JPH0421814Y2 - - Google Patents

Info

Publication number
JPH0421814Y2
JPH0421814Y2 JP15373186U JP15373186U JPH0421814Y2 JP H0421814 Y2 JPH0421814 Y2 JP H0421814Y2 JP 15373186 U JP15373186 U JP 15373186U JP 15373186 U JP15373186 U JP 15373186U JP H0421814 Y2 JPH0421814 Y2 JP H0421814Y2
Authority
JP
Japan
Prior art keywords
raw material
bunker
blast furnace
pressure equalizing
pressure
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
Application number
JP15373186U
Other languages
Japanese (ja)
Other versions
JPS6360461U (en
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 filed Critical
Priority to JP15373186U priority Critical patent/JPH0421814Y2/ja
Publication of JPS6360461U publication Critical patent/JPS6360461U/ja
Application granted granted Critical
Publication of JPH0421814Y2 publication Critical patent/JPH0421814Y2/ja
Expired legal-status Critical Current

Links

Landscapes

  • Blast Furnaces (AREA)

Description

【考案の詳細な説明】 [産業上の利用分野] 本考案は炉頂装入装置に係り、特にセンターフ
イード型ベルレス式炉頂装入装置の均圧バンカの
構造を改良した炉頂装入装置に関するものであ
る。
[Detailed description of the invention] [Field of industrial application] The present invention relates to a furnace top charging device, and in particular, a furnace top charging device that improves the structure of the pressure equalizing bunker of a center feed type bellless type furnace top charging device. It is related to the device.

[従来の技術] 近年、高炉に用いられる炉頂装入装置として
は、炉内原料分布の自由度が大きいということか
らベルレス式炉頂装入装置が採用されている。
[Prior Art] In recent years, a bellless type furnace top charging device has been adopted as a furnace top charging device used in a blast furnace because it has a large degree of freedom in distributing raw materials in the furnace.

特に、原料分布の均一性の改善や原料供給工程
の短縮等を目的として、2基のバンカを上下二段
に配列したセンターフイード型ベルレス式炉頂装
入装置が採用される傾向にある。
In particular, for the purpose of improving the uniformity of raw material distribution and shortening the raw material supply process, there is a tendency to adopt a center-feed type bellless furnace top charging device in which two bunkers are arranged in two stages, one above the other.

従来、この種の炉頂装入装置は、第2図及び第
3に示す如く構成されていた。
Conventionally, this type of furnace top charging device has been constructed as shown in FIGS. 2 and 3.

第2図に示す第1の従来例にあつては、高炉a
の上部に高炉a内への原料の装入時に高炉aから
圧力が漏洩して高炉aの内部圧力が変動するのを
防止するために、その内部に区画された均圧室b
の内部圧力を高炉aの内部圧力と均等な圧力状態
に保持して高炉a内に原料cを装入するようにし
た均圧バンカdが設けられている。この均圧バン
カdの上部にはさらにバンカeが設けられてお
り、このバンカeは固定式或いは回転式となつて
いる。上段のバンカeの原料搬出口f及び下段の
均圧バンカdの原料導入口gは同軸上に各々一箇
所であつた。このように構成された炉頂装入装置
hの上段のバンカeの上部開口部に臨ませて、こ
のバンカe内に鉱石やコークス等の原料cを運搬
するベルトコンベア等の原料供給系iが地上から
傾斜して設けられている。尚、上記上段のバンカ
eが固定式の場合には通常上記ベルトコンベア等
の原料供給系i直下に旋回シユート(図示せず)
が設置されている。
In the first conventional example shown in FIG.
In order to prevent pressure from leaking from the blast furnace A and fluctuating the internal pressure of the blast furnace A when raw materials are charged into the blast furnace A, there is a pressure equalizing chamber B partitioned inside the blast furnace A.
A pressure equalizing bunker d is provided to charge raw material c into the blast furnace a while maintaining the internal pressure of the blast furnace a to be equal to the internal pressure of the blast furnace a. A bunker e is further provided above the pressure equalizing bunker d, and this bunker e is of a fixed type or a rotating type. The raw material outlet f of the upper bunker e and the raw material inlet g of the lower pressure equalizing bunker d were located at one location each on the same axis. A raw material supply system i such as a belt conveyor for conveying raw materials c such as ore and coke is installed inside the bunker e, facing the upper opening of the bunker e in the upper stage of the furnace top charging device h configured as described above. It is installed at an angle from the ground. If the upper bunker e is of a fixed type, there is usually a rotating chute (not shown) directly below the raw material supply system i such as the belt conveyor.
is installed.

