JPH0772286B2 - Topless charging method for bellless blast furnace - Google Patents

Topless charging method for bellless blast furnace

Info

Publication number
JPH0772286B2
JPH0772286B2 JP63320501A JP32050188A JPH0772286B2 JP H0772286 B2 JPH0772286 B2 JP H0772286B2 JP 63320501 A JP63320501 A JP 63320501A JP 32050188 A JP32050188 A JP 32050188A JP H0772286 B2 JPH0772286 B2 JP H0772286B2
Authority
JP
Japan
Prior art keywords
charging
furnace
blast furnace
coke
ore
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 - Fee Related
Application number
JP63320501A
Other languages
Japanese (ja)
Other versions
JPH02166208A (en
Inventor
幹治 武田
昌治 宮川
義孝 澤
武 内山
Original Assignee
川崎製鉄株式会社
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
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Application filed by 川崎製鉄株式会社 filed Critical 川崎製鉄株式会社
Priority to JP63320501A priority Critical patent/JPH0772286B2/en
Publication of JPH02166208A publication Critical patent/JPH02166208A/en
Publication of JPH0772286B2 publication Critical patent/JPH0772286B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Blast Furnaces (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は炉内装入物の炉内円周方向の分布偏差を少なく
するようにしたベルレス高炉の炉頂装入方法に関し、特
に原料の装入位置や種類を3以上異ならせてコークスと
鉱石を層状に装入するベルレス高炉の炉頂装入方法に係
わる。
Description: TECHNICAL FIELD The present invention relates to a method for charging a furnace top of a bellless blast furnace, which reduces distribution deviation of furnace interior charges in the furnace circumferential direction, and particularly to charging of raw materials. It relates to a method for charging the top of a bellless blast furnace in which coke and ore are charged in layers by changing the charging positions and types by 3 or more.

〔従来の技術〕[Conventional technology]

第2図の高炉の原料装入によって生ずる高炉内円周方向
の鉱石/コークス(O/C)分布偏差の発生状況の一例を
示す高炉炉頂が縦断面図である。
FIG. 2 is a vertical cross-sectional view of the top of the blast furnace showing an example of the occurrence state of the ore / coke (O / C) distribution deviation in the circumferential direction of the blast furnace caused by charging the raw material of the blast furnace shown in FIG.

従来の高炉の原料装入は、対向して設置された複数の炉
頂バンカ1、2と、垂直シュート3と、変向の可能な旋
回シュート4を用いてなされている。
The raw material charging of the conventional blast furnace is performed by using a plurality of furnace top bunkers 1 and 2 which are installed to face each other, a vertical chute 3 and a swiveling chute 4 which can be turned.

垂直シュート3内を通過する原料は、どちらの炉頂バン
カ1,2から排出するかで、垂直シュート内の異なる位置
を落下のルートとして選び、その結果偏流を起こし炉内
円周方向に分布偏差を生ずる。すなわち、落下する原料
は、旋回シュート4上の異なる位置に落下するから、そ
の偏流の差だけシュート上での移動距離がd1,d2,と変動
し、これがため移動時間、シュートを離れる原料落下速
度、落下の軌跡が変動し、最終的には炉内堆積位置が変
動して装入物層の炉周方向の装入物の分布偏差、とりわ
け第2図のプロフィル中に見られるようなO/C分布の偏
差を生じるに至る。この場合、とりわけ原料の装入位置
を極端に偏らせた場合や原料の種類(粒径等)を大きく
変化させた場合に大きな偏差が現われる。
The raw material passing through the vertical chute 3 is selected as a dropping route at different positions in the vertical chute depending on which of the top bunkers 1 and 2 is discharged. As a result, a drift occurs and the distribution deviation in the circumferential direction of the furnace occurs. Cause That is, since the falling raw material falls to different positions on the swirling chute 4, the moving distance on the chute fluctuates as d 1 and d 2 due to the difference in the drift, which causes the moving time and the raw material leaving the chute. The fall velocity and the trajectory of the fall fluctuate, and finally the deposit position in the furnace fluctuates, and the distribution deviation of the charge in the peripheral direction of the charge layer, especially as seen in the profile of FIG. It leads to deviation of O / C distribution. In this case, a large deviation appears especially when the charging position of the raw material is extremely biased or when the type (particle size etc.) of the raw material is greatly changed.

