JPS60251208A - Method for charging raw material to blast furnace - Google Patents

Method for charging raw material to blast furnace

Info

Publication number
JPS60251208A
JPS60251208A JP10703184A JP10703184A JPS60251208A JP S60251208 A JPS60251208 A JP S60251208A JP 10703184 A JP10703184 A JP 10703184A JP 10703184 A JP10703184 A JP 10703184A JP S60251208 A JPS60251208 A JP S60251208A
Authority
JP
Japan
Prior art keywords
raw material
hopper
furnace
charged
chute
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.)
Pending
Application number
JP10703184A
Other languages
Japanese (ja)
Inventor
Yoshio Takei
竹井 良夫
Takeichi Iwanaga
岩永 竹市
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 JP10703184A priority Critical patent/JPS60251208A/en
Publication of JPS60251208A publication Critical patent/JPS60251208A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace

Landscapes

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

Abstract

PURPOSE:To attain a satisfactory and stable furnace condition by storing separately or superposedly, for example, coarse grained raw material and fine- grained raw material in a hopper, discharging separately and successively the coarse-grained raw material and the fine-grained raw material from the hopper in one batch and charging the raw materials to the respective desired positions via a chute in the furnace. CONSTITUTION:The raw material from a charging belt conveyor 1 is classified by a classifying damper 14. The coarse-grained raw material 12 is charged into the inside cylindrical part 15 of the upper hopper 3 and is further charged into the inside cylindrical part 15' of the lower hopper 6 and is stored therein. The fine-grained raw material 13 is charged into the outside cylindrical part 16 of the upper hopper 3 and is further charged into the outside cylindrical part 16' of the lower hopper 6 and is stored therein. The pressure in the hopper 6 is equalized and thereafter a gate valve 7 and a lower seal valve 8 are opened to discharge first the material 12 in the part 15' into the chute 9 in the furnace. Said material is charged into the desired position in the furnace by the swiveling and tilting operation of the chute. The raw material 13 in the part 16' is similarly charged into the furnace in succession thereto.

Description

【発明の詳細な説明】 (産業上の利用分野〕 本発明は、ベルレス式装入装置による高炉への原料装入
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a method for charging raw materials into a blast furnace using a bellless charging device.

(従来技術) 高炉におけるベルレス式装入装置においては、含鉄鉱石
、コークス等の原料はホッパーからシュートを介して炉
内に装入されるように々つており、シューi・の旋回、
傾動によって原料の落下位置を変えることにより、炉内
における鉱石/コークスの比、ガス流分布等を制御し所
望の炉況を得るようにしている。
(Prior art) In a bell-less charging device for a blast furnace, raw materials such as iron-bearing ore and coke are charged into the furnace from a hopper via a chute.
By changing the falling position of the raw materials by tilting, the ore/coke ratio, gas flow distribution, etc. in the furnace are controlled to obtain desired furnace conditions.

そして近年、例えば特開昭55−62106号の発明に
見られるように特に炉内のガス流分布を制御する目的で
、装入原料を予め粗粒と細粒とに分は粗粒は炉中心部に
、細粒は炉壁周辺部に装入するという方法が普及されつ
つある。
In recent years, for example, as seen in the invention of JP-A No. 55-62106, for the purpose of particularly controlling the gas flow distribution in the furnace, the charging raw material is divided into coarse particles and fine particles in advance, and the coarse particles are placed in the center of the furnace. In recent years, a method of charging fine grains around the furnace wall is becoming popular.

第4図は、従来の粒度別装入の代表例を示すものであり
、この従来の原料装入方法においては、粗粒原料12を
装入ベルトコンベヤー1.旋回シュート?、上部ホッパ
ー3を経て排圧された下部ホッパー6に排出貯蔵し、均
圧したのち下部ホッパー6から炉内シュート9を介して
その旋回と傾動操作によって炉内に装入し、炉内に12
’の様な原料分布を形成する。
FIG. 4 shows a typical example of conventional charging according to particle size. In this conventional raw material charging method, coarse grain raw material 12 is charged onto a belt conveyor 1. Rotating chute? After passing through the upper hopper 3 and storing it in the lower hopper 6, which is evacuated, the pressure is equalized, and then charged into the furnace from the lower hopper 6 through the furnace chute 9 by rotating and tilting the furnace.
Forms a raw material distribution like '.

