JPS635668B2 - - Google Patents
Info
- Publication number
- JPS635668B2 JPS635668B2 JP13704785A JP13704785A JPS635668B2 JP S635668 B2 JPS635668 B2 JP S635668B2 JP 13704785 A JP13704785 A JP 13704785A JP 13704785 A JP13704785 A JP 13704785A JP S635668 B2 JPS635668 B2 JP S635668B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- ore
- receiving plate
- feeding device
- lid
- 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
Links
- 238000005485 electric heating Methods 0.000 claims description 11
- 239000000571 coke Substances 0.000 description 10
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 6
- 239000011701 zinc Substances 0.000 description 6
- 229910052725 zinc Inorganic materials 0.000 description 6
- 238000004821 distillation Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 230000007246 mechanism Effects 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 238000003723 Smelting Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000004570 mortar (masonry) Substances 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010292 electrical insulation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000012840 feeding operation Methods 0.000 description 1
- 239000003779 heat-resistant material Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
- Furnace Charging Or Discharging (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、亜鉛等の鉱石の蒸留製錬に用いられ
る電熱炉に、鉱石とコークスとの混合物を供給、
装入するための電熱炉の給鉱装置に関するもので
ある。Detailed Description of the Invention (Field of Industrial Application) The present invention provides a method for supplying a mixture of ore and coke to an electric furnace used for distillation and smelting of ores such as zinc.
This relates to a feeding device for an electric furnace for charging.
(従来の技術)
はじめに、亜鉛製錬時の還元に用いられる電熱
炉の従来の給鉱装置の概要につき、第3図ないし
第5図を参照して説明する。(Prior Art) First, an outline of a conventional ore feeding device for an electric heating furnace used for reduction during zinc smelting will be explained with reference to FIGS. 3 to 5.
竪型円筒体より成る炉1の上端面は、回転式の
炉蓋2で閉塞されていて、この炉蓋2の上面に形
成された無心の歯板2aは、炉外に設置された駆
動機構3により連続駆動されており、すなわち、
駆動モータ4に直結された変速機5の出力ピニオ
ン5aに駆動されて連続回転している。 The upper end surface of the furnace 1, which is a vertical cylindrical body, is closed with a rotary furnace lid 2, and a toothless plate 2a formed on the upper surface of this furnace lid 2 is connected to a drive mechanism installed outside the furnace. It is continuously driven by 3, that is,
It is driven by an output pinion 5a of a transmission 5 directly connected to a drive motor 4 and rotates continuously.
しかして、炉蓋2の周上の1箇所には、給鉱孔
2bが上下に貫通して穿開されていて、かつこの
給鉱孔2bは、炉蓋2に従動して1体に回転する
シユート6の下端開口に接続されている。 Therefore, an ore feed hole 2b is drilled at one location on the circumference of the furnace lid 2, penetrating vertically, and this ore feed hole 2b follows the furnace lid 2 and rotates as one body. It is connected to the lower end opening of the chute 6.
ところで、このシユート6には、上方に連成さ
れた図示しないホツパから、焼結された亜鉛鉱石
と整粒されたコークスとの混合物(重量比で、鉱
石2:コークス1)が連続的に流下しており、こ
れにより炉1内には、上記混合物(以下、装入物
という)が給鉱孔2bから連続して落下するよう
になつている。 By the way, a mixture of sintered zinc ore and sized coke (weight ratio: 2 ore: 1 coke) is continuously flowing down into this chute 6 from a hopper (not shown) connected above. As a result, the above-mentioned mixture (hereinafter referred to as the charge) continuously falls into the furnace 1 from the ore feed hole 2b.
しかして炉1内に流入した装入物は、炉内の上
部に一旦給鉱層Fを形成した上で、逐次下方に移
動して行くが、給鉱層Fの表面は、装入時におい
て給鉱孔2bが連続的に旋回していることから、
給鉱孔2bの直下の周線上では山が高く、かつ炉
心C付近では摺鉢状に凹入した形状を成してい
る。 The charge that has flowed into the furnace 1 once forms an ore feed layer F in the upper part of the furnace and then moves downward one by one, but the surface of the ore feed layer F is Since the hole 2b rotates continuously,
The mountain is high on the circumferential line directly below the ore feed hole 2b, and has a concave shape near the core C.
