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JPH0314883B2 - - Google Patents
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JPH0314883B2 - - Google Patents

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Publication number
JPH0314883B2
JPH0314883B2 JP14890783A JP14890783A JPH0314883B2 JP H0314883 B2 JPH0314883 B2 JP H0314883B2 JP 14890783 A JP14890783 A JP 14890783A JP 14890783 A JP14890783 A JP 14890783A JP H0314883 B2 JPH0314883 B2 JP H0314883B2
Authority
JP
Japan
Prior art keywords
charging
furnace
hopper
raw materials
raw material
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
JP14890783A
Other languages
Japanese (ja)
Other versions
JPS6043414A (en
Inventor
Mamoru Inoe
Takashi Miwa
Kenshiro Matsumoto
Toshifumi Kawagoe
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP14890783A priority Critical patent/JPS6043414A/en
Publication of JPS6043414A publication Critical patent/JPS6043414A/en
Publication of JPH0314883B2 publication Critical patent/JPH0314883B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/008Composition or distribution of the charge

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Iron (AREA)
  • Blast Furnaces (AREA)

Description

【発明の詳細な説明】 本発明は製鉄業における高炉への原料装入方法
に関し、詳しくは異形かつ粒径の異なる複数種の
原料を均一に混合して炉内に装入する方法に係わ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method of charging raw materials into a blast furnace in the steel industry, and more particularly, to a method of uniformly mixing a plurality of raw materials having irregular shapes and different particle sizes and charging the mixture into a blast furnace.

周知の如く高炉操業において、炉内における鉱
石類、コークスなどの装入物の炉内半径方向の原
料類粒度分布はその通気抵抗により燃料比などと
共に安定な操業を支配する主要な因子の一つであ
る。
As is well known, in blast furnace operation, the particle size distribution of the raw materials such as ore, coke, and other charges in the radial direction of the furnace is one of the main factors governing stable operation, along with the fuel ratio, due to its ventilation resistance. It is.

近年、原料事情により鉱石類の種類が多岐にわ
たり、焼結鉱、ペレツト、塊鉱石などが用いら
れ、これらを適宜混合して高炉に装入されてい
る。これら鉱石類の物理性状、たとえば形状は焼
結鉱、塊鉱石は角ばつた不規則な形をしている
が、ペレツトは表面が滑らかな球形状を呈してい
る。また、粒径については焼結鉱は24mm、ペレツ
トは11mm、および塊鉱石は14mm(いづれも平均粒
径)と大きく違つている。
In recent years, various types of ores have been used due to raw material conditions, such as sintered ores, pellets, lump ores, etc., and these are appropriately mixed and charged into a blast furnace. The physical properties of these ores are, for example, sintered ores, and lump ores have angular and irregular shapes, but pellets have a spherical shape with a smooth surface. In addition, the particle sizes are significantly different: sintered ore is 24mm, pellets are 11mm, and lump ore is 14mm (average particle size for each).

従つて、これらの鉱石類を均等に混合し、また
粒径も均一にして炉内に装入しなければ前述のよ
うな炉内における半径方向の分布制御は適正に行
なうことは不可能となるものである。
Therefore, unless these ores are mixed evenly and have a uniform particle size before being charged into the furnace, it will be impossible to properly control the radial distribution in the furnace as described above. It is something.

このような多種類の鉱石類原料を高炉へ装入す
る方法の従来例について説明すると、第1図に示
す如く焼結鉱ホツパー1A、ペレツトホツパー1
B、塊鉱石ホツパー1Cより各切出装置2によつ
てベルトコンベア3に切出され、焼結鉱4a、ペ
レツト4b、塊鉱石4cとブロツク毎に運搬され
てサージホツパー5内に装入され層状に貯蔵され
る。貯蔵された各種原料は切出装置6によつてベ
ルトコンベア7に切出され一応混合状態で炉頂へ
運搬される。他方還元剤であるコークスは、コー
クスホツパー8より切出装置9より前記ベルトコ
ンベア7に切出され切替シユート10を介して鉱
石類は貯蔵ホツパー11、コークスは貯蔵ホツパ
ー12に又は、両方の貯蔵ホツパー11,12に
交互に鉱石類とコークスが一旦貯留され流量調節
ゲート弁13によつて制御されながら交互に切出
され、炉内の旋回シユート14によつて炉内半径
方向に還元通気性が良好になるよう鉱石類、コー
クスと層状に分布装入されるものである。
To explain a conventional method of charging such various kinds of ore raw materials into a blast furnace, as shown in FIG.
B. The lump ore hopper 1C cuts out the lump ore to the belt conveyor 3 by each cutting device 2, and transports it block by block as sintered ore 4a, pellets 4b, and lump ore 4c, and charges it into the surge hopper 5 in layers. stored. The various stored raw materials are cut out onto a belt conveyor 7 by a cutting device 6 and transported to the top of the furnace in a mixed state. On the other hand, coke, which is a reducing agent, is cut out from a coke hopper 8 through a cutting device 9 to the belt conveyor 7, and via a switching chute 10, ores are stored in a storage hopper 11, coke is stored in a storage hopper 12, or both are stored. Ores and coke are stored alternately in hoppers 11 and 12, and are cut out alternately while being controlled by a flow rate regulating gate valve 13. Reduction ventilation is maintained in the radial direction inside the furnace by a rotating chute 14 inside the furnace. The ore and coke are distributed and charged in layers to ensure good quality.

