JPS61201709A - Method for operating blast furnace to attain low si content - Google Patents

Method for operating blast furnace to attain low si content

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Publication number
JPS61201709A
JPS61201709A JP4245185A JP4245185A JPS61201709A JP S61201709 A JPS61201709 A JP S61201709A JP 4245185 A JP4245185 A JP 4245185A JP 4245185 A JP4245185 A JP 4245185A JP S61201709 A JPS61201709 A JP S61201709A
Authority
JP
Japan
Prior art keywords
blast furnace
amount
hot metal
ore
furnace
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
JP4245185A
Other languages
Japanese (ja)
Inventor
Hiroyuki Yoshioka
博行 吉岡
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
Sumitomo Metal Industries Ltd
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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP4245185A priority Critical patent/JPS61201709A/en
Publication of JPS61201709A publication Critical patent/JPS61201709A/en
Pending legal-status Critical Current

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  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To stabilize the operation of a blast furnace and to reduce the amount of a ferroalloy used in a steel manufacturing stage as well as to increase the amount of Mn in molten pig iron and to reduce the amount of Si by using powdery Mn and MgO sources in the blast furnace after agglomeration. CONSTITUTION:Fine ore contg. Mn, MgO and CaO sources as principal components is kneaded with cement as a binder, molded, crushed and charged into a blast furnace. The crushed product is similar in shape to sintered ore and has a large angle of repose and gas permeability, so it has satisfactory properties as a starting material for a blast furnace. By this method, the productivity is enhanced, the fuel ratio is lowered and the gas permeability in the furnace is increased. As a result, the amount of Si in molten pig iron can be reduced to the desired value.

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、高炉操業の安定化と製鋼工程での合金鉄使
用量の低減を目的として、溶銑中St濃度を低下させる
高炉操業方法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a blast furnace operating method for reducing the St concentration in hot metal for the purpose of stabilizing blast furnace operation and reducing the amount of ferroalloy used in the steelmaking process.

従来技術とその問題点 高炉内における溶銑中へのSt移行は、炉床湯溜部にお
けるスフグーメタル反応よりもむしろSIOガスを媒介
とするガス−メタル反応が主要な役割をはたしている。
Prior art and its problems In the transfer of St into hot metal in a blast furnace, a gas-metal reaction mediated by SIO gas plays a major role, rather than a sulfur-metal reaction in the hearth sump.

SIOガスを媒介とする溶銑中へのSi移行は、次の2
つの過程に大別される(鉄と鋼vo1.5Si9282
19頁)。
Si transfer into hot metal via SIO gas is as follows:
It is roughly divided into two processes (Tetsu to Hagane vol. 1.5 Si9282
(page 19).

すなわち、■レースウェイ近傍の高温低酸素分圧領域に
おけるコークス中灰分を主源とするSIO。
That is, (1) SIO whose main source is ash in coke in the high temperature, low oxygen partial pressure region near the raceway.

とコークス中の固定炭素との反応によるSIOガスの生
成過程、■軟化融着帯以下における上昇ガス流中に含ま
れるSiOガスと滴下している溶銑中の炭素との反応に
よる溶銑中へのSt移行過程であり、この両過程を反応
式で表わすと以下のようになる。
The generation process of SIO gas by the reaction between the carbon and the fixed carbon in the coke; ■ The generation process of SIO gas in the hot metal by the reaction between the SiO gas contained in the rising gas flow below the softening cohesive zone and the carbon in the dripping hot metal. This is a transition process, and the reaction equations for both processes are as follows.

