JPS6113913Y2 - - Google Patents

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Publication number
JPS6113913Y2
JPS6113913Y2 JP13447183U JP13447183U JPS6113913Y2 JP S6113913 Y2 JPS6113913 Y2 JP S6113913Y2 JP 13447183 U JP13447183 U JP 13447183U JP 13447183 U JP13447183 U JP 13447183U JP S6113913 Y2 JPS6113913 Y2 JP S6113913Y2
Authority
JP
Japan
Prior art keywords
furnace
charging
raw material
partition plate
tube
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
JP13447183U
Other languages
Japanese (ja)
Other versions
JPS6043992U (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 JP13447183U priority Critical patent/JPS6043992U/en
Publication of JPS6043992U publication Critical patent/JPS6043992U/en
Application granted granted Critical
Publication of JPS6113913Y2 publication Critical patent/JPS6113913Y2/ja
Granted legal-status Critical Current

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  • Vertical, Hearth, Or Arc Furnaces (AREA)
  • Manufacture Of Iron (AREA)

Description

【考案の詳細な説明】 本考案は鉄鉱石、ペレツト等を還元ガスにてガ
ス還元するための竪型還元炉の原料装入装置の改
良に関し、特に炉高を出来るだけ低くして高圧操
業にも充分対処し得るように構成された竪型還元
炉の炉内の円周方向の原料粒度偏析を有効に防止
することができる竪型還元炉の原料装置を提供す
るものである。
[Detailed description of the invention] This invention relates to the improvement of a raw material charging device for a vertical reduction furnace for gas reduction of iron ore, pellets, etc. using reducing gas. The object of the present invention is to provide a raw material device for a vertical reduction furnace that can effectively prevent raw material particle size segregation in the circumferential direction within the vertical reduction furnace that is configured to sufficiently cope with the above problems.

炉高を出来るだけ低くして高圧操業にも充分対
処し得る竪型還元炉の原料装入装置として、第1
図に示す様な装入装置が提供されている。即ち、
コンベヤ1より原料を受ける炉頂ホツパー2とこ
のホツパー2内の原料をゲート弁3及びシール弁
4を介して受け、ゲート弁5及びシール弁6を介
して竪型炉7へ原料を供給する均排圧槽8を設け
た竪型還元炉7において、この還元炉の上方内部
に仕切板9を設けて原料の収納空間を形成し、こ
の仕切板9に、原料を流下せしめる装入筒10
を、例えば第1図のA−A断面図を示す第2図の
如く炉芯11を中心とする同芯円軌跡上に等間隔
で、間欠的に例えば6本吊下固定して竪型炉7内
に貯留ホツパー12を構成し、上記仕切板9と装
入筒10の下端を頂点とする装入物13のストツ
クラインとの間に形成された空間部の炉壁14に
排ガスの導出管15を設けてなる原料装入装置で
ある。
The first material charging device for a vertical reduction furnace is designed to keep the furnace height as low as possible and fully handle high-pressure operations.
A charging device as shown in the figure is provided. That is,
A furnace top hopper 2 receives raw materials from a conveyor 1, and a system that receives raw materials in this hopper 2 via a gate valve 3 and a seal valve 4, and supplies raw materials to a vertical furnace 7 via a gate valve 5 and a seal valve 6. In a vertical reduction furnace 7 equipped with an exhaust pressure tank 8, a partition plate 9 is provided in the upper interior of the reduction furnace to form a storage space for raw materials, and a charging tube 10 in which the raw materials are allowed to flow down into the partition plate 9.
For example, as shown in FIG. 2, which shows a cross-sectional view taken along line A-A in FIG. A storage hopper 12 is configured within the chamber 7, and an exhaust gas outlet pipe is installed in the furnace wall 14 of the space formed between the partition plate 9 and the stock line of the charge 13 whose apex is the lower end of the charging tube 10. This is a raw material charging device provided with 15.