つぎに排圧系統11を操作し7て、下部ホッパー6の排
圧を行ない装入ベルトコンベヤー1.旋回シュート2を
経て上部ホッパー3に貯蔵されている細粒原料13を下
部ホッパー6に排出貯蔵し、均圧系10を操作してホッ
パー6の均圧を行なったのちホッパ−6下部のゲート弁
7.下部シール弁8を開けて炉内シュート9を介して、
その旋回と傾動により炉内に装入し、13’の様な原料
分布を形成するようになっている。
Next, the exhaust pressure system 11 is operated to evacuate the lower hopper 6 and the charging belt conveyor 1. The fine raw material 13 stored in the upper hopper 3 via the rotating chute 2 is discharged and stored in the lower hopper 6, and after the pressure equalization system 10 is operated to equalize the pressure in the hopper 6, the gate valve at the bottom of the hopper 6 is activated. 7. Open the lower seal valve 8 and feed through the furnace chute 9.
By rotating and tilting the material, it is charged into the furnace and a raw material distribution as shown in 13' is formed.

この従来の装入方法においでは、粗粒原料12と細粒原
料13とを分は夫々1バツチ(ホッパーの均圧、排圧操
作の1サイクルを意味し、以下1バツチという)で装入
するため、バッチ数が倍増し、下部ホッパー6の均圧、
排圧操作が増え給米として炉内シュート9から炉内への
原料装入可能時間が減少することになり、炉内シュート
の旋回数も少なくせざるを得す、炉内への原料装入分布
のきめ細かい制御が困難である等の難点がある。
In this conventional charging method, the coarse raw material 12 and the fine raw material 13 are each charged in one batch (meaning one cycle of hopper pressure equalization and pressure evacuation operation, hereinafter referred to as one batch). Therefore, the number of batches is doubled, and the pressure in the lower hopper 6 is equalized.
The increase in exhaust pressure operation reduces the time available for charging raw material from the furnace chute 9 into the furnace as rice feed, and the number of revolutions of the furnace chute must also be reduced. There are drawbacks such as difficulty in finely controlling the distribution.

なお、この場合において、旋回数を多くすると原料の装
入能力が低下する。特に二段垂直ホッパー型のベルレス
式装入装置においてその影響が犬である。
In this case, increasing the number of revolutions will reduce the raw material charging capacity. This is particularly true for bellless charging systems with two-stage vertical hoppers.

(発明が解決しようとする問題点) 本発明は、ベルレス式装入装置を有する高炉において、
例えば原料を粗粒と細粒に分けて装入する場合の前記従
来方法における難点を改善し炉内シュート旋回数を多く
し、かつ必要装入能力を有オリに確保し、炉内への装入
原料分布のきめ細かい制御を可能とするものであり、原
料装入効率全良好とし、良好でかつ安定した炉況を形成
し、高炉操業成りヤ犬巾に改畳するものである。
(Problems to be Solved by the Invention) The present invention provides a blast furnace having a bellless charging device.
For example, by improving the drawbacks of the conventional method when charging raw materials separately into coarse particles and fine particles, increasing the number of rotations of the chute in the furnace, and ensuring the required charging capacity, it is possible to charge the raw material into the furnace. This enables fine control of the distribution of raw materials, improves raw material charging efficiency, creates good and stable furnace conditions, and improves blast furnace operation.

(問題点を解決するための手段プ 本発明の特徴は、ホッパー内に例えば粗粒原料と細粒原
料を分離するか又は重ねて貯蔵し、1バツチで粗粒原料
と細粒原料とを別々に順次ホッパーから排出し・炉内シ
ュートを介1〜でそれぞれ炉内 3− の所望位置に装入するようにしたところにある。
(Means for Solving the Problems) A feature of the present invention is that, for example, coarse grain raw materials and fine grain raw materials are stored separately or stacked in a hopper, and coarse grain raw materials and fine grain raw materials are separated in one batch. The materials are sequentially discharged from the hopper and charged to desired positions in the furnace through the in-furnace chutes 1 to 3, respectively.