以上の説明から判るように、コークス1種、鉱石1種を
装入する場合、2つの炉頂バンカ1、2のうち、一方か
ら鉱石を切り出し他方からはコークスを切出してこれを
交互に継続すると、炉周方向O/C分布に大きな偏りを生
ずる原因となる。
As can be seen from the above description, when charging one kind of coke and one kind of ore, if the ore is cut out from one of the two furnace top bunkers 1 and 2 and the coke is cut out from the other, the alternating operation is continued. , Causes a large deviation in O / C distribution in the furnace circumferential direction.

これらの問題を解決するため、実公昭59−5725では炉中
心軸上に排出口を有するホッパを二個垂直に配置した装
入装置を開示している。この装置では、円周方向のアン
バランスは解消するが、装入速度が低下する。また、装
置の高さが高くなるので設備費が増大するという問題を
有している。
In order to solve these problems, Japanese Utility Model Publication No. 59-5725 discloses a charging device in which two hoppers having discharge ports are vertically arranged on the central axis of the furnace. This device eliminates the circumferential unbalance but reduces the charging speed. Further, since the height of the device becomes high, there is a problem that equipment cost increases.

また、特公昭61−30993ではカットゲートを設けて垂直
シュート内の流れを絞って炉中心軸上に原料が落下する
ようにしている。特開昭53−102808では、垂直シュート
上部にコーンを設けて偏流を防止する方法が開示されて
いる。これらの技術は、いずれも原料の落下する流路を
著しく狭くすることにより、原料の落下軌跡を制御しよ
うとするものである。
In Japanese Patent Publication No. Sho 61-30993, a cut gate is provided to restrict the flow in the vertical chute so that the raw material falls on the central axis of the furnace. Japanese Patent Laid-Open No. 53-102808 discloses a method in which a cone is provided above a vertical chute to prevent drift. All of these techniques attempt to control the trajectory of the raw material by narrowing the flow path through which the raw material falls.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

原料の落下流路に偏流を防止する装置を付加する方法で
は、炉内分布偏差を完全になくすることは容易ではな
く、また完全になる程に防止装置を付加するとカットゲ
ート上、コーン上に棚つりをおこすという問題が生ず
る。つまり効果的に同心軸上に原料を落下させるには落
下流路を原料がつまった状態で流れるように著しく流路
を絞る必要がある。従って、原料の水分等が変動し、原
料の流れが悪くなると容易に詰りを生じ、安定的に原料
の装入を制御することは困難となる。
It is not easy to completely eliminate the distribution deviation in the furnace with the method of adding a device to prevent uneven flow in the falling flow path of the raw material, and if a preventive device is added to the extent that it becomes complete, it will be on the cut gate and cone. The problem of causing shelving arises. That is, in order to effectively drop the raw material on the concentric shaft, it is necessary to significantly narrow the flow passage so that the raw material flows in the falling flow passage in a clogged state. Therefore, if the water content of the raw material fluctuates and the flow of the raw material deteriorates, clogging easily occurs, and it becomes difficult to control the charging of the raw material in a stable manner.

本発明は原料の流路に偏流防止装置を設けるのではな
く、原料装入サイクルに変更を加えて炉内の分布偏差を
解消しようとするものである。
The present invention does not provide a drift prevention device in the flow path of the raw material, but tries to eliminate the distribution deviation in the furnace by changing the raw material charging cycle.

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明はベルレス高炉の炉頂装入方法において、炉頂バ
ンカを3個並列に設け、原料装入をコークス2装入鉱石
2装入の4回、又はコークス2装入鉱石3装入もしくは
コークス3装入鉱石2装入の5回の何れかとし、前記3
個のバンカに前記原料を同順に順番装入し高炉内に装入
することを特徴とするベルレス高炉の炉頂装入方法であ
る。
The present invention is a bell-less blast furnace top blasting method in which three bunker tops are provided in parallel, and raw material is charged four times with 2 coke 2 ore 2 or coke 2 ore 3 or coke. 3 charge ore 2 charge any of 5 times, the above 3
It is a method for charging the top of a bellless blast furnace, wherein the raw materials are sequentially charged in the same order into individual bunker and then charged into the blast furnace.

