JPS5848549Y2 - Raw material charging device for vertical reduction furnace - Google Patents
Raw material charging device for vertical reduction furnaceInfo
- Publication number
- JPS5848549Y2 JPS5848549Y2 JP4432980U JP4432980U JPS5848549Y2 JP S5848549 Y2 JPS5848549 Y2 JP S5848549Y2 JP 4432980 U JP4432980 U JP 4432980U JP 4432980 U JP4432980 U JP 4432980U JP S5848549 Y2 JPS5848549 Y2 JP S5848549Y2
- Authority
- JP
- Japan
- Prior art keywords
- raw material
- charging device
- reduction furnace
- furnace
- charging
- 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
Landscapes
- Manufacture Of Iron (AREA)
- Vertical, Hearth, Or Arc Furnaces (AREA)
Description
【考案の詳細な説明】
本考案d1鉄鉱石、ペレット等を還元ガスにてガス還元
するための竪型炉の原料装入装置に関するものである。[Detailed Description of the Invention] The present invention d1 relates to a raw material charging device for a vertical furnace for gas reduction of iron ore, pellets, etc. with reducing gas.
従来の原料装入装置としては例えば第1図に見る如く炉
内装入物の粒度偏析を改善するため原料は炉頂部外に設
けられた複数本の装入管1を介し炉内に装入される如く
なしている。In a conventional raw material charging device, for example, as shown in Fig. 1, raw materials are charged into the furnace through a plurality of charging pipes 1 provided outside the top of the furnace in order to improve the particle size segregation of the contents in the furnace. I'm doing it like that.
ところが最近還元炉の生産性を向上させるため高圧操業
が有効であることが確認された。However, it has recently been confirmed that high-pressure operation is effective in improving the productivity of reduction furnaces.
この高圧操業を行なうためには当然のことながら別途ホ
ッパー、ゲート弁、シール弁等を必要とするがこれらを
従来の装入装置に設置するとなると装置高さが非常に高
くなるという難点を有していた。In order to perform this high-pressure operation, a separate hopper, gate valve, seal valve, etc. are naturally required, but if these are installed in a conventional charging device, the height of the device becomes extremely high. was.
そこでこれら問題点を解決せんがため炉高をできるだけ
低くして高圧操業にも充分対処し得るような且つ炉内の
粒度偏析の少ない装置として第2図に示すような装入装
置が提供されている。Therefore, in order to solve these problems, a charging device as shown in Fig. 2 has been provided as a device that lowers the furnace height as much as possible, can sufficiently cope with high-pressure operation, and has less particle size segregation inside the furnace. There is.
即ち均排圧槽8を設けた竪型還元炉において上記還元炉
の上方内部に仕切板を設けて原料の収納空間を形成し、
該仕切板に原料を流下せしめる装入管5を1本以上吊下
固定して上記炉内に貯留ホッパー3を構成し、上記仕切
板と上記パイプの下端を頂点とする装入物ストックライ
ンとの間に形成された空間部の還元炉炉壁に排ガスの導
出管11を有している装入装置である。That is, in a vertical reduction furnace equipped with a pressure equalization tank 8, a partition plate is provided inside the upper part of the reduction furnace to form a storage space for raw materials,
A storage hopper 3 is configured in the furnace by suspending and fixing one or more charging pipes 5 through which raw materials flow down to the partition plate, and a charge stock line having the apex at the lower end of the partition plate and the pipe is formed. This charging device has an exhaust gas outlet pipe 11 on the wall of the reduction furnace in the space formed between the two.
ところがこのような装入装置にあって原料を装入した場
合、上記貯留ホッパー3内の装入物粒度分布において装
入位置近傍には細粒が多く周辺程粗粒が増加する傾向に
なる。However, when such a charging device is used to charge raw materials, the particle size distribution of the charge in the storage hopper 3 tends to have many fine particles near the charging position and an increase in coarse particles toward the periphery.
これは原料の落下による動的流れによるものである。This is due to the dynamic flow caused by falling raw materials.
この傾向は還元炉の炉径が拡大する程、顕著に現われて
くる。This tendency becomes more pronounced as the diameter of the reduction furnace increases.
このような装入物の粒度偏析が上記貯留ホッパー3内で
生じると上記装入管5を介して還元炉本体2内でも同様
の粒度偏析となって現われてくる。When such particle size segregation of the charge occurs in the storage hopper 3, similar particle size segregation occurs in the reduction furnace main body 2 via the charging pipe 5.