また、第3図に示す第2の従来例にあつては、
上段のバンカeの原料搬出口f及びこれと係合す
る下段の均圧バンカdの原料導入口gが各々複数
に分岐して形成されている点で第1の従来例と相
異している。
Furthermore, in the second conventional example shown in FIG.
This differs from the first conventional example in that the raw material outlet f of the upper bunker e and the raw material inlet g of the lower pressure equalizing bunker d that engages with this are each branched into a plurality of parts. .

[考案が解決しようとする問題点] ところで、この種の炉頂装入装置hにあつては
以下の如き問題点があつた。
[Problems to be solved by the invention] By the way, this type of furnace top charging device h has the following problems.

第1の従来例にあつては上段のバンカeを回転
させるか、或いは旋回シユートを作動させながら
上段のバンカe内に原料cを受け入れ貯留するこ
とになる。このように原料cを受け入れることに
より、上段のバンカe内では原料c中の粗粒及び
細粒が略均一に混合された状態で貯留される。
In the first conventional example, the raw material c is received and stored in the upper bunker e while rotating the upper bunker e or operating the rotating chute. By receiving the raw material c in this manner, the coarse particles and fine particles in the raw material c are stored in the upper bunker e in a substantially uniformly mixed state.

しかし、上段のバンカe内の原料cが下段の均
圧バンカd内に導入された時、粗粒と細粒との原
料cの分離が再度発生し、下段の均圧バンカd内
には径方向外方に粗粒の原料cが堆積され、径方
向内方に細粒の原料cが堆積されるという偏析状
態で貯留されることになる。従つて、この偏析状
態の原料cが高炉a内に装入されると、原料cの
流出特性により、初期には均圧バンカdの中央部
の細粒の原料cが流出し、漸次周辺部の粗粒の原
料cが流出することになり、経時的に高炉a内に
装入される原料cの粒度が変動するという問題が
あつた。
However, when the raw material c in the upper bunker e is introduced into the lower pressure equalizing bunker d, separation of the raw material c into coarse particles and fine particles occurs again, and the diameter The raw material c is stored in a segregated state in which coarse grained raw material c is deposited outward in the radial direction and fine grained raw material c is deposited radially inward. Therefore, when the raw material c in this segregated state is charged into the blast furnace a, due to the outflow characteristics of the raw material c, initially the fine grained raw material c in the center of the pressure equalizing bunker d flows out, and gradually the raw material c in the surrounding area flows out. There was a problem in that the coarse-grained raw material c would flow out, and the particle size of the raw material c charged into the blast furnace a would fluctuate over time.

また、第2の従来例にあつても、上段のバンカ
eの原料搬出口f及びこれと係合する下段の均圧
バンカdの原料導入口gが各々複数に分岐されて
いるため、第1の従来例よりは均圧バンカd内の
径方向の原料cの偏析状態は改善されているもの
の、高炉a内に装入される原料cの経時的な粒度
の変動を防止することはできないという問題があ
つた。
In addition, even in the second conventional example, since the raw material outlet f of the upper bunker e and the raw material inlet g of the lower pressure equalizing bunker d that engage with this are each branched into a plurality of branches, the first Although the segregation state of the raw material c in the radial direction in the pressure equalizing bunker d is improved compared to the conventional example, it is said that it is not possible to prevent fluctuations in the particle size of the raw material c charged into the blast furnace a over time. There was a problem.

上述の如き問題点に鑑みて本考案は均圧バンカ
内に貯留される原料の粗粒と細粒との混合状態を
均一にして、高炉内に装入される原料の粒度が経
時的に変動することなく、均一な混合状態で装入
することができる炉頂装入装置を提供することを
目的とするものである。
In view of the above-mentioned problems, the present invention makes the mixed state of coarse particles and fine particles of the raw material stored in the pressure equalizing bunker uniform, and prevents the particle size of the raw material charged into the blast furnace from changing over time. It is an object of the present invention to provide a furnace top charging device that can charge in a uniformly mixed state without having to do so.