しかしながら、このような装入方法は、次のよ
うな難点を有する。すなわち、前記のサージホツ
パー5、および炉頂の貯蔵ホツパー11,12に
一旦貯蔵するに際し、ベルトコンベアより落下装
入しホツパー内に堆積させる場合、粒径の大きい
ものは遠くへ落下し、粒径の小さいものは近くに
落下する。また、ホツパー内に堆積してゆく過程
で△山が形成され大径のものは転がり量が大きい
ため壁ぎわの円周方向に多く堆積し、小径のもの
は△山の中心部に多く堆積する。パーコレーシヨ
ン特にペレツトは表面がなめらかで球形であるた
め転がり量が大きいためそのほとんどが壁ぎわ円
周上に堆積する。このようにサージホツパーで偏
析し、さらに炉頂の貯蔵ホツパーで偏析を増幅し
た状態で切出され、旋回シユートで炉内での半径
方向における分布制御を行なつてもガス流の制御
は困難となるものである。
However, such a charging method has the following drawbacks. That is, when temporarily storing in the surge hopper 5 and the storage hoppers 11 and 12 at the top of the furnace, if the particles are dropped from the belt conveyor and deposited in the hoppers, particles with large diameters fall far away, and particles with small diameters Small objects fall nearby. In addition, in the process of being deposited in the hopper, △ peaks are formed, and large diameter particles roll over a large amount, so they accumulate in the circumferential direction along the wall, while small diameter particles accumulate in the center of the △ peaks. Percolation Pellets, in particular, have a smooth surface and are spherical, so they roll a lot, so most of them are deposited on the circumference of the wall. In this way, the gas segregates in the surge hopper and is cut out in a state where the segregation is amplified in the storage hopper at the top of the furnace, making it difficult to control the gas flow even if the distribution is controlled in the radial direction in the furnace using a rotating chute. It is something.

本発明は、このような実情に鑑み、炉頂の貯蔵
ホツパーに異形かつ粒径の異なる複数種の原料を
均一に混合するよう貯留させて、炉内に装入する
方法を提供するものであり、その特徴は各原料ホ
ツパーよりベルトコンベア上に各種原料を所定割
合で層状に積載して炉頂の貯蔵ホツパーに運び混
合状態で落下させるようにし、また貯蔵ホツパー
内での偏析を防止する方法として装入筒および整
流分配機構を介して装入貯留し、その後炉内に装
入するようにするものであり、この方法によつて
各原料および粒度が均一に混合されるので、炉内
での旋回シユートによる半径方向での装入分布制
御が容易に行えるものである。
In view of these circumstances, the present invention provides a method for storing a plurality of raw materials of irregular shapes and different particle sizes in a storage hopper at the top of the furnace so as to uniformly mix them, and charging the raw materials into the furnace. The feature is that various raw materials are stacked in a predetermined ratio on a belt conveyor from each raw material hopper and transported to the storage hopper at the top of the furnace and dropped in a mixed state, and as a method to prevent segregation in the storage hopper. The material is charged and stored through a charging tube and a rectification/distribution mechanism, and then charged into the furnace.This method allows each raw material and particle size to be mixed uniformly, so there is no problem in the furnace. The charging distribution can be easily controlled in the radial direction using the rotating chute.

以下実施例によつて本発明法を具体的に説明す
る。
The method of the present invention will be specifically explained below with reference to Examples.

まづ、各原料ホツパよりベルトコンベア上に各
種原料を所定割合で層状に切出す方法は、第2図
に示すように焼結鉱ホツパー1A、ペレツトホツ
パー1B、および塊鉱石ホツパー1Cの各切出し
装置2を高さ方向に差をつけ、ベルトコンベア3
上に積載するに当り1番下に焼結鉱4aを、次に
ペレツト4bを、そして1番上に塊鉱石4Cが層
状になるように切出し、積載して炉頂に運搬す
る。このような積載状態でコンベア3より落下さ
せると各種原料は均等に混合されて落下するもの
である。
First, the method of cutting out various raw materials in layers at a predetermined ratio onto a belt conveyor from each raw material hopper is as shown in FIG. with a difference in the height direction, belt conveyor 3
When loading on top, the sintered ore 4a is cut out in a layered manner, followed by pellets 4b at the bottom, and lump ore 4C at the top, loaded and transported to the top of the furnace. When the raw materials are dropped from the conveyor 3 in such a loaded state, the various raw materials are evenly mixed and dropped.