なお16は均排圧槽8のゲート弁5より流出し
た原料を一旦貯留して原料の落下による動的流れ
を防止して貯留ホツパー12内での炉半径方向の
粒度偏析を改善するためにホツパー12内に設け
た装入筒である。
Note that 16 is a hopper for temporarily storing the raw material flowing out from the gate valve 5 of the equalizing pressure tank 8 to prevent dynamic flow due to falling of the raw material and improving grain size segregation in the furnace radial direction within the storage hopper 12. This is a charging cylinder provided in 12.

ところが、この装入装置にあつては、炉芯11
を中心とする半径D円軌跡上に等間隔で間欠的に
配設した各装入筒10下端に、装入筒10下端を
頂点とする山型ストツクラインが形成され、装入
筒10内を流下する原料は、装入筒10下端を中
心とする周囲に転動供給されるため、装入筒10
直下部には、細粒が多くて、上記円軌跡上の装入
筒10−10間の中間部には、粗粒が増加する傾
向になる。
However, in this charging device, the furnace core 11
A chevron-shaped stock line with the lower end of the charging cylinder 10 as its apex is formed at the lower end of each charging cylinder 10 which is arranged intermittently at equal intervals on a circular locus with a radius D centered at . Since the raw material flowing down is supplied rolling around the lower end of the charging cylinder 10,
There is a tendency that there are many fine grains directly below, and coarse grains increase in the middle part between the charging cylinders 10-10 on the circular locus.

このような炉芯11より半径D位置の炉内の円
周方向の粒度偏析が生じると円周方向の還元ガス
流れが分布が不均一となり必要な還元ガス量が増
加する。
When such particle size segregation occurs in the circumferential direction within the furnace at the radius D from the furnace core 11, the distribution of the reducing gas flow in the circumferential direction becomes non-uniform and the required amount of reducing gas increases.

上記炉芯を中心とする同芯円軌跡上に等間隔で
配設した複数の装入筒の下端開口を結ぶ同芯円軌
跡上に形成される粒度偏析を改善するために、多
数の装入筒を密接設置して、装入筒下端から流下
する原料の円周方向の転動を減少することが考え
られるがこの場合には、隣接する装入筒間の炉芯
部排ガス通路面積が激減して、上記排ガスの通気
抵坑が増大し、これにより還元ガスの吹込圧力が
増大したり、ダストの筒付着によつて炉芯部排ガ
スの排出そのものが短期間で困難となる等の問題
が生じる。
In order to improve particle size segregation that is formed on a concentric circular locus that connects the lower end openings of multiple charging cylinders arranged at equal intervals on a concentric circular locus centered on the furnace core, a large number of charging tubes are It is possible to install the tubes closely together to reduce rolling of the raw material flowing down from the bottom end of the charging tube in the circumferential direction, but in this case, the area of the exhaust gas passage in the furnace core between adjacent charging tubes is drastically reduced. As a result, the above-mentioned ventilation resistance of the exhaust gas increases, which causes problems such as an increase in the blowing pressure of the reducing gas, and the exhaust gas itself from the furnace core becomes difficult to discharge in a short period of time due to dust attached to the cylinder. arise.

本考案は上記問題を引き起すことなく、炉芯を
中心とする同芯円軌跡上に等間隔で間欠的に配設
した複数の装入筒の下端開口を結ぶ同芯円軌跡上
に形成される粒度偏析(以下円周方向粒度偏析と
いう)を解消する原料装入装置を提供するもので
あり、その要旨は次の通りである。
The present invention does not cause the above-mentioned problems, and the charging tubes are formed on a concentric circular locus that connects the lower end openings of a plurality of charging tubes arranged intermittently at equal intervals on a concentric circular locus centered on the furnace core. The purpose of the present invention is to provide a raw material charging device that eliminates grain size segregation (hereinafter referred to as circumferential grain size segregation), and its gist is as follows.