■(Sin、) + C= 5iO(f) + Go(
f)■5IO(f)十Ω=鉦十GO(f) ここで、()はその化合物がスフグ中に存在することを
示す慣用表記法であり、元素名の下線はその成分が溶銑
中に存在することを示す慣用表記法である。また、<y
>はその化合物が気体であることを示す慣用表記法であ
る。従って、溶銑中Si濃度の制御方法としては、Si
Oガス発生度応の制御と溶銑中へのSi移行反応の制御
がある。
■(Sin,) + C= 5iO(f) + Go(
f) ■5IO (f) 10 Ω = 10 GO (f) Here, () is the conventional notation to indicate that the compound is present in the puffer fish, and the underlined element name indicates that the component is present in the hot metal. This is a customary notation to indicate the existence of something. Also, <y
> is a common notation to indicate that the compound is a gas. Therefore, as a method for controlling the Si concentration in hot metal, Si
There is control of the degree of O gas generation and control of the Si transfer reaction into the hot metal.

実際の高炉操業において、前者の制御手段としては、コ
ークス中灰分量の制御による羽口前持ち込みSin、量
の制御や羽口前温度制御によるSIOガス発生速度の制
御等が実施されている。後者の制御手段としては、装入
物分布制御に基づいたコークス比制御による融着帯レベ
ルの管理や焼結鉱の被還元性・軟化融着性状制御による
融着帯レベルの制御等がある(鉄と鋼vOムロSi98
2 129頁)。
In actual blast furnace operation, the former control means include controlling the amount of ash in the coke to bring Sin in before the tuyere, controlling the amount, and controlling the SIO gas generation rate by controlling the temperature before the tuyere. The latter control means include controlling the cohesive zone level by controlling the coke ratio based on charge distribution control, and controlling the cohesive zone level by controlling the reducibility and softening and cohesive properties of sintered ore ( Tetsu to Hagane vO Muro Si98
2 p. 129).

溶銑中のsiz度の制御方法としては、上記の高φ内で
の溶銑中へのSN移行メカニズムに立脚した制御手段以
外に、送風羽口から酸化鉄を炉内に吹込み、下記■の反
応によって溶銑中Siを酸化させる、いわゆる炉内脱珪
手段が開発されている(特開昭53−87908、特開
昭56−29601、特開昭58−77508等)。
In addition to the above-mentioned control method based on the SN transfer mechanism into the hot metal within a high diameter, iron oxide is blown into the furnace from the blast tuyeres, and the following reaction A so-called in-furnace desiliconization means for oxidizing Si in hot metal has been developed (JP-A-53-87908, JP-A-56-29601, JP-A-58-77508, etc.).

■Si + 2FeO= (Sift) + 2Feま
た、製鋼工程での合金鉄使用量の低減を主な目的として
、その時点での経済情勢に基づいて、高炉にマンガン鉱
石を装入し、溶銑中Mnを上昇させる操業が従来から行
なわれている。この操業において、高炉に装入するマン
ガン鉱石は適正な高炉使用粒度に比較して大きいため、
破砕してふるいにかけ、ふるい上(5〜25■)を塊鉱
石として炉頂より装入し、ふるい下(−5m、 )は焼
結鉱原料として配合され、通常よりもMnが富化された
焼結鉱として高炉に装入されている。
■Si + 2FeO = (Sift) + 2Fe Also, with the main purpose of reducing the amount of ferroalloy used in the steelmaking process, manganese ore is charged into the blast furnace based on the economic situation at the time, and Mn in the hot metal is reduced. Conventionally, operations have been carried out to increase the In this operation, the manganese ore charged to the blast furnace is large compared to the appropriate particle size for use in the blast furnace.
It was crushed and sieved, and the top of the sieve (5 to 25 cm) was charged from the top of the furnace as lump ore, and the bottom of the sieve (-5 m, ) was blended as a sintered ore raw material, enriched in Mn more than usual. It is charged into a blast furnace as sintered ore.