[問題点を解決するための手段] 従来技術における問題点を解決するために本考
案は下部が高炉の装入口に接続され、上部が原料
供給系に接続し、原料を導入するための原料導入
口を有すると共に、内部が高炉内圧と均圧にシー
ルされる均圧バンカと、この均圧バンカ内に傾動
かつ旋回自在に設けられ、上記原料導入口から導
入される原料を均圧バンカ内に均一に分配貯蔵す
るための分配シユートとを備えたものである。
[Means for Solving the Problems] In order to solve the problems in the conventional technology, the present invention has a lower part connected to the charging port of the blast furnace, an upper part connected to the raw material supply system, and a raw material introduction system for introducing the raw materials. A pressure equalizing bunker has a mouth and the inside is sealed to equalize the internal pressure of the blast furnace, and a pressure equalizing bunker is provided inside the pressure equalizing bunker so as to be tiltable and rotatable, and the raw material introduced from the raw material inlet is introduced into the pressure equalizing bunker. It is equipped with a distribution chute for uniformly distributing and storing.

[作用] 上述の如く構成され、上記均圧バンカ内に傾動
かつ旋回自在に分配シユートが設けられたので、
この分配シユートが傾動することにより均圧バン
カの径方向に、旋回することにより均圧バンカの
周方向に原料の粒度を調整することができ、均圧
バンカ内に均一に分配貯蔵され、高炉内に装入す
る原料に経時的な粒度の変動がなくなり、均一に
混合された状態で装入されるものである。
[Function] Since the distribution chute is configured as described above and is provided in the pressure equalizing bunker so as to be tiltable and pivotable,
By tilting this distribution chute, the particle size of the raw material can be adjusted in the radial direction of the pressure equalizing bunker, and by rotating it, the particle size of the raw material can be adjusted in the circumferential direction of the pressure equalizing bunker. There is no variation in particle size of the raw materials charged over time, and the raw materials are charged in a uniformly mixed state.

[実施例] 以下に本考案の一実施例を添付図面に従つて詳
述する。
[Example] An example of the present invention will be described in detail below with reference to the accompanying drawings.

第1図に示す如く、高炉1の上部には同軸に且
つ単段に均圧バンカ2が設けられている。この均
圧バンカ2の下部は高炉1の装入口3に接続され
ている。また、均圧バンカ2の上部は原料供給系
4に接続されている。この原料供給系4は例えば
地上から傾斜して設けられたベルトコンベア等に
て形成されている。この均圧バンカ2の上部には
上記原料供給系4から供給される鉱石やコークス
等の原料5を導入するための原料導入口6が設け
られている。この原料導入口6は例えばホツパに
て形成され、上方に向けて順次拡径されている。
この均圧バンカ2の内部には均圧室7が区画さ
れ、高炉1内への原料5の装入時に高炉1から圧
力が漏洩して高炉1の内部圧力が変動するのを防
止すべく均圧室7の内部圧力を高炉1の内部圧力
と均等な圧力状態に保持するようその上部及び下
部に各々上部シール弁8及び下部シール弁9を備
えている。また、均圧バンカ2内の均圧室7の上
方には傾動かつ旋回自在に分配シユート10が設
けられている。この分配シユート10は均圧バン
カ2の外部に設けられた駆動機構11に接続され
ている。更に、この分配シユート10の直上には
上記原料導入口6から均圧バンカ内に導入される
原料5を確実に分配シユート10へと導くための
内部ホツパ12が設けられている。そして、上記
原料導入口6の下部には上部ゲート弁13の設け
られ、上記均圧バンカ2の下部には下部ゲート弁
14が設けられて本考案の炉頂装入装置15は構
成されている。
As shown in FIG. 1, a pressure equalizing bunker 2 is provided coaxially and in a single stage in the upper part of the blast furnace 1. The lower part of this pressure equalizing bunker 2 is connected to the charging port 3 of the blast furnace 1. Further, the upper part of the pressure equalizing bunker 2 is connected to a raw material supply system 4. This raw material supply system 4 is formed, for example, by a belt conveyor or the like provided inclined from the ground. A raw material inlet 6 is provided in the upper part of the pressure equalizing bunker 2 for introducing raw material 5 such as ore or coke supplied from the raw material supply system 4. This raw material inlet 6 is formed by, for example, a hopper, and its diameter is gradually enlarged upward.
A pressure equalization chamber 7 is partitioned inside the pressure equalization bunker 2, and the pressure equalization chamber 7 is partitioned to prevent pressure from leaking from the blast furnace 1 and fluctuating the internal pressure of the blast furnace 1 when the raw material 5 is charged into the blast furnace 1. In order to keep the internal pressure of the pressure chamber 7 equal to the internal pressure of the blast furnace 1, an upper seal valve 8 and a lower seal valve 9 are provided at the upper and lower parts of the pressure chamber 7, respectively. Further, a distribution chute 10 is provided above the pressure equalization chamber 7 in the pressure equalization bunker 2 so as to be tiltable and pivotable. This distribution chute 10 is connected to a drive mechanism 11 provided outside the pressure equalizing bunker 2. Further, an internal hopper 12 is provided directly above the distribution chute 10 to reliably guide the raw material 5 introduced into the pressure equalizing bunker from the raw material inlet 6 to the distribution chute 10. An upper gate valve 13 is provided at the bottom of the raw material inlet 6, and a lower gate valve 14 is provided at the bottom of the pressure equalization bunker 2, thereby configuring the furnace top charging device 15 of the present invention. .