なお、逐次炉内の下方に移動した装入物は、電
極7の通電熱によるコークス成分の燃焼加熱によ
り、鉱石から亜鉛蒸気を発生し、これにより排鉱
と分離された亜鉛成分は、コンデンサ8に流出す
るようになつており、しかしてこのような蒸留作
動間にあつては、炉心C付近の炉内温度は1.200
℃付近に達し、また炉壁寄りの周辺部は、900℃
付近の温度になつている。 Incidentally, the charge that has been moved downward in the furnace generates zinc vapor from the ore by combustion heating of the coke component by the electric heat applied to the electrode 7, and the zinc component separated from the discharged ore is transferred to the capacitor 8. During this distillation operation, the temperature inside the reactor near core C is 1.200.
℃, and the surrounding area near the furnace wall reaches 900℃.
The temperature has reached the nearby temperature.
そのほか、上述したように、混合物の装入物に
おいて炉蓋2を連続旋回させることにより、装入
物の給鉱層Fの表面形状に周縁上の山形分布を成
形させるようにした目的は、転がり易い特性を有
するコークス成分を成るべく炉壁寄りに分布させ
ると共に、転がり難い特性を有する鉱石成分を炉
心C付近に集めて、装入物に対する加熱効率を高
めると共に、鉱石に対する蒸留効率を高めるため
である。 In addition, as mentioned above, the purpose of forming the surface shape of the feed layer F of the charge into a mountain-shaped distribution on the periphery by continuously rotating the furnace cover 2 in the charge of the mixture is to make it easier to roll. This is to distribute the characteristic coke components as close to the furnace wall as possible, and to collect the ore components that are difficult to roll near the core C, thereby increasing the heating efficiency for the charge and the distillation efficiency for the ore. .
なお、上述した従来構造においては、炉蓋2の
1箇所に給鉱孔2bが穿開されているように説明
したが、実際の従来構造においては、第5図に鎖
線で示すように、炉蓋2の半径線上の3箇所に中
心距離の異る3つの給鉱孔を穿開しておき、電熱
炉の運転に当つてシユート6の下端を何れかの選
択された給鉱孔に接続させることにより、給鉱層
Fの成分分布状態を選択的に変え得るようにして
いる。 In the conventional structure described above, the ore feed hole 2b is bored in one place in the furnace lid 2, but in the actual conventional structure, the furnace lid Three ore feed holes with different center distances are drilled at three locations on the radius line of the lid 2, and the lower end of the chute 6 is connected to one of the selected ore feed holes when operating the electric heating furnace. This makes it possible to selectively change the component distribution state of the ore feed layer F.
(発明が解決しようとする問題点)
ところで、上述した構成の従来の給鉱装置にお
いては、炉蓋2を回転駆動させるための駆動機構
3を付設する必要があり、しかも炉蓋2の重量が
大きい(数トン)ために5.5kw程度の大きな動力
容量を要することから、電熱炉の設備費用と運転
費用との点で大きな負担となり、また、保守作業
時等において炉蓋2を着脱作業する際には、駆動
ピニオン5aを炉蓋2から手離す作業に大きな手
間がかかるという問題がある。(Problems to be Solved by the Invention) By the way, in the conventional ore feeding device having the above-described configuration, it is necessary to attach a drive mechanism 3 for rotationally driving the furnace lid 2, and the weight of the furnace lid 2 is large. Because it is large (several tons), it requires a large power capacity of about 5.5kw, which creates a large burden in terms of equipment costs and operating costs for the electric heating furnace. However, there is a problem in that it takes a lot of effort to remove the drive pinion 5a from the furnace lid 2.
それ以外にも、炉蓋2の歯板2aの外周縁の下
面が炉1の上端縁に摺接するサンドシール部Sに
は、電気的絶縁が必要であるが、サンドシール部
には、絶縁不良等のトラブルが発生し易いという
問題点があつた。 In addition, electrical insulation is required for the sand seal portion S where the lower surface of the outer peripheral edge of the tooth plate 2a of the furnace cover 2 slides into contact with the upper edge of the furnace 1. There was a problem that such troubles were likely to occur.