塊マンガン鉱石または焼結鉱として高炉に装入されたマ
ンガン酸化物は、軟化融着帯以下においてマンガン歩留
9がほぼ75%であり、装入マンガン量に応じて溶銑中
Mnが富化される。前記0式の溶銑中へのSi移行反応
の速度式を以下に示すが、溶銑中Mnの富化は溶銑中引
の活量係数/S1を上昇させるため溶銑中Siを低減さ
せる効果がある。
Manganese oxide charged into a blast furnace as lump manganese ore or sintered ore has a manganese yield 9 of approximately 75% below the softened cohesive zone, and Mn in the hot metal is enriched according to the amount of manganese charged. Ru. The rate equation of the Si transfer reaction into the hot metal of Equation 0 is shown below, and the enrichment of Mn in the hot metal has the effect of reducing the Si in the hot metal because it increases the activity coefficient/S1 of the hot metal.

■SiO(g) + C=鉦+co <y>t asi = /Si −(%5i) 10f/Si = 0.177 (%c)+0.122
(%Si) +0.2Si〔%Mn ) +0.057
 (%S〕しかし、上記した従来の溶銑中Mn富化方法
には、次のような問題点があった。
■SiO (g) + C = gong + co <y>t asi = /Si - (%5i) 10f/Si = 0.177 (%c) +0.122
(%Si) +0.2Si[%Mn) +0.057
(%S) However, the above-described conventional method for enriching Mn in hot metal has the following problems.

まず、ふるい下(−5wm )を焼結鉱原料とじて使用
すると、焼結鉱原料中のに4oが上昇し焼結機のコーク
ス原単位一定のままでは成品焼結鉱の還元粉化指数(R
DI)が悪化するため、成品焼結鉱の還元粉化指数(R
DI)を一定KM持するにはコークス原単位を上昇させ
る必要があり、焼結鉱製造コストのアップにつながると
いう問題がある。
First, when the bottom of the sieve (-5wm) is used as sintered ore raw material, the 4O in the sintered ore raw material increases, and if the coke consumption rate of the sintering machine remains constant, the reduction pulverization index of the finished sintered ore ( R
The reduced pulverization index (R) of finished sintered ore deteriorates.
In order to maintain DI) at a constant KM, it is necessary to increase the coke consumption rate, which leads to an increase in the production cost of sintered ore.

また、マンガン磁石を高炉炉頂から装入した場合の溶銑
中31低減効果は、送風羽口からマンガン磁石粉を吹き
込んだ場合より小さいという問題がある。なお、高炉送
風羽口からマンガン磁石粉を吹き込んだ場合の溶銑中S
t低減効果としては、マンガン鉱石中に含まれるマンガ
ン酸化物と共に鉄酸化物が、下記■、■式に示す脱珪反
応を起こすとして説明される。
Further, there is a problem in that the effect of reducing 31 in hot metal when manganese magnets are charged from the top of the blast furnace is smaller than when manganese magnet powder is blown into the blast tuyeres. In addition, S in hot metal when manganese magnet powder is blown from the blast furnace tuyere.
The t reduction effect is explained by the fact that iron oxide together with manganese oxide contained in manganese ore causes a desiliconization reaction shown in the following formulas (1) and (2).

■Sf + 2 (MnO) = 2Mn + (SI
Oり■Si + 2 (Fed) = 2 Fe + 
(Sift)上記脱珪反応を利用して、マンガン酸化物
粉を送風羽口から高炉、に吹込む炉内脱珪方法について
は、例えば特願昭57−25983により公知であるが
、従来の送風羽口吹込みの場合、マンガン鉱石全量を破
砕する必要があり、破砕コストが非常に高くつく欠点が
ある。
■Sf + 2 (MnO) = 2Mn + (SI
Oori ■Si + 2 (Fed) = 2 Fe +
(Sift) An in-furnace desiliconization method in which manganese oxide powder is blown into a blast furnace from a blowing tuyere using the desiliconization reaction described above is known, for example, from Japanese Patent Application No. 57-25983. In the case of tuyere injection, it is necessary to crush the entire amount of manganese ore, which has the disadvantage that the crushing cost is very high.