尚、上記高炉1の装入口3の直下には傾動かつ
旋回自在に炉内分配シユート16が設けられてい
る。
An in-furnace distribution chute 16 is provided directly below the charging port 3 of the blast furnace 1 so as to be tiltable and rotatable.

次に以上の如く構成された本考案の炉頂装入装
置の一実施例における作用を述べる。
Next, the operation of one embodiment of the furnace top charging device of the present invention constructed as described above will be described.

ベルトコンベア等の原料供給系4によつて炉頂
装入装置15の原料導入口6の直上まで運搬され
た鉱石やコークス等の原料5は上記原料導入口6
に供給される。この時、ホツパにて形成された原
料導入口6の下部に設けられた上部ゲート弁13
は開放されている。また、均圧バンカ2の下部に
設けられた下部ゲート弁14及び下部シール弁9
は閉成されている。
The raw material 5 such as ore or coke, which is transported by the raw material supply system 4 such as a belt conveyor to just above the raw material inlet 6 of the furnace top charging device 15, is transferred to the raw material inlet 6 of the furnace top charging device 15.
is supplied to At this time, an upper gate valve 13 provided at the bottom of the raw material inlet 6 formed in the hopper
is open. In addition, a lower gate valve 14 and a lower seal valve 9 provided at the lower part of the pressure equalizing bunker 2
is closed.

この原料導入口6より導入された原料5は均圧
バンカ2内に設けられた内部ホツパ12により分
配シユート10へと導かれる。この分配シユート
10は駆動機構11により傾動及び旋回作動す
る。この分配シユート10の傾動は均圧バンカ2
内の径方向の原料5の粒度調整を可能とし、又、
旋回は均圧バンカ2内の周方向の原料5の粒度調
整を可能にしており、原料5の堆積形態を可変と
し原料分布調整の自由度を向上させている。通
常、ベルトコンベア等の原料供給系6にて炉頂装
入装置15の直上へと運搬される原料5は運搬中
に細粒の原料5がベルト面に落ちて、ベルトの先
端部から供給される時点では原料帯の上層部は主
として粗粒の原料5、下層部は細粒の原料5とい
う分離形態を示しているが、このように分離して
原料導入口6に供給された原料5も均圧バンカ2
内に設けられた分配シユート10により分配投入
されるため、均圧バンカ2内に貯留される時点で
は粗粒と細粒との原料5の偏析が少なく比較的均
一に混合された状態で貯留されることになる。
The raw material 5 introduced through the raw material inlet 6 is guided to the distribution chute 10 by an internal hopper 12 provided in the pressure equalizing bunker 2. This distribution chute 10 is tilted and rotated by a drive mechanism 11. This tilting of the distribution chute 10 is caused by the pressure equalizing bunker 2.
It is possible to adjust the particle size of the raw material 5 in the radial direction, and
The rotation makes it possible to adjust the particle size of the raw material 5 in the circumferential direction within the pressure equalizing bunker 2, and makes the deposition form of the raw material 5 variable, thereby improving the degree of freedom in adjusting the raw material distribution. Normally, the raw material 5 is transported directly above the furnace top charging device 15 by a raw material supply system 6 such as a belt conveyor, and during transportation, fine grained raw material 5 falls onto the belt surface and is supplied from the tip of the belt. At the time of separation, the upper layer of the raw material belt is mainly coarse-grained raw material 5, and the lower layer is mainly fine-grained raw material 5, but the raw material 5 separated in this way and supplied to the raw material inlet 6 is also separated. Equal pressure bunker 2
Since the raw material 5 is distributed and fed through a distribution chute 10 provided in the pressure equalizing bunker 2, when it is stored in the pressure equalizing bunker 2, there is little segregation of the raw material 5 into coarse particles and fine particles, and it is stored in a relatively uniformly mixed state. That will happen.

