JPH028310A - Low si operating method in blast furnace - Google Patents

Low si operating method in blast furnace

Info

Publication number
JPH028310A
JPH028310A JP15748988A JP15748988A JPH028310A JP H028310 A JPH028310 A JP H028310A JP 15748988 A JP15748988 A JP 15748988A JP 15748988 A JP15748988 A JP 15748988A JP H028310 A JPH028310 A JP H028310A
Authority
JP
Japan
Prior art keywords
coke
auxiliary raw
raw material
blast furnace
layer
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
JP15748988A
Other languages
Japanese (ja)
Inventor
Tomonori Kato
友則 加藤
Hirohisa Hotta
堀田 裕久
Akio Shimomura
昭夫 下村
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP15748988A priority Critical patent/JPH028310A/en
Publication of JPH028310A publication Critical patent/JPH028310A/en
Pending legal-status Critical Current

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  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To reduce Si content in molten iron without giving a tuyere in a blast furnace any damage by charging the auxiliary raw material composing of CaO or MgO source into coke layer in the furnace. CONSTITUTION:In the coke 1 and ore 2 charged as alternately layer by layer in the blast furnace at multi-steps, the auxiliary raw material (flux) 3 composing of about 5-30mm grain size of CaO or MgO is charged into layer of the coke 1. The auxiliary raw material 3 is desirable to charge at circumferential edge part in the furnace at the layer of the coke 1. The charged auxiliary raw material 3 is descended to near raceway together with the coke 1 and generation of SiO gas from ash in the coke 1 is restrained and the Si content in the molten iron is reduced.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、高炉の低Si操業法に関するものである。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for operating a blast furnace with low Si.

〔従来の技術〕[Conventional technology]

高炉から出銑される溶銑中のSi含有量を低下させるこ
とについては、従来から種々の検討が重ねられてきたと
ころであり、このSi含有量の低減は、SiO□(J)
 +c (s) −+ 5lo(y) 十co (y)
  ・・・(1)SiO(#) + C(JL)−+ 
5i(J)+co(y)  ・・・(2)上記(1)式
に従って、レースウェイ近傍のコークス中の灰分からS
iOガスが発生し、そして、上記(2)式に従って、S
iOが溶銑中のCによって還元され、銑中に移行する。
Various studies have been made to reduce the Si content in hot metal tapped from blast furnaces.
+c (s) −+ 5lo(y) 10co(y)
... (1) SiO (#) + C (JL) - +
5i (J) + co (y) ... (2) According to the above formula (1), S
iO gas is generated, and according to equation (2) above, S
iO is reduced by C in the hot metal and migrates into the pig iron.

第3図に、上記(1)式の反応に及ぼす、C/20およ
びM2Oの影響を示す。なお、このときの試験条件は、
第1表に示す通シである。
FIG. 3 shows the influence of C/20 and M2O on the reaction of formula (1) above. The test conditions at this time are:
The rules are shown in Table 1.

第1表 第3図から明らかなように、Cユ0またはMgOの添加
量が増大するにつれて、Si0ガスの発生量が減少する
ことがわかる。
As is clear from Table 1 and FIG. 3, it can be seen that as the amount of C0 or MgO added increases, the amount of Si0 gas generated decreases.

従来、高炉内にC(10まだはMgO源からなる副原料
を装入するために、例えば、高炉羽口から粉状の副原料
を炉内に吹き込む方法がとられている。
Conventionally, in order to charge an auxiliary raw material consisting of a C (10 or MgO source) into a blast furnace, a method has been adopted, for example, in which a powdered auxiliary raw material is blown into the furnace through a blast furnace tuyere.