以下本発明の実施例を第1図に示す本発明を実施するた
めのベルレス装入装置例と共に説明する。
Embodiments of the present invention will be described below along with an example of a bellless charging device for carrying out the present invention shown in FIG.

この本発明を実施するためのベルレス装入装置例におい
ては、装入ベルトコンベヤー1と旋回シュート2′との
間に分級ダンパー14を設け、旋回シュート2′は旋回
部札と直筒部ば□からなっている。
In this example of a bellless charging device for carrying out the present invention, a classification damper 14 is provided between the charging belt conveyor 1 and the rotating chute 2', and the rotating chute 2' is connected to the rotating part and the straight cylinder part. It has become.

父上部ホッパー3と下部ホッパー6内には、夫々内筒部
15 、15’と外筒部16,16’が設けられ、この
内筒部15 、15’の下部には夫々可動リング1 ’
i’ 、 1 ’i”が装着されている。
Inner cylinder parts 15, 15' and outer cylinder parts 16, 16' are provided in the upper hopper 3 and lower hopper 6, respectively, and a movable ring 1' is provided at the lower part of the inner cylinder parts 15, 15', respectively.
i', 1 'i' is attached.

かくして本発明においては・装入ベルトコンベヤーlか
らの原料(含鉄鉱石の場合を例とし以下原料という。)
は分級ダンパー14により分級され、粗粒原料12(例
えば粒径10wn以上のもの)は旋回シュート/の直筒
部2′lを通って上部ホッパー3の内面部15内に投入
、貯蔵され、細粒原料13(例えば粒径5〜10.mの
もの〕は旋回部札全通−4= って上部ホッパ−30外筒部16内に投入、貯蔵される
。これらの粗粒原料12と細粒原料13が1バッチ操作
で炉内に装入される単位となる。
Thus, in the present invention: - Raw material from the charging belt conveyor l (hereinafter referred to as raw material, taking the case of iron-containing ore as an example);
is classified by the classification damper 14, and the coarse raw material 12 (for example, those with a particle size of 10wn or more) is fed into the inner surface 15 of the upper hopper 3 through the straight cylinder part 2'l of the rotating chute and stored. The raw material 13 (for example, those with a particle size of 5 to 10.m) is fed into the outer cylindrical portion 16 of the upper hopper 30 and stored in the rotating section. The raw material 13 is a unit charged into the furnace in one batch operation.

そして、上部ホッパ−3下部のゲート弁4.上部シール
弁5を開き、先ず内筒部15内の粗粒原料12を下部ホ
ッパー6の内筒部15′内に排出。
And the gate valve 4 at the bottom of the upper hopper 3. The upper seal valve 5 is opened, and first, the coarse raw material 12 in the inner cylinder part 15 is discharged into the inner cylinder part 15' of the lower hopper 6.

貯蔵し、内筒部15′内先、粗粒原料を排出完了後又は
完了直前に上部ホッパー3の内筒部15下部の可動リン
グ1′7を上方に移動し、外筒部16内の細粒原料13
を下部ホッパー6の内筒部ld内の粗粒原料12の頂部
を経て外筒部16/内に排出。
After or just before the completion of discharging the coarse raw material inside the inner cylinder part 15', the movable ring 1'7 at the lower part of the inner cylinder part 15 of the upper hopper 3 is moved upward to remove the fine particles in the outer cylinder part 16. Grain raw material 13
is discharged through the top of the coarse raw material 12 in the inner cylinder part ld of the lower hopper 6 into the outer cylinder part 16/.

貯蔵し、上部ホッパ−3下部のゲート弁4.上部シール
弁5を閉じる。
Storage, upper hopper 3 lower gate valve 4. Close the upper seal valve 5.