上記均圧バンカ2内に原料5が貯留されると、
原料導入口6の上部ゲート弁13を閉成すると共
に、均圧バンカ2の上部に設けられた上部シール
弁8を閉成する。そして、均圧バンカ2内に区画
された均圧室7の内部圧力を高炉1の内部圧力と
均等な圧力にして保持する。爾後、均圧バンカ2
の下部に設けられた下部ゲート弁14及び下部シ
ール弁9を開放して均圧バンカ2内の原料5を高
炉1内に装入する。均圧バンカ2から高炉1の装
入口3に装入された原料5は高炉1内に傾動かつ
旋回自在に設けられた炉内分配シユート16へと
導かれ、この炉内分配シユート16により原料5
は高炉1内に均一に分配装入される。ここで、均
圧バンカ2内の原料5は一般的に、まず均圧バン
カ2内の中央下部の原料5から高炉1内へと流出
し、中央部、中央上部及び周辺部の順に落下し、
高炉1内へと流出する。しかし、本考案にあつて
は均圧バンカ2内に原料5が偏析の少ない状態で
貯留されているため、上述の如き状態で原料5が
高炉1内に流出しても、流出時に粗粒と細粒との
原料5の分離、或いは経時的な原料5の粒度の変
動が無くなり、均一に混合された状態で高炉1内
へと装入されるものである。
When the raw material 5 is stored in the pressure equalizing bunker 2,
The upper gate valve 13 of the raw material inlet 6 is closed, and the upper seal valve 8 provided at the upper part of the pressure equalizing bunker 2 is also closed. Then, the internal pressure of the pressure equalizing chamber 7 partitioned within the pressure equalizing bunker 2 is maintained equal to the internal pressure of the blast furnace 1. After that, equal pressure bunker 2
The lower gate valve 14 and the lower seal valve 9 provided at the lower part of the bunker are opened, and the raw material 5 in the pressure equalizing bunker 2 is charged into the blast furnace 1. The raw material 5 charged from the pressure equalization bunker 2 to the charging port 3 of the blast furnace 1 is guided to an in-furnace distribution chute 16 provided in the blast furnace 1 so as to be tiltable and rotatable.
are uniformly distributed and charged into the blast furnace 1. Here, the raw material 5 in the pressure equalizing bunker 2 generally first flows out into the blast furnace 1 from the raw material 5 at the lower center in the pressure equalizing bunker 2, and falls in the order of the center, the upper center, and the periphery.
It flows into the blast furnace 1. However, in the present invention, the raw material 5 is stored in the pressure-equalizing bunker 2 in a state with little segregation, so even if the raw material 5 flows into the blast furnace 1 in the above-mentioned condition, it becomes coarse particles when it flows out. Separation of the raw material 5 from fine particles or fluctuation in particle size of the raw material 5 over time is eliminated, and the raw material 5 is charged into the blast furnace 1 in a uniformly mixed state.

[考案の効果] 以上要するに本考案によれば次の如き優れた効
果を発揮する。
[Effects of the invention] In summary, the present invention provides the following excellent effects.

(1) 均圧バンカ内に傾動かつ旋回自在に分配シユ
ートを設けたので、高炉内に装入する原料に経
時的な粒度の変動が無くなり、均一に混合され
た状態で装入されるため、原料分布調整の自由
度の高い装置を提供することができ、高炉内反
応を促進させることができる。
(1) Since a distribution chute is installed inside the pressure equalization bunker so that it can tilt and rotate freely, there is no change in particle size of the raw materials charged into the blast furnace over time, and the raw materials are charged in a uniformly mixed state. It is possible to provide an apparatus with a high degree of freedom in adjusting raw material distribution, and it is possible to promote reactions in the blast furnace.