〔解決しようとする課題〕[Problem to be solved]

しかし、高炉羽目から粉状のC,20’4たはM2O源
からなる副原料を炉内に吹き込む方法は、以下の問題を
有している。即ち、副原料を粉状に粉砕するための設備
が必要である。また、粉状の副原料を炉内に吹き込むた
めの設備が必要である。さらに、副原料の吹込みによっ
て高炉羽目に摩耗や破損が生じる。
However, the method of blowing an auxiliary raw material consisting of powdered C, 20'4 or M2O source into the blast furnace from the blast furnace has the following problems. That is, equipment for pulverizing the auxiliary raw material into powder is required. Additionally, equipment for blowing powdered auxiliary raw materials into the furnace is required. Furthermore, the injection of auxiliary raw materials causes wear and damage to the blast furnace siding.

従って、この発明の目的は、CaO4たはM2O源から
−なる副原料を、高炉羽口から吹き適寸ずに、溶銑のS
i含有量を低減することができる、高炉の低Si操業法
を提供することにある。
Therefore, an object of the present invention is to blow the auxiliary raw material consisting of CaO4 or M2O source from the blast furnace tuyere into the S of hot metal.
An object of the present invention is to provide a low-Si operating method for a blast furnace that can reduce the i content.

〔課題を解決するだめの手段〕[Failure to solve the problem]

この発明は、C,,0またはMgO源からなる粒状副原
料を、炉内のコークス層内に装入し、かくして、溶銑中
のSi含有量を低下させることに特徴を有するものであ
る。
The present invention is characterized in that a granular auxiliary raw material consisting of a C,,0 or MgO source is charged into a coke layer in a furnace, thereby reducing the Si content in hot metal.

次に、この発明の高炉の低Si操業法の一実施態様を図
面を参照しながら説明する。
Next, one embodiment of the method for operating a blast furnace with low Si according to the present invention will be described with reference to the drawings.

第1図は、この発明の一実施態様によって高炉に原料を
装入したときの高炉の概略断面図である。
FIG. 1 is a schematic sectional view of a blast furnace when raw materials are charged into the blast furnace according to an embodiment of the present invention.

第1図に示すように、この発明は、交互に層状に且つ上
下多段に装入されるコークスlと鉱石2のうち・、コー
クスlの層内に、粒径5から301TrrnのCaO4
たはMgO源からなる副原料(フランクス)3を装入す
るものである。高炉の安定操業を図るために、副原料3
は、コークスlの層の炉内周縁部に装入するのが良い。
As shown in FIG. 1, in the present invention, among coke l and ore 2 which are charged alternately in layers and in upper and lower stages, CaO4 with a particle size of 5 to 301 Trrn is added to the coke l layer.
In this case, an auxiliary raw material (Franks) 3 consisting of an MgO source or MgO source is charged. In order to ensure stable operation of blast furnaces, auxiliary raw materials 3
is preferably charged at the periphery of the coke layer in the furnace.

コークス層中に装入された副原料3は、コークスと共に
レースウェイ4近傍脣で降下し、コークス中の灰分から
発生するSiOガスの発生を抑制して、溶銑中のSi含
有量を低下させる。
The auxiliary raw material 3 charged into the coke layer descends together with the coke near the raceway 4, suppresses the generation of SiO gas generated from the ash in the coke, and reduces the Si content in the hot metal.

〔実施例〕〔Example〕

マクネサイ) (Myco3)を5から30調の粒径に
整粒したものからなる副原料を、第1図に示すように、
炉内周縁部のコークス層内に装入して、高炉操業を行っ
た。そして、副原料原単位と溶銑(温度1480から1
490°C)中のSi含有量との関係を調べた。この結
果を第2図に示す。
As shown in Fig. 1, an auxiliary raw material consisting of (Myco3) sized to a particle size of 5 to 30 is used.
The blast furnace was operated by charging it into the coke layer at the periphery of the furnace. Then, the basic unit of auxiliary raw materials and hot metal (temperature 1480 to 1
490°C) was investigated. The results are shown in FIG.

次に、副原料を5から30論の粒径を有する生ドロマイ
ト(J、CO3,%CO3)に代えて、同様に、副原料
原単位と溶銑中のSi含有量との関係について調べた。
Next, the relationship between the basic unit of the auxiliary raw material and the Si content in the hot metal was similarly investigated by replacing the auxiliary raw material with raw dolomite (J, CO3, %CO3) having a particle size of 5 to 30 troms.