本発明は、このような問題点を解消するために
なされたものであつて、すなわち本発明は、炉蓋
を炉の上端に固定させたままの状態で、炉内上部
の給鉱層の表面分布形状に、上述した従来構造の
場合と同様な成分分布形状が得られるようにした
電熱炉の給鉱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 problems. Specifically, the present invention aims to improve the surface distribution of the ore feed layer in the upper part of the furnace while the furnace cover remains fixed to the upper end of the furnace. It is an object of the present invention to provide an ore feeding device for an electric heating furnace in which a component distribution shape similar to that of the conventional structure described above can be obtained.
(問題点を解決するための手段)
その目的を達成するため、本発明の構成におい
ては、竪型円筒体より成る炉の上端面には、中心
位置に給鉱孔を開口させている炉蓋が覆着、固定
されると共に、上記炉蓋の下面から適当寸法の対
接間隔だけ下がつた炉内位置に、炉心を中心とす
る円板形の受板がほぼ水平に吊下されている構造
としている。(Means for solving the problem) In order to achieve the object, in the configuration of the present invention, the upper end surface of the furnace consisting of a vertical cylindrical body has a furnace lid with an ore feed hole opened at the center position. is covered and fixed, and a disk-shaped support plate centered on the reactor core is suspended almost horizontally at a position in the reactor that is lowered from the lower surface of the reactor lid by an appropriate contact distance. It has a structure.
(作用)
このような構造により、炉蓋中心の給鉱孔から
炉内に落下した装入物は、受板の中央部に当つて
受板上に一旦堆積し、その堆積層の形状が、受板
の周縁を裾とする円錐形に成長した後は、受板の
全周縁から装入部が溢れ出して炉内を落下し、そ
の結果、炉内上部の給鉱層の表面の分布形状は、
従来の給鉱装置の旋回落下の場合と同様に、炉内
の炉壁寄りの周縁上に高い山が形成された有効な
形状となる。(Function) With this structure, the charge that falls into the furnace from the ore feed hole in the center of the furnace lid hits the center of the receiving plate and is temporarily deposited on the receiving plate, and the shape of the deposited layer is After growing into a conical shape with the periphery of the receiving plate as its hem, the charged portion overflows from the entire periphery of the receiving plate and falls into the furnace, and as a result, the distribution shape of the surface of the feed layer in the upper part of the furnace changes. ,
As in the case of a conventional ore feeder rotating fall, an effective shape is formed in which a high peak is formed on the peripheral edge of the furnace near the furnace wall.
(実施例)
以下、図示する2つの実施例に基づき、本発明
の構成を具体的に述べる。(Example) Hereinafter, the configuration of the present invention will be specifically described based on two illustrated examples.
(a) 第1の実施例(第1図参照)
この実施例の給鉱装置においては、単純な耐
熱板材より成る炉蓋8が、炉1の上端に着脱可
能に覆着、固定されると共に、炉蓋8の中心位
置には、給鉱孔8aが穿開された上で、同給鉱
孔8aは、下動のシユート9の下端開口に接続
されている。(a) First embodiment (see Figure 1) In the ore feeding device of this embodiment, a furnace lid 8 made of a simple heat-resistant plate is removably covered and fixed to the upper end of the furnace 1. An ore feed hole 8a is drilled in the center of the furnace lid 8, and the ore feed hole 8a is connected to the lower end opening of a downwardly movable chute 9.
なお、炉蓋8の周線上の複数箇所(図示で
は、左右の2箇所)には、後述する吊下棒10
が貫通する通し孔8bが開けられている。 In addition, at multiple locations on the circumference of the furnace lid 8 (in the illustration, two locations on the left and right), there are hanging rods 10, which will be described later.
A through hole 8b is opened through which the through hole 8b passes.