発  明  の  目  的 この発明は、従来の前記実情にかんがみ、なされたもの
であり、粉Mn鉱や粉MfO源等を焼結鉱や塊コークス
と同様な形で用いることが可能で、かつ経済的に溶銑中
Mnの上昇および溶銑中Siの低下をはかることができ
る高炉操業方法を提案することを目的とするものである
Purpose of the Invention This invention was made in view of the above-mentioned conventional situation, and it is possible to use powdered Mn ore, powdered MfO source, etc. in the same form as sintered ore and lump coke, and it is economical. The purpose of the present invention is to propose a blast furnace operating method that can increase Mn in hot metal and decrease Si in hot metal.

発明の構成 この発明に係る低SI操業方法は、Mn 、 WifO
*CaOtAを主成分とした粉粒鉱石を、セメシト類を
バインダーとして混疎し、成型後破砕したものを高iK
装入することにより、溶銑中S 171度を低下させる
ことを特徴とするものである。
Structure of the Invention The low SI operation method according to the present invention comprises Mn, WifO
*Powdered ore containing CaOtA as the main component is mixed with semesites as a binder, molded and then crushed to produce high iK.
It is characterized by reducing S171 degrees in hot metal by charging it.

すなわち、この発明は粉Mn K、粉MpO源等を、い
わゆる非焼成塊成鉱と同様に塊成化して高炉に使用する
ことによプ、溶銑中sla度を低下させる方法である。
That is, the present invention is a method of reducing the sla degree in hot metal by agglomerating powdered Mn K, powdered MpO sources, etc. in the same way as so-called uncalcined agglomerated ore and using it in a blast furnace.

高炉に使用される非焼成塊成鉱として知られているコー
ルドボンド絋は、粉鉱石、石灰石粉にセメント等のバイ
ンダーを混合後ブロック状に成型し、破砕する方法で製
造されるのが一般的である。
Cold bonded ore, known as unfired agglomerate used in blast furnaces, is generally manufactured by mixing fine ore or limestone powder with a binder such as cement, then forming it into a block shape, and crushing it. It is.

このような方法で製造されるコールドボンド砿は破砕す
るため形状が焼結鉱に類似し、安息角が大となるととも
に、通気性、還元後の状態は焼結鉱と同様であシ、高炉
原料として良好な性状を有することが認められている。
Because the cold bonded metal produced by this method is crushed, it has a shape similar to sintered ore, has a large angle of repose, and has the same air permeability and state after reduction as sintered ore. It is recognized that it has good properties as a raw material.

1 この発明は、鉄磁石をセメントバインダーで塊成化する
、いわゆるコールドボンド法および上記性状を有するコ
ールドボンド鉱に着目し、高燐溶銑の低Si化に有効な
溶銑中Mnの上昇、スラグ中MfOおよび塩基度の上昇
をはかるために用いるMn源、MpO源、CaO源をコ
ールドボンド法で塊成化して高炉装入物として用いるこ
とを特徴とするものである。
1 This invention focuses on the so-called cold bond method in which iron magnets are agglomerated with a cement binder and cold bond ore having the above properties. This method is characterized in that the Mn source, MpO source, and CaO source used to increase MfO and basicity are agglomerated by a cold bond method and used as blast furnace charge.

第1図はこの発明に係る高炉装入物の製造プロセスの一
例を示すも、ので、粉Mn源、粉MfO源、粉CaO源
とポルトランドセメント等のバインダーを混合し、これ
をブロック状に成型し、蒸気養生後破砕する。ここで、
Mn源、MgO源、CaO源としては、万俺粉、粉蛇紋
岩、ドロマイト粉、Niスラグ、鉄分含有ダスト等を用
いることができる。なお、使用する粉粒鉱石としては、
高温性状を考慮して10■以下で111111以上が1
0〜70%含まれる鉱石を使用するのが好ましい。すな
わち、1謳以上の鉱石はそのままの状態で残留し、軟化
収縮にほとんど寄与しないこと、また鉱石中に1+w+
以上の粒径のものが10%以上あれば通常の高炉原料と
同等の軟化性状が得られ、かつ70%を超えると規準の
回転強度より低くなり実用に耐えないものになる。
Figure 1 shows an example of the manufacturing process for blast furnace charge according to the present invention. Therefore, a powdered Mn source, powdered MfO source, powdered CaO source and a binder such as Portland cement are mixed and this is formed into a block shape. After steam curing, crush. here,
As the Mn source, the MgO source, and the CaO source, it is possible to use powdered powder, powdered serpentine, dolomite powder, Ni slag, iron-containing dust, and the like. The powder ore used is as follows:
Considering high temperature properties, 10■ or less and 111111 or more are 1
Preference is given to using ores containing from 0 to 70%. In other words, one or more ores remain as they are and hardly contribute to softening and shrinkage.
If the particle size is 10% or more, a softening property equivalent to that of a normal blast furnace raw material can be obtained, and if it exceeds 70%, the rotational strength becomes lower than the standard rotational strength and becomes unusable.