これを第1図によってさらに詳しく説明する。第1図は
3個並列に設けられた炉頂バンカの平面を模式的に示し
たものである。3個のバンカL、M、Nに対して、コー
クス(C)、鉱石(O)の装入回数をコークス1装入鉱
石1装入の2回、コークス2装入鉱石2装入の4回、又
はコークス2装入鉱石3装入の5回とすれば、バンカ
L、M、Nに入るC、Oは次のようになる。
This will be described in more detail with reference to FIG. FIG. 1 schematically shows a plane of three roof top bunker provided in parallel. Coke (C) and ore (O) were charged to the three bunkers L, M and N four times, one for coke 1 and one for ore 1 and 2 for ore 2 and coke 2. Or, if the charging of coke is 2 times and the charging of ore is 3 times, C and O entering the bunker L, M and N are as follows.

(a)装入回数を2回とした場合、 バンカ 装入物 I II L C O M O C N C O (b)装入回数を4回とした場合、 バンカ 装入物 I II III IV L C O O C M C C O O N O C C O (c)装入回数を5回とした場合、 バンカ 装入物 I II III IV V L C O C O O M C O O C O N O C O C O 〔作用〕 バンカをL、M、Nの3個とし、これに順次装入して順
次高炉内に排出するCとOの装入回数を第1図のように
3を除く2、4、5とすると、各装入回数を3連続繰返
すと1サイクルとなり、この1サイクルにおいて、各バ
ンカはそれぞれ互いに位相が異なる順序で同順にCとO
を受け入れ排出することとなる。従って、各装入時に、
各バンカによる偏流があっても、1サイクルをとって見
れば炉内装入物分布は各方向に均質化される。
(A) When the number of times of charging is two, the bunker charge I II L C O M O C N C O (b) When the number of times of charging is four, the bunker charge I II III IV L C C O C M C C C O O N O C C O (c) When the charging number is 5, the bunker charge I II III IV V L C O C O O M C O O C O N O C O C O [Action] Three bunker L, M, N are sequentially charged into the bunker and discharged sequentially into the blast furnace. Except for 3 as shown in Fig. 1, 2 4 and 5, one cycle is obtained by repeating the charging times three times in succession, and in this one cycle, the bunker has the phases C and O in the same order in the mutually different phases.
Will be accepted and discharged. Therefore, at the time of each charging,
Even if there is a drift due to each bunker, the distribution of the contents in the furnace interior is homogenized in each direction when viewed from one cycle.

さらに炉頂バンカの個数を3個とするのは次の理由によ
る。通常炉頂バンカは2個180゜対角方向に設置されて
おり、排出方向を軸として対称となっている。2個のバ
ンカで装入回数を(C↓C↓O↓)(コークス2装入鉱
石1装入)もしくは(C↓O↓O↓)(コークス1装入
鉱石2装入)の3回とするとC、Oの分率の分布は均一
化されるが、量的な不均一性が180゜毎に残る。これに
対し、3〜4個の炉頂バンカを設けると120゜毎、90゜
毎と不均一性が解消される。一方、4個のバンカを炉頂
に設けるには、炉頂部のバンカの取付けスペース、排出
弁の取合いが難しく、設備費が過大となる。また、2個
のバンカでは、装入回数が限られ、高生産時にはC↓O
↓O↓(コークス1装入、鉱石2装入)が困難となる。
以上の理由により炉頂バンカの個数は3個にする必要が
ある。
Furthermore, the number of furnace top bunker is set to 3 for the following reason. Normally, two furnace bunkers are installed 180 ° diagonally and symmetrical about the discharge direction. With two bunker, the number of times of charging is (C ↓ C ↓ O ↓) (coke 2 charged ore 1 charged) or (C ↓ O ↓ O ↓) (coke 1 charged ore 2 charged) 3 times Then, the distribution of C and O fractions is made uniform, but quantitative non-uniformity remains every 180 °. On the other hand, if three or four furnace top bunkers are installed, the unevenness can be eliminated every 120 ° and 90 °. On the other hand, if four bunkers are provided on the top of the furnace, it is difficult to fit the space for installing the bunkers on the top of the furnace and the exhaust valve, and the equipment cost becomes excessive. Also, with two bunker, the number of times of charging is limited, and C ↓ O during high production.
↓ O ↓ (1 charge of coke, 2 charges of ore) becomes difficult.
For the above reasons, the number of furnace top bunker must be three.