(2) 均圧バンカの上部が原料供給系に接続されて
いるので、炉頂装入装置の高さを減少させるこ
とができ、ベルトコンベア等の原料供給系の設
備を縮小することができ、設備コストを低減す
ることができる。
(2) Since the upper part of the pressure equalizing bunker is connected to the raw material supply system, the height of the furnace top charging device can be reduced, and the equipment of the raw material supply system such as belt conveyors can be reduced. Equipment costs can be reduced.

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

第1図は本考案の炉頂装入装置の一実施例を示
す概略図、第2図は第1の従来例を示す概略図、
第3図は第2の従来例を示す概略図である。 図中、1は高炉、2は均圧バンカ、4は原料供
給系、5は原料、6は原料導入口、10は分配シ
ユート、15は炉頂装入装置である。
FIG. 1 is a schematic diagram showing an embodiment of the furnace top charging device of the present invention, FIG. 2 is a schematic diagram showing a first conventional example,
FIG. 3 is a schematic diagram showing a second conventional example. In the figure, 1 is a blast furnace, 2 is a pressure equalizing bunker, 4 is a raw material supply system, 5 is a raw material, 6 is a raw material inlet, 10 is a distribution chute, and 15 is a furnace top charging device.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 下部が高炉の装入口に接続され、上部が原料供
給系に接続し、原料を導入するための原料導入口
を有すると共に、内部が高炉内圧と均圧にシール
される均圧バンカと、該均圧バンカ内に傾動かつ
旋回自在に設けられ、上記原料導入口から導入さ
れる原料を均圧バンカ内に均一に分配貯蔵するた
めの分配シユートとを備えたことを特徴とする炉
頂装入装置。
A pressure equalizing bunker whose lower part is connected to the charging port of the blast furnace, whose upper part is connected to the raw material supply system, has a raw material inlet for introducing the raw material, and whose inside is sealed to equalize the internal pressure of the blast furnace; A furnace top charging device characterized by comprising a distribution chute which is provided in a pressure bunker so as to be tiltable and rotatable, and for uniformly distributing and storing raw materials introduced from the raw material inlet into the pressure equalizing bunker. .
JP15373186U 1986-10-08 1986-10-08 Expired JPH0421814Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15373186U JPH0421814Y2 (en) 1986-10-08 1986-10-08

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15373186U JPH0421814Y2 (en) 1986-10-08 1986-10-08

Publications (2)

Publication Number Publication Date
JPS6360461U JPS6360461U (en) 1988-04-22
JPH0421814Y2 true JPH0421814Y2 (en) 1992-05-19

Family

ID=31072874

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15373186U Expired JPH0421814Y2 (en) 1986-10-08 1986-10-08

Country Status (1)

Country Link
JP (1) JPH0421814Y2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102912059A (en) * 2012-11-22 2013-02-06 中冶赛迪工程技术股份有限公司 Top charging device of shaft furnace

Also Published As

Publication number Publication date
JPS6360461U (en) 1988-04-22

Similar Documents

Publication Publication Date Title
JPH0421814Y2 (en)
US4067452A (en) Charging apparatus for receptacle
JPH046761B2 (en)
JPS59211515A (en) Charging device for charge
JP4608906B2 (en) Raw material charging method for bell-less blast furnace
JPH04358011A (en) Device for charging raw material
JPH04235206A (en) Method and apparatus for charging raw material in bellless blast furnace
KR20020037545A (en) Method for charging the charging materials into the blast furnace
JP2004346414A (en) Charging device for blast furnace
JPH02305911A (en) Bell-less type raw material charging method for vertical furnace
JPS6138901Y2 (en)
JPS60251208A (en) Method for charging raw material to blast furnace
JPS61202080A (en) Method and device for charging raw material in vertical typefurnace
JP2782786B2 (en) Raw material charging apparatus and charging method for bellless blast furnace
JPS61227109A (en) Charging method for blast furnace charge
JPH04183809A (en) Method for changing raw material in ball-less blast furnace
JPS63100113A (en) Bell-less charging apparatus in blast furnace
JPH0329311Y2 (en)
JPH0421724B2 (en)
CN117248088A (en) Multi-tank bell-less blast furnace distribution system
JPS6031065Y2 (en) Bellless charging device with multiple upper hoppers
JPH0354388Y2 (en)
JPH01500359A (en) Blast furnace charging equipment
JPH05179320A (en) Raw material charging method for bell-less blast furnace
SU470169A1 (en) Blast furnace bell-and-hopper arrangement