次に、炉1の直上の高所11には、左右の懸
下枠12と、両懸下枠12の下端間に水平に渡
設された案内フレーム13とによりコ形に形成
されて成るブラケツト14が固設されると共
に、両懸下枠12の基部の中間位置には、昇降
駆動用の動圧シリンダ15が下向きに設置され
ていて、かつ同シリンダ15の作動杆15aの
下端には、水平な吊下げバー16の中央部が取
付けられている。 Next, at a high place 11 directly above the furnace 1, there is a bracket formed in a U-shape by left and right suspension frames 12 and a guide frame 13 horizontally installed between the lower ends of both suspension frames 12. 14 is fixedly installed, and a dynamic pressure cylinder 15 for lifting and lowering is installed facing downward at an intermediate position between the bases of both suspension frames 12, and at the lower end of an operating rod 15a of the cylinder 15, A central portion of a horizontal hanging bar 16 is attached.
しかして、吊下げバー16の左右両端には、
セラミツク等の耐熱、耐絶縁材より成る吊下棒
10の上端が取付けられていて、かつ各吊下棒
10の途中は、フレーム13のガイド孔に案内
挿通された上で、炉蓋8の通し孔8bをシール
された状態で貫通し、更にその下端には、板端
を挾持し得るようにしたリテーナ10aが形成
されている。 Therefore, at both left and right ends of the hanging bar 16,
The upper ends of hanging rods 10 made of a heat-resistant and insulating material such as ceramic are attached, and the middle of each hanging rod 10 is guided through a guide hole in the frame 13, and then inserted through the furnace lid 8. A retainer 10a is formed at the lower end of the retainer 10a, which passes through the hole 8b in a sealed manner and can hold the end of the plate.
また、炉1の内空の炉蓋8の下面から適当寸
法の対接間隔dだけ下つた位置には、炉心Cを
中心とする円板形の耐熱質の受板17が水平に
張架されていて、同受板17は、左右の直径線
上の両端部が、夫々両吊下棒10の下端のリテ
ーナ10aに固着、保持されている。 Further, at a position below the lower surface of the inner furnace lid 8 of the furnace 1 by a contact distance d of an appropriate size, a disk-shaped heat-resistant receiving plate 17 with the core C in the center is suspended horizontally. Both end portions of the receiving plate 17 on the left and right diameter lines are fixed and held by the retainers 10a at the lower ends of both the hanging rods 10, respectively.
ここで、このように構成された実施例の給鉱
装置の作動につき説明する。 Here, the operation of the ore feeding device of the embodiment configured as described above will be explained.
シユート9を経て給鉱孔8aから炉1内に落
下した装入物、すなわち鉱石成分とコークス成
分との混合物は、受板17の中心部に当つて受
板17上に堆積し、その堆積層Eの形状が、図
示のように、受板17の周縁を裾とする円錐形
に成長した後は、装入物が受板17の全周縁か
ら炉内の炉壁寄りに溢れ出し、その結果、給鉱
層下は、従来の旋回落下の場合と同様に、炉壁
寄りの周線上に高い山を成す部分Aと、中央の
摺鉢形を成す部分Bとに同心円状に分布され
る。 The charge that has fallen into the furnace 1 from the ore feed hole 8a via the chute 9, that is, the mixture of ore components and coke components, hits the center of the receiving plate 17 and is deposited on the receiving plate 17, and the deposited layer is After the shape of E grows into a conical shape with the periphery of the receiving plate 17 as its base as shown in the figure, the charge overflows from the entire periphery of the receiving plate 17 toward the furnace wall in the furnace, resulting in As in the case of the conventional rotating drop, the bottom of the feed layer is distributed concentrically into a part A that forms a high mountain on the circumference near the furnace wall and a part B that forms a mortar shape in the center.
しかしてこのような分布によると、従来構造
の項で述べたように、給鉱層Fの山部分Aは、
コークスリツチ層となり、かつ炉心C付近の摺
鉢部分Bは、シンタ(鉱石)リツチ層となつ
て、亜鉛成分の有効な蒸留分離作用が行われ
る。 However, according to this distribution, as mentioned in the section on the conventional structure, the mountain portion A of the ore feeding layer F is
The mortar part B, which becomes a coke rich layer and is near the core C, becomes a sinter (ore) rich layer, and an effective distillation separation action of the zinc component is performed.