ついで、下部ホッパー6内を均圧してのち下部ホッパ−
6下部のゲート弁7.下部シール弁8を開き、先ず下部
ホッパ−60内筒部15′内の粗粒原料12を1円シュ
ート9に排出し、炉内シュート9の旋回と傾動操作によ
り、炉内の所望位置に装入し所望の原料分布12’−i
z影形成る。内筒部15’内から粗粒原料12を排出完
了後又は、完了直前に下部ホッパー6の内筒部15/下
部の可動リング1′2′を」ニガに移動し、外筒部16
′内の細粒原料13を炉内シュート9に排出し、炉内シ
ュート9の旋回と傾動操作により炉内の所望位置に装入
し、所望の原料分布13’を形成し、下部ホッパー6 
下部のゲート弁7.下部シール弁8fc閉じて1バッチ
操作を完了する。
Then, after equalizing the pressure inside the lower hopper 6, the lower hopper
6 Lower gate valve 7. The lower seal valve 8 is opened, and the coarse raw material 12 in the inner cylindrical part 15' of the lower hopper 60 is first discharged into the 1-yen chute 9, and then loaded into the desired position in the furnace by rotating and tilting the furnace chute 9. Input desired raw material distribution 12'-i
z Shadow formation. After or just before the completion of discharging the coarse raw material 12 from inside the inner cylinder part 15', move the inner cylinder part 15/lower movable ring 1'2' of the lower hopper 6 to the outer cylinder part 16.
' The fine raw material 13 in the furnace is discharged into the furnace chute 9, and charged at a desired position in the furnace by rotating and tilting the furnace chute 9 to form a desired raw material distribution 13'.
Lower gate valve7. Close the lower seal valve 8fc to complete one batch operation.

このようにして粗粒原料12と細粒原料13を上部ホッ
パー3.下部ホッパー6内に区分して貯蔵し、1バッチ
操作の中で・粗粒原料12と細粒原料13を別々に下部
ホッパー6から炉内シュートを介して炉内の夫々の所望
位置に装入して所望の原料分布12’、13’を形成す
るものである。
In this way, the coarse raw material 12 and the fine raw material 13 are transferred to the upper hopper 3. They are stored separately in the lower hopper 6, and during one batch operation, the coarse raw material 12 and the fine raw material 13 are separately charged from the lower hopper 6 to their respective desired positions in the furnace via the furnace chute. In this way, a desired raw material distribution 12', 13' is formed.

第2図および第3図は、本発明を実施するための他のベ
ルレス装入装置例を示すものであり、主に上部ホッパー
3.下部ホッパー6における粗粒原料12と細粒原料1
3の貯蔵区分および排出形態の変形例を示すものである
2 and 3 show another example of a bellless charging device for carrying out the present invention, which mainly includes an upper hopper 3. Coarse raw material 12 and fine raw material 1 in lower hopper 6
3 shows a modification of the storage section and discharge form of No. 3.

即ち、第2図に示したものは、上部ホッパー3内を粗粒
原料12の貯蔵部と細粒原料13の貯蔵部に区分し、そ
れぞれにゲート弁4と上部シール弁5を設け、それイ1
れの貯蔵部の位置に対応して下部ホッパー6内に粗粒原
料12の貯蔵部と細粒原料13の貯蔵部を区分して設け
ると共にこの両貯蔵部間にホッパー内ゲート弁18を介
在させ、更に共通のゲート弁7と下部シール弁8を設け
たものである。
That is, in the case shown in FIG. 2, the inside of the upper hopper 3 is divided into a storage area for the coarse raw material 12 and a storage area for the fine raw material 13, and each is provided with a gate valve 4 and an upper seal valve 5. 1
Corresponding to the positions of these storage parts, a storage part for coarse grain raw material 12 and a storage part for fine grain raw material 13 are separately provided in the lower hopper 6, and an in-hopper gate valve 18 is interposed between these two storage parts. , further provided with a common gate valve 7 and lower seal valve 8.

又第3図に示したものは、上部ホッパー3内を粗粒原料
貯蔵部と複数の細粒原料貯蔵部に区分し、それぞれにゲ
ート弁4.上部シール弁5を設け、このそれぞれの貯蔵
部の位置に対応して下部ホッパー6内に粗粒原料の貯蔵
部と細粒原料の貯蔵部を区分して設けると共に粗粒原料
の貯蔵部と細粒原料の貯蔵部間に可動リング17′を設
け、共通の−マ − ゲート弁マ、下部シール弁8を設けたものである。
Also, in the one shown in FIG. 3, the inside of the upper hopper 3 is divided into a coarse raw material storage section and a plurality of fine grain raw material storage sections, each of which is provided with a gate valve 4. An upper seal valve 5 is provided, and a coarse raw material storage area and a fine raw material storage area are separately provided in the lower hopper 6 corresponding to the positions of the respective storage areas. A movable ring 17' is provided between the granular raw material storage sections, and a common -margate valve and lower seal valve 8 are provided.

