plant | |
| JP2921381B2 (en) | Electric furnace with rotating pre-tropics | |
| IE841674L (en) | Liquefying pulverulent batch materials particularly glass | |
| JPH0613950B2 (en) | Rotary kiln for heating powdery material and method for heating material | |
| JP2921380B2 (en) | Electric arc furnace with pre-tropics | |
| CA2198411A1 (en) | Method of operating an arc furnace, and an arc furnace | |
| JPH03207989A (en) | Method and device for charging material containing metal in metallic furnace | |
| RU2293938C1 (en) | Scrap heater of electric-arc steel-melting mean- and low- power furnace by means of flue gases | |
| JP2842198B2 (en) | Electric furnace with rotating pre-tropics | |
| JPH09217991A (en) | Iron scrap preheating device and preheating method | |
| KR900002522B1 (en) | A method for transferring glass batch material to a heating vessel and a device for liquefying powdered materials. | |
| JP7312499B1 (en) | metal melting furnace | |
| US4094667A (en) | Melting of fine particulate material in a high-speed rotary furnace | |
| JPH06191615A (en) | Powder disperser | |
| JP3588877B2 (en) | Ore and coke charging method in bellless blast furnace | |
| JP2000039267A (en) | Refuse melting furnace and refuse melting equipment using the same | |
| US4681537A (en) | Method and apparatus for continuously charging a steelmaking furnace | |
| JPH0979754A (en) | Continuous melting furnace | |
| CN113464961A (en) | Sludge incineration feeding and scattering machine | |
| RU2576973C2 (en) | Method of heating of loaded metal in melting unit, and heater of loaded material and melting unit | |
| JP2001090933A (en) | Waste melting equipment | |
| US3929459A (en) | Charging an electric furnace | |
| JPH07198273A (en) | Electric furnace with tilted shaft type pretropics |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19990330 |
|
| LAPS | Cancellation because of no payment of annual fees |