貯蔵ホツパー11への投入方法は、第3図に示
すように切替シユート(図示せず)を介して装入
筒15内を通つて落下するようにする。すなわ
ち、この装入筒を通るようにすることは粒径の大
きいものが遠くへ飛散することを防止し、混合状
態で落下するようにするためである。装入筒15
の中芯下方に、さらに整流分配機構を設ける。整
流分配機構は、上下開放の円筒状の整流筒16で
あり、前記装入筒15から落下した原料はまず(イ)
の如く整流筒16内に入り整流の役目をして下か
ら流出し(ロ)の如く堆積してゆく、整流筒16より
溢れた原料は円周上に堆積した(ロ)の上部に(ハ)の如
く流れ込みほとんど△山を形成しない、従つて粒
径の大きいものや球状のペレツトも転がらないた
め偏析を防止することが可能となり、混合状態で
貯留できるものである。尚、装入筒15および整
流筒16の下方先端部を適宜絞ることはそれぞれ
の効果がより発揮されるので好ましい。
The method of charging the material into the storage hopper 11 is to drop it through the charging tube 15 via a switching chute (not shown) as shown in FIG. That is, the purpose of passing through this charging tube is to prevent particles with large diameters from scattering far and to allow them to fall in a mixed state. Charging cylinder 15
A rectifying and distributing mechanism is further provided below the center core. The rectification/distribution mechanism is a cylindrical rectification cylinder 16 with an open top and bottom, and the raw material falling from the charging cylinder 15 is first
The raw material that overflows from the rectifying tube 16 enters the rectifying tube 16 and plays a rectifying role, flows out from below and is deposited as shown in (b). ), it flows in and hardly forms a Δ peak, and therefore, even large particles or spherical pellets do not roll, making it possible to prevent segregation and allowing them to be stored in a mixed state. Incidentally, it is preferable to appropriately narrow down the lower end portions of the charging tube 15 and the straightening tube 16 because the respective effects are more effectively exhibited.

整流分配機構の他の実施例について説明する
と、第4図に示す如く装入筒15の中芯下方にド
ーナツ状の整流板17を設ける。装入筒15より
落下し、整流板17の穴を通つて落下した原料
は、の如く堆積し、板に当つた原料はの如く
円周方向に落下し△山を形成しないので偏析を防
止できるものである。
Another embodiment of the rectifying and distributing mechanism will be described. As shown in FIG. 4, a donut-shaped rectifying plate 17 is provided below the center of the charging tube 15. The raw materials that fall from the charging tube 15 and fall through the holes in the rectifier plate 17 are deposited as shown, and the raw materials that hit the plate fall in the circumferential direction as shown, and do not form △ mountains, so segregation can be prevented. It is something.

このように装入された原料と、前記説明した従
来の方法で装入した原料を貯蔵ホツパーより切出
し炉内の旋回シユートよりどれだけ原料別に均等
に装入されているか調査した結果を第5図に示
す。
The raw materials charged in this way and the raw materials charged by the conventional method explained above were cut out from the storage hopper and the results of investigating how much of each raw material was evenly charged from the rotating chute in the furnace are shown in Figure 5. Shown below.

該第5図において縦軸は総排出量各原料割合
で、横軸は積算排出量である。SOは焼結鉱、P
はペレツトおよびSLは塊鉱石を示し、実線で本
発明の実施例で点線は比較例を示す。この図から
も明らかの如く従来法は各原料共大巾に偏析を起
していたが本発明法では、各原料共ほとんど偏析
を起さず所望通りの割合で炉内に投入されている
ことが明らかである。尚、本実施例では炉内への
装入を旋回シユートを説明したが、ベル式装入に
も適用できることは云うまでもない。また、従来
のサージホツパーを使用する場合は、サージホツ
パーに装入筒および整流分配機構を設け、層状に
積載された各原料をサージホツパーに装入して均
一に混合貯留し、しかる後、混合状態で切出しベ
ルトコンベアで炉頂の貯蔵ホツパーへ装入すれば
2段階で均一混合できるのでより効果的で好まし
い。
In FIG. 5, the vertical axis represents the proportion of each raw material in the total amount discharged, and the horizontal axis represents the cumulative amount discharged. SO is sintered ore, P
SL indicates pellets and SL indicates lump ore, solid lines indicate examples of the present invention, and dotted lines indicate comparative examples. As is clear from this figure, in the conventional method, each raw material was segregated to a wide extent, but in the method of the present invention, each raw material is charged into the furnace at the desired ratio without causing almost any segregation. is clear. In this embodiment, charging into the furnace was explained using a rotating chute, but it goes without saying that bell-type charging is also applicable. In addition, when using a conventional surge hopper, the surge hopper is equipped with a charging tube and a rectification/distribution mechanism, and each raw material loaded in layers is charged into the surge hopper, mixed and stored uniformly, and then cut out in a mixed state. It is more effective and preferable to charge the materials into the storage hopper at the top of the furnace using a belt conveyor because uniform mixing can be achieved in two stages.