力お実施例においては、粗粒原料12はホラ、+−3、
ホッパー6の円筒部15.15’に貯蔵し、細粒原料は
外筒部16.16’に貯蔵し、粗粒原料排出後、細粒原
料を排出するようにしているが、この貯蔵位置関係、排
出順序は随時必要に応じて任意に変更できるようにする
のが有効である。又、原料は含鉄鉱石を例としたが、コ
ークスその他の原料にも適用できることはいうまでもな
い。又、炉頂への原料搬送がベルトコンベヤーlによっ
て行表われ分級ダンパー14で分級してホッパー3に投
入するようになっているが、スキップカーによる場合も
適用可能であり、又他の分級手段を構するとともできる
In the practical example, the coarse raw material 12 is a hora, +-3,
The raw materials are stored in the cylindrical portion 15.15' of the hopper 6, and the fine raw materials are stored in the outer cylindrical portion 16.16', and after the coarse raw materials are discharged, the fine raw materials are discharged. It is effective to allow the discharge order to be changed arbitrarily as needed. Further, although iron-containing ore is used as an example of the raw material, it goes without saying that the present invention can also be applied to coke and other raw materials. In addition, the raw material is conveyed to the top of the furnace by a belt conveyor 1, classified by a classification damper 14, and then fed into the hopper 3, but it is also possible to use a skip car, or other classification means can be used. You can also do it by setting up.

更に前記実施例においては、粒度別装入を例としている
が、例えば銘柄別装入にも適用可能であり、粒度別装入
の場合も含みホッパーから異極原料を同時に排出して、
混合し炉内に装入すること 8− も可能である。
Further, in the above embodiments, charging by particle size is taken as an example, but it is also applicable to charging by brand, for example, and includes the case of charging by particle size, in which different polarity raw materials are simultaneously discharged from the hopper,
It is also possible to mix and charge the mixture into the furnace.

(発明の効果) 本発明による装入方法においては、粗粒原料と細粒原料
を排圧、均圧操作の1サイクルの中で、粒度あるいは銘
柄の異なった原料の装入ができ、炉内シュートの旋回数
を多くして高炉々内原料分布をきめ細かく制御すること
ができるので炉内のガス流分布を理想的に形成すること
ができる。したがって原料表人効率も良好でめり炉況を
良好にかつ安定させることができ、高炉操業成、4tを
大巾に改善することができる。
(Effects of the Invention) In the charging method according to the present invention, raw materials of different particle sizes or brands can be charged into the furnace within one cycle of evacuation and pressure equalization operations for coarse grain raw materials and fine grain raw materials. By increasing the number of revolutions of the chute, it is possible to finely control the distribution of raw materials in the blast furnaces, so that the gas flow distribution in the furnaces can be ideally formed. Therefore, the raw material efficiency is also good, the conditions in the milling furnace can be made good and stable, and the production capacity of the blast furnace can be greatly improved by 4 tons.