この結果を第2図に合わせて示す。The results are also shown in FIG.

第2図から明らかなように、副原料原単位量が増加する
につれて、溶銑中のSi含有量が低下することがわかる
As is clear from FIG. 2, it can be seen that as the basic unit amount of auxiliary raw materials increases, the Si content in the hot metal decreases.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、この発明によれば、CO,Oまた
はM2C源からなる副原料を、コークス層内に装入する
ことによって、従来のように高炉羽口に損傷を与えるこ
となく、高炉の低Si操業が図れるといった有用な効果
がもたらされる。
As explained above, according to the present invention, by charging the auxiliary raw material consisting of CO, O or M2C sources into the coke layer, the blast furnace can be heated without damaging the blast furnace tuyeres unlike the conventional method. Useful effects such as low Si operation can be achieved.

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

第1図は、この発明の一実施態様にょシ、高炉に鉱石お
よびコークスを装入した状態を示す断面図、第2図は、
副原料原単位と溶銑中のSi含有量との関係を示すグラ
フ、第3図は、M、))O/ 5i02とSiOガス発
生速度との関係を示すグラフである。 図面において、 l・・コークス    2・・・鉱石、3・・・副原料
FIG. 1 is a sectional view showing one embodiment of the present invention, in which ore and coke are charged into a blast furnace, and FIG.
FIG. 3 is a graph showing the relationship between the basic unit of auxiliary raw material and the Si content in hot metal, and FIG. 3 is a graph showing the relationship between M,))O/5i02 and the SiO gas generation rate. In the drawing, 1...Coke 2...Ore, 3...Auxiliary raw materials.

Claims (1)

【特許請求の範囲】[Claims] 1 CaOまたはMgO源からなる粒状副原料を、炉内
のコークス層内に装入し、かくして、溶銑中のSi含有
量を低下させることを特徴とする、高炉の低Si操業法
1. A low-Si operation method for a blast furnace, characterized in that a granular auxiliary material consisting of a CaO or MgO source is charged into a coke layer in a furnace, thereby reducing the Si content in hot metal.
JP15748988A 1988-06-25 1988-06-25 Low si operating method in blast furnace Pending JPH028310A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15748988A JPH028310A (en) 1988-06-25 1988-06-25 Low si operating method in blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15748988A JPH028310A (en) 1988-06-25 1988-06-25 Low si operating method in blast furnace

Publications (1)

Publication Number Publication Date
JPH028310A true JPH028310A (en) 1990-01-11

Family

ID=15650804

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15748988A Pending JPH028310A (en) 1988-06-25 1988-06-25 Low si operating method in blast furnace

Country Status (1)

Country Link
JP (1) JPH028310A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07138624A (en) * 1993-11-15 1995-05-30 Nkk Corp Operation of blast furnace
US5419599A (en) * 1993-07-01 1995-05-30 E. J. Brooks Company Rotatable seal
JP2011512314A (en) * 2008-02-20 2011-04-21 シービーディー エナジー リミテッド Reduction of silica

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61153209A (en) * 1984-12-26 1986-07-11 Nippon Kokan Kk <Nkk> Low-s operation method in blast furnace
JPS61201709A (en) * 1985-03-04 1986-09-06 Sumitomo Metal Ind Ltd Method for operating blast furnace to attain low si content

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61153209A (en) * 1984-12-26 1986-07-11 Nippon Kokan Kk <Nkk> Low-s operation method in blast furnace
JPS61201709A (en) * 1985-03-04 1986-09-06 Sumitomo Metal Ind Ltd Method for operating blast furnace to attain low si content

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5419599A (en) * 1993-07-01 1995-05-30 E. J. Brooks Company Rotatable seal
JPH07138624A (en) * 1993-11-15 1995-05-30 Nkk Corp Operation of blast furnace
JP2011512314A (en) * 2008-02-20 2011-04-21 シービーディー エナジー リミテッド Reduction of silica

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