なお、シリンダ15の昇降調整操作により受
板17の対接間隔dを狭くすれば、コークスの
リツチ密度が周辺に偏り、また対接間隔dを広
くすれば、コークスのリツチ密度が炉心C寄り
に広がるので、炉1の環境条件に応じて炉内温
度の温度分布を最良状態に調整、維持すること
ができる。 If the contact distance d between the receiving plates 17 is narrowed by adjusting the elevation of the cylinder 15, the coke richness density will be biased towards the periphery, and if the contact distance d is widened, the coke rich density will be shifted closer to the core C. Since it spreads, the temperature distribution in the furnace 1 can be adjusted and maintained in the best condition according to the environmental conditions of the furnace 1.
(b) 第2の実施例(第2図参照)
この実施例の給鉱装置の構成は、受板18の
径寸と、受板18の保持態様が異る以外は、す
べて第1の実施例の場合の構成と等しく、すな
わち、炉1の上端面に炉蓋8が固定されると共
に、高所11には、ブラケツト14とシリンダ
15とが設置され、かつ作動杆15aには、吊
下げバー16が取付けられている。(b) Second embodiment (see Figure 2) The configuration of the ore feeding device of this embodiment is completely different from that of the first embodiment except for the diameter of the receiving plate 18 and the manner in which the receiving plate 18 is held. The configuration is the same as in the example, that is, the furnace lid 8 is fixed to the upper end surface of the furnace 1, a bracket 14 and a cylinder 15 are installed at the high place 11, and the operating rod 15a has a hanging A bar 16 is attached.
ところで左右の各吊下棒19の下端には、水
平な取付アーム19aがL形に固設されてい
て、かつ同アーム19aの内方端には、受板1
8を取付けるためのボルト孔が開けられてお
り、これにより径寸の小さい受板18は着脱自
在にボルト20によりアーム19aに固着され
ている。 Incidentally, a horizontal mounting arm 19a is fixed in an L shape at the lower end of each of the left and right hanging rods 19, and a receiving plate 1 is attached to the inner end of the arm 19a.
A bolt hole for attaching the arm 19 is made, and the small diameter receiving plate 18 is detachably fixed to the arm 19a by a bolt 20.
なお、この実施例の場合には、使用する受板
が、小径の受板18のほかに、径寸の異なる中
径、大径(受板17の径寸と等しい)の受板が
別に準備されていて、上述と同じボルト孔に取
付け得るようになつていて、表記では、受板1
8を選択して使用したものである。 In the case of this embodiment, in addition to the small diameter receiving plate 18, medium diameter and large diameter receiving plates (equal to the diameter of the receiving plate 17) with different diameters are prepared separately. It is designed so that it can be installed in the same bolt hole as mentioned above, and in the notation, the receiving plate 1
8 was selected and used.
この実施例の給鉱装置の作動においては、受
板18の径寸が小さいことから、堆積層Eの裾
径が小さく、その結果、給鉱層Fの山部の同心
径が小さくなつて山部が炉心Cに近寄り、これ
により炉壁寄りのコークス比が高い分布を示
す。 In the operation of the ore feeding device of this embodiment, since the diameter of the receiving plate 18 is small, the hem diameter of the deposited layer E is small, and as a result, the concentric diameter of the peak of the ore feeding layer F becomes small. is closer to the reactor core C, resulting in a distribution with a higher coke ratio near the reactor wall.
なお、受板18を別の大径の受板に交換すれ
ば、上述した第1実施例におけると同様な給鉱
層の分布になることは言うまでもない。 It goes without saying that if the receiving plate 18 is replaced with another receiving plate having a larger diameter, the distribution of the ore feeding layer will be similar to that in the first embodiment described above.
以上述べたように、本発明の実施例において
は、その給鉱作動について従来と同様な装入物の
分布が得られ、これにより鉱石の良好な蒸留作用
が得られる。 As described above, in the embodiment of the present invention, a distribution of the charge similar to the conventional one is obtained for the ore feeding operation, and thereby a good distillation action of the ore is obtained.