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

第1図、第2図、第3図は本発明による高炉への原料装
入方法ヲ英雄するためのベルレス式装入装置例を示す縦
断面説明図、第4図は従来の尚炉への原料装入方法を実
施するためのベルレス式装入装置例を示す縦断面説明図
である。 1・ ・・・・・ベルトコンベヤー 2・・・・ ・・シュート 3・・・ ・・・上部ホッパー 4・・・・・・ゲート弁 5・・・・・・上部シール弁 6・・・・・・下部ホッパー ?・・ ・・・・ゲート弁 8・・・・・・下部シール弁 9・・・・・・炉内シュート lO・・・・・均圧系 11・・・・・排圧系 12・・・・・粗粒原料 13・・・・・細粒原料 14・・・・・分級ダンパー 15・・・・・上部ホッパーの内筒部 15・・・・・下部ホッパーの内筒部 16・・・・・上部ホッパーの外筒部 16′・・・・・下部ホッパー〇外筒部1’7.1’7
’・・・可動リング −11− 18・・・・・下部ホッパー内ゲート弁出 願 人 新
日本製鍼株式会社 2 第2図 第3図
1, 2, and 3 are longitudinal cross-sectional explanatory views showing an example of a bellless type charging device for improving the method of charging materials into a blast furnace according to the present invention, and FIG. FIG. 2 is an explanatory longitudinal cross-sectional view showing an example of a bellless charging device for carrying out a raw material charging method. 1... Belt conveyor 2... Chute 3... Upper hopper 4... Gate valve 5... Upper seal valve 6... ...lower hopper? ...Gate valve 8...Lower seal valve 9...Furnace chute 1O...Pressure equalization system 11...Exhaust pressure system 12... ... Coarse grain raw material 13 ... Fine grain raw material 14 ... Classification damper 15 ... Inner cylinder part 15 of upper hopper ... Inner cylinder part 16 of lower hopper ... ... Upper hopper outer cylinder part 16' ... Lower hopper outer cylinder part 1'7.1'7
'...Movable ring -11- 18...Lower hopper internal gate valve Application person Shin Nippon Acupuncture Co., Ltd. 2 Figure 2 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 原料をホッパーからシュートを介して炉内に装入するベ
ルレス式装入装置において、ホッパー内に原料を粒度別
、銘柄別等種別に貯蔵し・これらの原料をホッパーの均
圧、排圧操作の1サイクルの中で種別に順次ホッパーか
ら排出できるようになしシュートを介して炉内の夫々の
所望位置に装入することを特徴とする高炉への原料装入
方法。
In a bell-less charging device that charges raw materials from a hopper into a furnace via a chute, raw materials are stored in the hopper by particle size, brand, etc., and these raw materials are used for pressure equalization and exhaust pressure operations in the hopper. A method for charging raw materials into a blast furnace, characterized in that raw materials are charged to respective desired positions in the furnace through a chute so that raw materials can be sequentially discharged from a hopper according to type in one cycle.
JP10703184A 1984-05-26 1984-05-26 Method for charging raw material to blast furnace Pending JPS60251208A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10703184A JPS60251208A (en) 1984-05-26 1984-05-26 Method for charging raw material to blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10703184A JPS60251208A (en) 1984-05-26 1984-05-26 Method for charging raw material to blast furnace

Publications (1)

Publication Number Publication Date
JPS60251208A true JPS60251208A (en) 1985-12-11

Family

ID=14448759

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10703184A Pending JPS60251208A (en) 1984-05-26 1984-05-26 Method for charging raw material to blast furnace

Country Status (1)

Country Link
JP (1) JPS60251208A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0525515A (en) * 1991-07-16 1993-02-02 Sumitomo Metal Ind Ltd Method for charging raw material in bell-less blast furnace and apparatus therefor
JPH0565513A (en) * 1991-09-05 1993-03-19 Sumitomo Metal Ind Ltd Method for charging raw material into bell-less blast furnace and apparatus therefor
JPH0570817A (en) * 1991-05-20 1993-03-23 Sumitomo Metal Ind Ltd Method and apparatus for charging raw material in bell-less blast furnace
WO2003002768A1 (en) * 2001-06-28 2003-01-09 Startec Iron, Llc Equipment for distribution and feeding of charge and fuel in shaft furnaces of rectangular cross section

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0570817A (en) * 1991-05-20 1993-03-23 Sumitomo Metal Ind Ltd Method and apparatus for charging raw material in bell-less blast furnace
JPH0525515A (en) * 1991-07-16 1993-02-02 Sumitomo Metal Ind Ltd Method for charging raw material in bell-less blast furnace and apparatus therefor
JPH0565513A (en) * 1991-09-05 1993-03-19 Sumitomo Metal Ind Ltd Method for charging raw material into bell-less blast furnace and apparatus therefor
WO2003002768A1 (en) * 2001-06-28 2003-01-09 Startec Iron, Llc Equipment for distribution and feeding of charge and fuel in shaft furnaces of rectangular cross section
US6800113B2 (en) 2001-06-28 2004-10-05 Startec Iron Llc Equipment for distribution and feeding of charge and fuel in shaft furnaces of rectangular cross section

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