この発明では上紀粉Mn源、粉MfOg、粉CaO源に
バインダーとしてポルトランドセメントと必要なら水分
を加えて混合したものを、例えば振動エネルギーを用い
ブロック状に成型し、蒸気養生後所望の大きさに破砕す
る。ブロック状に成型した本のはその11の状態で使用
することも可能であるが、破砕して用いる方が高炉にお
ける安息角の向上と通気抵抗の改善がはかられる。すな
わち、主たる高炉装入物であるベレット、焼結鉱の安息
角はそれぞれ25°、30°であ夛、この発明の特にブ
ロック状のものを破砕したものは31°程度の安息角を
有し、良好な形状である焼結鉱の安息角に近づき、装入
分布が改善される。また、安息角が大きいため炉内での
充填率が低くfk!り、良好なガス流れを与えることが
できる。
In this invention, a mixture of a powdered Mn source, powdered MfOg, powdered CaO source, Portland cement as a binder, and moisture if necessary is formed into a block shape using, for example, vibration energy, and after steam curing, a desired size is formed. Crush into pieces. Although it is possible to use a book molded into a block shape in the state 11, it is better to use it after crushing it to improve the angle of repose and ventilation resistance in the blast furnace. That is, the angles of repose of pellets and sintered ore, which are the main blast furnace charges, are 25° and 30°, respectively, and the crushed block-shaped material according to the present invention has an angle of repose of about 31°. , the angle of repose is close to that of sintered ore, which is in good shape, and the charging distribution is improved. Also, because the angle of repose is large, the filling rate in the furnace is low fk! can provide good gas flow.

上記破砕後の粒径としては、高炉主原料である焼結鉱と
同様の10〜5o■程度が好ましい。また、この冷間成
型破砕鉱の主たる成分であるMn 、 MpO。
The particle size after crushing is preferably about 10 to 5 degrees, which is the same as that of sintered ore, which is the main raw material of the blast furnace. In addition, Mn and MpO are the main components of this cold-formed crushed ore.

CaOの含有量としては、特に限定するものではなJf
Mn5〜3o%、MP010〜40%、Ca010〜5
0%が適当である。
The content of CaO is not particularly limited.
Mn5~3o%, MP010~40%, Ca010~5
0% is appropriate.

なお、この発明における高炉装入物の製造手段を冷間成
型としたのは、Mn鉱やMfO源原料は一般に融点が高
いため、焼成あるいは加熱により成型することは熱的、
品質的に問題となるからである。また原料を混合する際
、バインダーとして固形の粉状セメントを用いる場合は
水分を加えなければならないが、液状のバインダーを用
いる場合は水分を加えなくてもよいので、水分は必要に
応じて添加すればよい。
The reason why cold forming is used as a means of producing the blast furnace charge in this invention is because Mn ore and MfO source materials generally have a high melting point.
This is because it poses a quality problem. Also, when mixing raw materials, if solid powder cement is used as a binder, water must be added, but if a liquid binder is used, it is not necessary to add water, so water can be added as necessary. Bye.