以上詳細に説明したように本発明法によれば各
原料の切出し装置の簡単な改良、および貯蔵ホツ
パーも従来のホツパーに簡単な機構を付加するだ
けの構成で目的を達成できる利点を有し、しかも
各原料および粒度が均一に混合されるので、炉内
での旋回シユートによる半径方向での装入分布制
御によつてガス流の調整が容易にでき高炉の安定
操業、燃料比の低減に大きく寄与できる優れた発
明である。
As explained in detail above, the method of the present invention has the advantage that the purpose can be achieved by simply improving the cutting device for each raw material, and by simply adding a simple mechanism to the storage hopper of the conventional hopper. Moreover, since each raw material and particle size are mixed uniformly, the gas flow can be easily adjusted by controlling the charging distribution in the radial direction using the rotating chute inside the furnace, which greatly contributes to stable operation of the blast furnace and a reduction in the fuel ratio. This is an excellent invention that can contribute.

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

第1図は従来例を説明するための高炉への原料
装入系統図、第2〜第5図は本発明の実施例図
で、第2図は原料ホツパーからの原料切出し側面
図、第3図第4図は炉頂貯蔵ホツパー正断面図、
第5図は貯蔵ホツパーの総排出量各原料割合と積
算排出量の関係図である。 1A,1B,1C……原料ホツパー、2,6,
9……切出装置、3,7……ベルトコンベア、4
a,4b,4c……装入原料、5……サージホツ
パー、8……コークスホツパー、10……切替シ
ユート、11,12……炉頂貯蔵ホツパー、13
……流量調節ゲート弁、14……旋回シユート、
15……装入筒、16……整流筒、17……整流
板。
Fig. 1 is a system diagram of charging raw materials into a blast furnace to explain a conventional example, Figs. 2 to 5 are illustrations of embodiments of the present invention, Fig. 2 is a side view of raw material cut out from a raw material hopper, and Fig. 3 Figure 4 is a front cross-sectional view of the furnace top storage hopper.
FIG. 5 is a diagram showing the relationship between the total discharge amount of the storage hopper, the proportion of each raw material, and the cumulative discharge amount. 1A, 1B, 1C... Raw material hopper, 2, 6,
9... Cutting device, 3, 7... Belt conveyor, 4
a, 4b, 4c...Charging raw material, 5...Surge hopper, 8...Coke hopper, 10...Switching chute, 11, 12...Furnace top storage hopper, 13
...Flow control gate valve, 14...Swivel chute,
15... Charging tube, 16... Rectifying tube, 17... Rectifying plate.

Claims (1)

【特許請求の範囲】[Claims] 1 異形かつ粒径の異なる複数の鉱石類原料を炉
内に装入する方法において、各原料ホツパーより
ベルトコンベア上に各種原料を所定割合で層状に
積載して炉頂に運搬し、炉頂の貯蔵ホツパー内の
上部中央部に設けた装入筒と、該装入筒中芯下方
に設けた整流分配機構を介して同ホツパー内に装
入し貯留した後、炉内に装入することを特徴とす
る高炉への原料装入方法。
1 In a method of charging a plurality of ore raw materials with irregular shapes and different particle sizes into a furnace, various raw materials are stacked at a predetermined ratio on a belt conveyor from each raw material hopper and transported to the top of the furnace. It is characterized by charging into the storage hopper through a charging tube provided in the upper center of the storage hopper and a rectification/distribution mechanism provided below the core of the charging tube, storing it in the same hopper, and then charging it into the furnace. A method of charging raw materials into a blast furnace.
JP14890783A 1983-08-15 1983-08-15 Method for charging raw material to blast furnace Granted JPS6043414A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14890783A JPS6043414A (en) 1983-08-15 1983-08-15 Method for charging raw material to blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14890783A JPS6043414A (en) 1983-08-15 1983-08-15 Method for charging raw material to blast furnace

Publications (2)

Publication Number Publication Date
JPS6043414A JPS6043414A (en) 1985-03-08
JPH0314883B2 true JPH0314883B2 (en) 1991-02-27

Family

ID=15463328

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14890783A Granted JPS6043414A (en) 1983-08-15 1983-08-15 Method for charging raw material to blast furnace

Country Status (1)

Country Link
JP (1) JPS6043414A (en)

Also Published As

Publication number Publication date
JPS6043414A (en) 1985-03-08

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