装入回数2(C↓O↓)(コークス1装入、鉱石1装
入)に比較すると装入回数4(C↓C↓O↓O↓)(コ
ークス2装入、鉱石2装入)はより多くの装入モードが
可能になりより望ましい形態である。すなわちコークス
装入C↓の1回目、2回目で異なった装入物の使用が可
能であり、例えば1回目のコークス装入C↓には大粒径
高品質のコークス、2回目のコークス装入C↓には小粒
径、低品質のコークスのように使い分けることにより原
料のコスト低減が可能となる。鉱石についても同様であ
る。
Charge number 4 (C ↓ C ↓ O ↓ O ↓) (coke 2 charge, ore 2 charge) compared to charge number 2 (C ↓ O ↓) (coke 1 charge, ore 1 charge) More charging modes are possible, which is a more desirable form. That is, it is possible to use different charging materials in the first and second coke charging C ↓. For example, in the first coke charging C ↓, a large particle size high quality coke and a second coke charging are used. It is possible to reduce the cost of raw materials by selectively using small particle size and low quality coke for C ↓. The same applies to ore.

装入回数5(C↓C↓O↓O↓O↓)(コークス2装
入、鉱石3装入)、または(C↓C↓C↓O↓O↓)
(コークス3装入、鉱石2装入)は、装入方法としては
望ましいが、生産量によっては回数を5回にすることに
より装入回数が少なくなるという問題を抱えている。こ
のような多機能を発揮するためにもバンカは最低3個、
装入回数は4、5がより望ましい形態である。
Charges 5 (C ↓ C ↓ O ↓ O ↓ O ↓) (2 coke charges, 3 ore charges), or (C ↓ C ↓ C ↓ O ↓ O ↓)
Although (coke 3 charging, ore 2 charging) is desirable as a charging method, it has a problem that the number of charging is reduced by setting the number of times to 5 depending on the production amount. At least 3 bunkers are needed to achieve such multi-functionality.
A more desirable form is 4 and 5 times.

〔実施例〕〔Example〕

炉容積4300m3の高炉において、1サイクル内の装入回数
を4回とする本発明の実施をした。第3図(a)に示す
高炉5の炉上部の円周方向の均一性を表わす8個のスキ
ンフロー温度計6の偏差σの変化を第3図(b)に示し
た。
The present invention was carried out in a blast furnace having a furnace volume of 4300 m 3 with the number of charging times being 4 in one cycle. FIG. 3 (b) shows changes in the deviation σ of the eight skin flow thermometers 6 representing the circumferential uniformity of the upper part of the blast furnace 5 shown in FIG. 3 (a).

本発明の実施後急激に偏差が減少し、約1/3となってい
る。また、第3図(b)、(c)、(d)に示すように
溶銑温度、[Si]の変動が減少しており、円周方向の不
均一性が解消したことがわかる。また、溶銑温度の変動
が減少したため平均溶銑温度の低下が可能となり、溶銑
温度が約1493℃まで低下している。この結果、[Si]が
0.2%低下しており、このことによる経済的効果は著し
いものがある。
After implementing the present invention, the deviation sharply decreases to about 1/3. Further, as shown in FIGS. 3 (b), (c), and (d), the changes in the hot metal temperature and [Si] are reduced, and it can be seen that the non-uniformity in the circumferential direction is eliminated. Moreover, since the fluctuation of the hot metal temperature is reduced, the average hot metal temperature can be lowered, and the hot metal temperature is lowered to about 1493 ° C. As a result, [Si]
It has decreased by 0.2%, and the economic effect of this is remarkable.