本考案は竪型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、この仕切板に原料を
流下せしめる装入筒を炉芯を中心とする同芯円軌
跡上に等間隔で、複数本吊下固定して上記炉内に
貯留ホツパーを構成し、上記仕切板と装入筒の下
端を頂点とする装入物ストツクラインとの間に形
成された空間部の炉壁に排ガスの導出管を設けて
なる竪型還元炉の原料装入装置において、 上記装入筒として、少なくとも装入筒下部にお
いて下方に向つて原料通路面積が漸増し、かつ下
端に円弧状開口を形成した装入筒を採用して上記
円弧状開口群により、仕切板の下方の炉内に炉芯
を中心とする同芯リング状の原料排出口を形成し
たことを特徴とする竪型還元炉の原料装入装置で
ある。
In this invention, a partition plate is provided inside the upper part of the vertical reduction furnace to form a storage space for raw materials, and charging tubes for allowing the raw material to flow down into this partition plate are arranged at equal intervals on a concentric circular locus centered on the furnace core. A storage hopper is formed in the furnace by suspending and fixing a plurality of hoppers. In a raw material charging device for a vertical reduction furnace provided with an exhaust gas outlet pipe, the charging tube has a material passage area that gradually increases downward at least at the bottom of the charging tube, and an arcuate opening is formed at the lower end. A vertical reduction furnace characterized in that a concentric ring-shaped raw material discharge port centered on the furnace core is formed in the furnace below the partition plate by using the above-mentioned group of arc-shaped openings. This is a raw material charging device.

以下本考案を図示の一実施例に基づいて説明す
る。
The present invention will be explained below based on an illustrated embodiment.

第3図、第4図、及び第5図、第6図は、本考
案の原料装入装置に採用する装入筒を例示したも
のであり、第3図、第5図は、装入筒16,17
の第4図、第6図に示すB−B線の垂直断面図で
あり、第4図、第6図は第3図第5図のC−C矢
視図である。
3, 4, 5, and 6 show examples of the charging tube used in the raw material charging device of the present invention. 16,17
FIGS. 4 and 6 are vertical sectional views taken along the line B-B shown in FIGS. 4 and 6, and FIGS. 4 and 6 are views taken along the line C-C in FIGS. 3 and 5. FIG.

第3図、第4図図示の装入筒16は、上端に径
2rの円状開口18を有し下端に炉芯11を中心と
する(D+r)及び半径(D−r)の円軌跡と、
炉芯11から角度π/3の両放射線軌跡とで形成され る1/6円弧状開口19を有し、上端開口(原料流
入口)18から下端開口(原料流出口)19に向
つて原料通路面積が漸増するようにしたものであ
る。
The charging tube 16 shown in FIGS. 3 and 4 has a diameter at the upper end.
It has a circular opening 18 of 2r and has a circular locus of (D+r) and radius (D-r) centered on the furnace core 11 at the lower end,
It has a 1/6 arc-shaped opening 19 formed by both radiation trajectories at an angle π/3 from the furnace core 11, and a raw material passageway from the upper end opening (raw material inlet) 18 to the lower end opening (raw material outlet) 19. The area is gradually increased.

なお下端開口の周方向両端は第4図破線図示の
如くRにしても良い。
Note that both circumferential ends of the lower end opening may be rounded as shown by broken lines in FIG.

第5図、第6図図示の装入筒17は、内径2rの
円筒体22の下端に第3図、第4図の如き形状の
装入筒16を連結したものである。
The charging cylinder 17 shown in FIGS. 5 and 6 is constructed by connecting a charging cylinder 16 having a shape as shown in FIGS. 3 and 4 to the lower end of a cylindrical body 22 having an inner diameter of 2r.

なお第3図第5図において20は装入筒16,
17の上端に設けた水平フランジであり、仕切板
9とボルト、ナツト等で連結して、装入筒16,
17を吊下固定する。
In addition, in FIGS. 3 and 5, 20 indicates the charging cylinder 16,
It is a horizontal flange provided at the upper end of 17, and is connected to the partition plate 9 with bolts, nuts, etc., and is connected to the charging tube 16,
17 is suspended and fixed.