しかして、実施例の構成においては、炉蓋8を
固定取付けとしたために、従来に比べ次のような
利点がある。 Therefore, in the configuration of the embodiment, since the furnace cover 8 is fixedly attached, there are the following advantages over the conventional structure.
(a) 動力駆動機構を必要とせず、従つて、設備
費、運転費がかからないほか、炉蓋の軽量化が
可能となる。(a) There is no need for a power drive mechanism, so equipment costs and operating costs are reduced, and the furnace cover can be made lighter.
(b) サンドシール部に絶縁対策を行う必要がな
く、かつトラブルがなくなる。(b) There is no need to take insulation measures for the sand seal part, and troubles are eliminated.
(c) 炉蓋の着脱作業に大きな手間と費用がかから
ず、電熱炉の保守が大幅に簡易化する。(c) The work of attaching and detaching the furnace lid does not require much effort and expense, and maintenance of the electric heating furnace is greatly simplified.
なお、上述した実施例の構成においては、受板
17,18を単一のシリンダで昇降させるように
したが、これに替え、夫々の吊下棒10,19ご
とに個別にシリンダを設けることにより、受板1
7,18に勾配を付け得るようにしても良く、こ
のようにすれば、給鉱層の成分を分布を多様化す
ることができる。 In the configuration of the above-described embodiment, the receiving plates 17 and 18 are raised and lowered by a single cylinder, but instead of this, a cylinder is provided for each of the hanging rods 10 and 19 individually. , catch plate 1
7 and 18 may be made to have a gradient, and by doing so, the distribution of the components of the ore-feeding layer can be diversified.
また、第2の実施例の構成においては、受板の
径寸を可変とするために、複数の異径の受板を選
択的に使用する方法を採つたが、これに替え、例
えばシヤツタ方式による拡径、縮径可能の組付け
構造の受板を使用するようにしても良い。 Furthermore, in the configuration of the second embodiment, in order to make the diameter of the receiving plate variable, a method was adopted in which a plurality of receiving plates of different diameters were selectively used. It is also possible to use a receiving plate with an assembly structure that allows diameter expansion and diameter reduction.
(発明の効果)
以上述べたように、本発明に係る電熱炉の給鉱
装置によれば、炉蓋を炉の上端面に固定させると
共に、炉蓋の中央部に穿開された給鉱孔の下方の
適当な高さの炉内に、受板をほぼ水平に吊架させ
るように構成したので、給鉱作動性を良好に維持
した上で、炉蓋を回転させるために従来要した一
切の費用や手間が省け、これにより電熱炉の経済
性、信頼性および保守性を向上させる効果があ
る。(Effects of the Invention) As described above, according to the ore feeding device for an electric heating furnace according to the present invention, the furnace lid is fixed to the upper end surface of the furnace, and the ore feeding hole is drilled in the center of the furnace lid. The structure is such that the receiving plate is suspended almost horizontally in the furnace at an appropriate height below the furnace, so while maintaining good ore feeding operability, there is no need for the conventional method of rotating the furnace lid. This has the effect of improving the economic efficiency, reliability, and maintainability of electric heating furnaces.
第1図は、本発明の第1の実施例を示す電熱炉
の給鉱装置の概略図、第2図は、第2の実施例を
示す給鉱装置の概略図、第3図は、従来の給鉱装
置の概要図、第4図は、第3図の上部の拡大図、
第5図は、第4図の上面図である。
C……炉心、d……対接間隔、1……炉、8…
…炉蓋、8a……給鉱孔、10,19……吊下
棒、15……可変駆動手段としてのシリンダ、1
7,18……互に径寸の異なる各受板。
FIG. 1 is a schematic diagram of an ore feeding device for an electric heating furnace showing a first embodiment of the present invention, FIG. 2 is a schematic diagram of an ore feeding device showing a second embodiment, and FIG. 3 is a conventional ore feeding device. Figure 4 is an enlarged view of the upper part of Figure 3.
FIG. 5 is a top view of FIG. 4. C...core, d...contact spacing, 1...furnace, 8...
...Furnace cover, 8a...Ore feed hole, 10, 19...Hanging rod, 15...Cylinder as variable drive means, 1
7, 18...Each receiving plate having a different diameter.