〔発明の効果〕〔The invention's effect〕

本発明によれば、ベルレス高炉に特有の高炉円周方向の
温度の不均一性を解消することができ結果として溶銑中
[Si]、溶銑温度の出銑口毎の偏差を解消することがで
きる。
According to the present invention, it is possible to eliminate the non-uniformity of the temperature in the circumferential direction of the blast furnace, which is peculiar to the bellless blast furnace, and as a result, it is possible to eliminate the deviation between the hot metal [Si] and the hot metal temperature for each tap hole. .

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

第1図は本発明方法の実施例のサイクルの内容を示す説
明図、第2図はベルレス高炉の炉頂付近の縦断面図、第
3図は本発明の効果を示すグラフである。 1、2……炉頂バンカ、3……垂直シュート 4……旋回シュート、5……高炉 6……スキンフロー温度計 L、M、N……バンカ、C……コークス O……鉱石
FIG. 1 is an explanatory view showing the contents of a cycle of an embodiment of the method of the present invention, FIG. 2 is a vertical sectional view of the vicinity of the top of a bellless blast furnace, and FIG. 3 is a graph showing the effect of the present invention. 1, 2 …… Burker on the top of the furnace, 3 …… Vertical chute 4 …… Swirl chute 5 …… Blast furnace 6 …… Skinflow thermometer L, M, N …… Bunker, C …… Coke O …… Ore

フロントページの続き (72)発明者 内山 武 千葉県千葉市川崎町1番地 川崎製鉄株式 会社技術研究本部内 (56)参考文献 特開 昭63−100113(JP,A)Front Page Continuation (72) Inventor Takeshi Uchiyama 1 Kawasaki-cho, Chiba-shi, Chiba Kawasaki Steel Co., Ltd. Technical Research Headquarters (56) Reference JP-A-63-100113 (JP, A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】ベルレス高炉の炉頂装入方法において、炉
頂バンカを3個並列に設け、原料装入をコークス2装入
鉱石2装入の4回、又はコークス2装入鉱石3装入もし
くはコークス3装入鉱石2装入の5回の何れかとし、前
記3個のバンカに前記原料を同順に順番に装入し高炉内
に装入することを特徴とするベルレス高炉の炉頂装入方
法。
1. A method for charging a bell-less blast furnace, wherein three furnace bunkers are provided in parallel, and raw materials are charged four times by charging two cokes and two ores, or charging two cokes and two ores. Alternatively, the coke 3 charging ore 2 charging is performed 5 times, and the raw materials are charged in the same order in the same order in the 3 bunker and charged into the blast furnace. How to enter.
JP63320501A 1988-12-21 1988-12-21 Topless charging method for bellless blast furnace Expired - Fee Related JPH0772286B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63320501A JPH0772286B2 (en) 1988-12-21 1988-12-21 Topless charging method for bellless blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63320501A JPH0772286B2 (en) 1988-12-21 1988-12-21 Topless charging method for bellless blast furnace

Publications (2)

Publication Number Publication Date
JPH02166208A JPH02166208A (en) 1990-06-26
JPH0772286B2 true JPH0772286B2 (en) 1995-08-02

Family

ID=18122155

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63320501A Expired - Fee Related JPH0772286B2 (en) 1988-12-21 1988-12-21 Topless charging method for bellless blast furnace

Country Status (1)

Country Link
JP (1) JPH0772286B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BR112013028519B8 (en) * 2011-05-31 2019-09-17 Nippon Steel & Sumitomo Metal Corp cargo loading apparatus for a blast furnace in a coneless loading apparatus and method of loading cargo in a blast furnace using said cargo loading apparatus
JP6515285B2 (en) * 2015-07-10 2019-05-22 日本製鉄株式会社 Raw material charging method for blast furnace

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63100113A (en) * 1986-10-16 1988-05-02 Nkk Corp Bell-less charging apparatus in blast furnace

Also Published As

Publication number Publication date
JPH02166208A (en) 1990-06-26

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