以上のような第3図、第4図(又は第5図、第
6図)の如き装入筒16(又は17)を、第1
図、第2図の従来の装入装置の装入筒10に替え
て配設することにより、第7図に示す如く、6本
の装入筒16の6つの円弧状下端開口19によつ
て、炉芯11を中心とする半径Dの円軌跡上に幅
2rのリング状原料排出口21が形成できる。
The charging cylinder 16 (or 17) as shown in FIGS. 3 and 4 (or FIGS. 5 and 6) is
By replacing the charging tube 10 of the conventional charging device shown in FIGS. , a width on a circular locus of radius D centered on the furnace core 11
A 2r ring-shaped raw material discharge port 21 can be formed.

またその時、第8図(又は第9図)の展開図に
示す如く装入筒16(又は17)の高さ方向全域
の装入筒16(又は17)相互間に、充分なる大
きさの炉芯部排ガス通路23が形成できる。
At that time, as shown in the developed view of FIG. 8 (or FIG. 9), a furnace of sufficient size is placed between the charging tubes 16 (or 17) over the entire height direction of the charging tubes 16 (or 17). A core exhaust gas passage 23 can be formed.

以上のように本考案は、装入筒の円弧状下端開
口群でリング状の原料排出口を形成するものであ
るから、各装入筒下端開口から排出される原料は
炉円周方向へ流れることなく炉半径方向の流れの
みとなり、炉半径方向の各位置の円周方向の原料
粒度偏析(粒度分布)が有効に防止できるもので
ある。
As described above, in the present invention, a ring-shaped raw material discharge port is formed by the group of arc-shaped lower end openings of the charging cylinder, so the raw material discharged from the lower end opening of each charging cylinder flows in the direction of the furnace circumference. The flow only occurs in the radial direction of the furnace, and the raw material particle size segregation (particle size distribution) in the circumferential direction at each position in the radial direction of the furnace can be effectively prevented.

また本考案は、上端開口から下端開口に向つて
原料通路面積が漸増する装入筒を用いるものであ
るから装入筒の高さ全域にわたつて隣接する装入
筒相互間に炉芯部排ガスの通路が形成されてい
る。
In addition, the present invention uses a charging tube in which the raw material passage area gradually increases from the upper end opening to the lower end opening, so that the exhaust gas from the furnace core is distributed between adjacent charging tubes over the entire height of the charging tube. A passageway has been formed.

これらの結果として還元ガスの吹込圧力の増大
や炉芯部排ガスの排出の困難性を招くことなく、
炉半径方向のガス流分布を円周方向で均一に維持
して必要還元ガス量を低位に維持することができ
るものである。
As a result, the reduction gas injection pressure does not increase or the exhaust gas from the furnace core becomes difficult to discharge.
The gas flow distribution in the radial direction of the furnace can be maintained uniformly in the circumferential direction, and the required amount of reducing gas can be maintained at a low level.