これは還元ガスの偏流となって現れ、ついには還元炉の
生産性にも影響を及ぼしてくる。This appears as a biased flow of the reducing gas, and eventually affects the productivity of the reducing furnace.
本考案においてはこれらの問題点を改善するため上記構
成になる装入装置の貯留ホッパー3内に装入筒4を第3
図に示す如く設けたものである。In the present invention, in order to improve these problems, a third charging cylinder 4 is installed in the storage hopper 3 of the charging device configured as described above.
It is installed as shown in the figure.
以下本考案について説明する。The present invention will be explained below.
上記構成の本考案の装入装置にあって、ゲート弁10よ
り流出した原料6は装入筒4内に一旦貯留され原料の落
下による動的流れが止められる。In the charging device of the present invention having the above configuration, the raw material 6 flowing out from the gate valve 10 is temporarily stored in the charging cylinder 4, and dynamic flow due to falling of the raw material is stopped.
その後還元炉2の下部より内容物を切出すことにより装
入筒4内の原料は徐々に貯留ホッパー3内に流出してい
く。Thereafter, by cutting out the contents from the lower part of the reduction furnace 2, the raw material in the charging cylinder 4 gradually flows out into the storage hopper 3.
以上のように装入筒4内で原料の運動エネルギーを消す
ことにより貯留ホッパー3内で’D 粒度偏析が改善さ
れ、これにより装入管5を介して還元炉2内での粒度偏
析が改善されるものである。As described above, by extinguishing the kinetic energy of the raw material in the charging tube 4, the 'D particle size segregation in the storage hopper 3 is improved, and this improves the particle size segregation in the reduction furnace 2 via the charging tube 5. It is something that will be done.
以上本考案によれば炉内の装入物粒度偏析が改善できま
た還元炉の生産性向上が期待できるものである。As described above, according to the present invention, it is possible to improve the grain size segregation of the charge in the furnace, and it is expected that the productivity of the reduction furnace will be improved.
第1図は従来の竪型還元炉の原料装入装置の構造を示す
図、第2図は高圧操業装置例を示す図、第3図は本案の
実施例装置の説明図である。
1・・・装入管、2・・・還元炉本体、3・・・貯留ホ
ッパ4・・・装入筒、5・・・装入管、6・・・原料、
7・・・ゲート弁、8・・・均排圧管、9・・・シール
弁、10・・・シール弁、11・・・排ガス管。FIG. 1 is a diagram showing the structure of a conventional raw material charging device for a vertical reduction furnace, FIG. 2 is a diagram showing an example of a high-pressure operation device, and FIG. 3 is an explanatory diagram of an example device of the present invention. DESCRIPTION OF SYMBOLS 1... Charging pipe, 2... Reduction furnace main body, 3... Storage hopper 4... Charging cylinder, 5... Charging pipe, 6... Raw material,
7... Gate valve, 8... Equalizing pressure pipe, 9... Seal valve, 10... Seal valve, 11... Exhaust gas pipe.
Claims (1)
の下部は複数本の装入管を介し炉内に連通せしめる如く
なした原料装入装置において、上記貯留ホッパー内の上
部に装入筒を臨ませたことを特徴とする竪型還元炉の原
料装入装置。In a raw material charging device, a storage hopper is formed in a furnace top main body, and a lower part of the storage hopper is communicated with the inside of the furnace via a plurality of charging pipes, and a charging cylinder is provided in an upper part of the storage hopper. A raw material charging device for a vertical reduction furnace, which is characterized by the fact that:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4432980U JPS5848549Y2 (en) | 1980-04-02 | 1980-04-02 | Raw material charging device for vertical reduction furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4432980U JPS5848549Y2 (en) | 1980-04-02 | 1980-04-02 | Raw material charging device for vertical reduction furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56146899U JPS56146899U (en) | 1981-11-05 |
JPS5848549Y2 true JPS5848549Y2 (en) | 1983-11-05 |
Family
ID=29639593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4432980U Expired JPS5848549Y2 (en) | 1980-04-02 | 1980-04-02 | Raw material charging device for vertical reduction furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5848549Y2 (en) |
-
1980
- 1980-04-02 JP JP4432980U patent/JPS5848549Y2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS56146899U (en) | 1981-11-05 |
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