Claims (1)
置に給鉱孔を開口させている炉蓋が覆着、固定さ
れると共に、上記炉蓋の下面から適当寸法の対接
間隔だけ下がつた炉内位置に、炉心を中心とする
円板形の受板がほぼ水平に吊架されていることを
特徴とする電熱炉の給鉱装置。 2 上記受板は、上記対接間隔を可変として吊架
されている特許請求の範囲第1項記載の電熱炉の
給鉱装置。 3 上記受板は、その径寸が変え得るように形成
されている特許請求の範囲第1項記載の電熱炉の
給鉱装置。 4 受板を円周方向数カ所で吊し、受板と水平面
との角度を変化させることにより、炉内への装入
物の分布状況を制御する特許請求の範囲第1項記
載の電熱炉の給鉱装置。[Claims] 1. A furnace lid with an ore feed hole opened at the center is covered and fixed to the upper end surface of the furnace consisting of a vertical cylindrical body, and an appropriate dimension is removed from the bottom surface of the furnace lid. An ore feeding device for an electric furnace, characterized in that a disk-shaped receiving plate centered on the reactor core is suspended almost horizontally at a position in the furnace that is lowered by a contact interval of . 2. The ore feeding device for an electric heating furnace according to claim 1, wherein the receiving plate is suspended so that the contact interval is variable. 3. The ore feeding device for an electric heating furnace according to claim 1, wherein the receiving plate is formed so that its diameter can be changed. 4. The electric heating furnace according to claim 1, wherein the receiving plate is hung at several locations in the circumferential direction and the distribution of the charge into the furnace is controlled by changing the angle between the receiving plate and the horizontal plane. Ore feeding equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13704785A JPS61295490A (en) | 1985-06-25 | 1985-06-25 | Feeder for electric heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13704785A JPS61295490A (en) | 1985-06-25 | 1985-06-25 | Feeder for electric heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61295490A JPS61295490A (en) | 1986-12-26 |
| JPS635668B2 true JPS635668B2 (en) | 1988-02-04 |
Family
ID=15189628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13704785A Granted JPS61295490A (en) | 1985-06-25 | 1985-06-25 | Feeder for electric heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61295490A (en) |
-
1985
- 1985-06-25 JP JP13704785A patent/JPS61295490A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61295490A (en) | 1986-12-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4474315A (en) | Molten metal transfer device | |
| JP2008285351A (en) | Material supply apparatus, single crystal drawing apparatus equipped with the same, and material supply method | |
| US2975036A (en) | Crystal pulling apparatus | |
| US4527329A (en) | Process for the manufacture "in situ" of carbon electrodes | |
| AU705067B2 (en) | Method and apparatus for producing self-baking carbon electrode | |
| JPS635668B2 (en) | ||
| JP2983881B2 (en) | Precision casting equipment with lock gate | |
| US4700355A (en) | Electrical melting furnace exchangeable electrode assembly a method for changing a contact electrode assembly | |
| US2300355A (en) | Process for the production of carbides and ferro-alloys | |
| US4133968A (en) | Apparatus for forming self-sintering electrodes | |
| US4730338A (en) | Coupling construction for an electric furnace | |
| US2822328A (en) | Bifurcated self-baking anode and gas collection means | |
| US3723093A (en) | Process for the continuous production of aluminum | |
| US1463970A (en) | Draw-off for electric furnaces | |
| US3075263A (en) | Apparatus for melting metals | |
| US5978410A (en) | Method for production of carbon electrodes | |
| KR101255891B1 (en) | Solid raw material supplying apparatus and single crystal growing device using the same | |
| US2857444A (en) | Gas collecting apparatus for open furnaces | |
| US2494501A (en) | Submerged resistor induction furnace | |
| US3129274A (en) | Reduction furnace provided with superstructure | |
| JPS6234717B2 (en) | ||
| JPH03193694A (en) | Crystal growing device | |
| JPH0196087A (en) | Equipment for pulling out single crystal | |
| JP2816623B2 (en) | Single crystal manufacturing apparatus and manufacturing method | |
| CN222865545U (en) | A smelting and processing device for recycling slag |