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

第1図、第2図は従来の竪型還元炉の原料装入
装置の説明図で、第2図は第1図のA−A断面
図、第3〜9図は本考案の原料装入装置の説明
図、第3図、第4図は本考案で使用する装入筒の
説明図、第7図は第3図、第4図又は第5図、第
6図の装入筒を採用したときの第1図竪型還元炉
のA−A矢視図、第8図、第9図は第3図、第4
図又は第5図、第6図の装入筒を採用したときの
装入筒の拡大展開断面図である。 1はコンベヤ、2は炉頂ホツパー、3はゲート
弁、4はシール弁、5はゲート弁、6はシール
弁、7は竪型還元炉、8は均排圧槽、9は仕切
板、10は装入筒、11は炉芯、12は貯留ホツ
パー、13は装入物、14は炉壁、15は排ガス
導出管、16は装入筒、17は装入筒、18は上
端開口、19は下端開口、20は水平フランジ、
21はリング状原料排出口、22は円筒体、23
は炉芯部排ガス通路。
Figures 1 and 2 are explanatory diagrams of a conventional raw material charging device for a vertical reduction furnace, Figure 2 is a sectional view taken along line A-A in Figure 1, and Figures 3 to 9 are illustrations of the raw material charging device of the present invention. An explanatory diagram of the device, Figures 3 and 4 are explanatory diagrams of the charging cylinder used in the present invention, and Figure 7 is an illustration of the charging cylinder used in Figures 3 and 4 or Figures 5 and 6. Figure 1 shows the vertical reduction furnace in the A-A direction, Figures 8 and 9 are shown in Figures 3 and 4.
FIG. 6 is an enlarged developed cross-sectional view of the charging tube when the charging tube shown in FIG. 5 or FIG. 6 is employed. 1 is a conveyor, 2 is a furnace top hopper, 3 is a gate valve, 4 is a seal valve, 5 is a gate valve, 6 is a seal valve, 7 is a vertical reduction furnace, 8 is an equalizing pressure tank, 9 is a partition plate, 10 11 is a furnace core, 12 is a storage hopper, 13 is a charge, 14 is a furnace wall, 15 is an exhaust gas outlet pipe, 16 is a charging cylinder, 17 is a charging cylinder, 18 is an upper end opening, 19 is the lower end opening, 20 is the horizontal flange,
21 is a ring-shaped raw material discharge port, 22 is a cylindrical body, 23
is the furnace core exhaust gas passage.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 竪型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、この仕切板に原料を流下せし
める装入筒を炉芯を中心とする同芯円軌跡上に等
間隔で、複数本吊下固定して上記炉内に貯留ホツ
パーを構成し、上記仕切板と装入筒の下端を頂点
とする装入物ストツクラインとの間に形成された
空間部の炉壁に排ガスの導出管を設けてなる竪型
還元炉の原料装入装置において、上記装入筒とし
て、少なくとも装入筒下部において下方に向つて
原料通路面積が漸増し、かつ下端に円弧状開口を
形成した装入筒を採用して上記円弧状開口群によ
り仕切板の下方の炉内に炉芯を中芯とする同芯リ
ング状の原料排出口を形成したことを特徴とする
竪型還元炉の原料装入装置。
A partition plate is installed in the upper interior of the vertical reduction furnace to form a storage space for the raw material, and a plurality of charging tubes for allowing the raw material to flow down the partition plate are arranged at equal intervals on a concentric circular locus centered on the furnace core. A storage hopper is formed in the furnace by fixing the main suspension, and the exhaust gas is led to the furnace wall in the space formed between the partition plate and the charge stock line with the bottom end of the charging cylinder as its apex. In a material charging device for a vertical reduction furnace provided with a tube, the material passage area gradually increases downward at least at the bottom of the charging tube, and an arcuate opening is formed at the lower end of the charging tube. Material charging of a vertical reduction furnace characterized by adopting a cylinder and forming a concentric ring-shaped material discharge port with the furnace core as the center core in the furnace below the partition plate using the group of circular arc-shaped openings. Device.
JP13447183U 1983-09-01 1983-09-01 Raw material charging device for vertical reduction furnace Granted JPS6043992U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13447183U JPS6043992U (en) 1983-09-01 1983-09-01 Raw material charging device for vertical reduction furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13447183U JPS6043992U (en) 1983-09-01 1983-09-01 Raw material charging device for vertical reduction furnace

Publications (2)

Publication Number Publication Date
JPS6043992U JPS6043992U (en) 1985-03-28
JPS6113913Y2 true JPS6113913Y2 (en) 1986-04-30

Family

ID=30302985

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13447183U Granted JPS6043992U (en) 1983-09-01 1983-09-01 Raw material charging device for vertical reduction furnace

Country Status (1)

Country Link
JP (1) JPS6043992U (en)

Also Published As

Publication number Publication date
JPS6043992U (en) 1985-03-28

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