実施例 第1表に示す組成を有し、第2表に示す粒度構成の原料
を混合し、150〜250txmの大きさのブロック状
に成型し50’C,8時間養生した後粒径5〜50■に
破砕して得られた第3表に示す成品性状の  ゛冷間成
型破砕砿を第4表に示す原料比率でA高炉(内容積27
00 d )に使用した実施結果を従来法と比較して第
4表に示す。
Examples Raw materials having the composition shown in Table 1 and the particle size structure shown in Table 2 were mixed, molded into a block shape with a size of 150 to 250 txm, and cured at 50'C for 8 hours. The cold-molded crushed iron having the product properties shown in Table 3 obtained by crushing it to 50cm was crushed into A blast furnace (inner volume 27cm) using the raw material ratio shown in Table 4.
00 d) are shown in Table 4 in comparison with the conventional method.

第4表より明らかなごとく、この発明方法は従来法と比
較し、生産性の上昇、燃料比の低下、炉内通気性の向上
が顕著であり、この結果溶銑中Siは低減している。
As is clear from Table 4, compared to the conventional method, the method of the present invention significantly increases productivity, lowers the fuel ratio, and improves the ventilation inside the furnace, and as a result, Si in the hot metal is reduced.

(以下余白) 第1表 使用原料の組成 第2表 使用原料の粒度構成 第3表成品性状 第4表 高炉原料比率 第  5  表   結    果 発明の効果 上記の実施例からも明らかなごとく、この発明方法によ
れば、焼結過程における焼結鉱品質の悪化、高炉操業に
おける通気性悪化を主とした操業への悪影響を与えず、
溶銑中Mnを上昇させて溶銑中のSi量を低下させるこ
とができるので、高炉操業の安定化と製鋼工程での合金
鉄使用量の低減に大なる効果を奏するものである。
(Leaving space below) Table 1 Composition of raw materials used Table 2 Particle size composition of raw materials used 3 Table Product properties Table 4 Blast furnace raw material ratio Table 5 Results Effects of the invention As is clear from the above examples, this invention According to the method, there is no negative impact on operations, mainly deterioration of sintered ore quality during the sintering process and deterioration of air permeability during blast furnace operation.
Since the amount of Si in the hot metal can be lowered by increasing the Mn in the hot metal, it is highly effective in stabilizing blast furnace operation and reducing the amount of ferroalloy used in the steelmaking process.

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

Claims (1)

【特許請求の範囲】[Claims] 溶銑中Si濃度を低下させる高炉操業方法において、M
n、MgO、CaO源を主成分とした粉粒鉱石を、セメ
ント類をバインダーとして混練し、成型後破砕したもの
を高炉に装入することにより、溶銑中Si濃度を低下さ
せることを特徴とする高炉の低Si操業方法。
In a blast furnace operating method for reducing the Si concentration in hot metal, M
This method is characterized by lowering the Si concentration in hot metal by kneading powdered ore mainly composed of n, MgO, and CaO sources with cement as a binder, and charging the crushed product after molding into a blast furnace. A method for operating a blast furnace with low Si.
JP4245185A 1985-03-04 1985-03-04 Method for operating blast furnace to attain low si content Pending JPS61201709A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4245185A JPS61201709A (en) 1985-03-04 1985-03-04 Method for operating blast furnace to attain low si content

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4245185A JPS61201709A (en) 1985-03-04 1985-03-04 Method for operating blast furnace to attain low si content

Publications (1)

Publication Number Publication Date
JPS61201709A true JPS61201709A (en) 1986-09-06

Family

ID=12636432

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4245185A Pending JPS61201709A (en) 1985-03-04 1985-03-04 Method for operating blast furnace to attain low si content

Country Status (1)

Country Link
JP (1) JPS61201709A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH028310A (en) * 1988-06-25 1990-01-11 Nkk Corp Blast furnace low Si operation method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH028310A (en) * 1988-06-25 1990-01-11 Nkk Corp Blast furnace low Si operation method

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