JPH04268001A - Method for operating blast furnace - Google Patents

Method for operating blast furnace

Info

Publication number
JPH04268001A
JPH04268001A JP2722591A JP2722591A JPH04268001A JP H04268001 A JPH04268001 A JP H04268001A JP 2722591 A JP2722591 A JP 2722591A JP 2722591 A JP2722591 A JP 2722591A JP H04268001 A JPH04268001 A JP H04268001A
Authority
JP
Japan
Prior art keywords
blast furnace
slag
fluidity
caf2
pulverized coal
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.)
Withdrawn
Application number
JP2722591A
Other languages
Japanese (ja)
Inventor
Kazuyoshi Yamaguchi
山口一良
Hiromitsu Ueno
上野浩光
Kenji Tamura
田村健二
Yoshio Okuno
奥野嘉雄
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 JP2722591A priority Critical patent/JPH04268001A/en
Publication of JPH04268001A publication Critical patent/JPH04268001A/en
Withdrawn legal-status Critical Current

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  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To secure the fluidity of a slag and to avoid inferior permeability when the fluidity of the bosh slag is deteriorated in the change of the kind of fine powdered coal (composition of ash) blown from a tuyere part, Al2O3 in iron ore charged from a furnace top or basicity (CaO/SiO2). CONSTITUTION:At the time of blowing CaF2-based flux (fluorite) together with fine powdered coal from the tuyere part, the mixed rate is adjusted so that CaF2 concn. in both slag becomes 2-10%. As the fluidity of both slag can be secured, the permeability on an operation in a blast furnace can be stabilized and molten iron can stably be supplied.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、炉頂から装入される鉄
鉱石、コークスと羽口部から吹込まれる微粉炭から生成
するボッシュスラグの流動性を確保することにより、生
産性を安定させた高炉操業法に関する。
[Industrial Application Field] The present invention stabilizes productivity by ensuring the fluidity of Bosch slag produced from iron ore and coke charged from the top of the furnace and pulverized coal injected from the tuyere. Regarding blast furnace operation method.

【0002】0002

【従来の技術】高炉操業にあっては、コークス代替とし
て、安価で燃焼性がよく発熱量の高い燃料(微粉炭、石
油、重油、ナフサ等)を羽口部より吹込み、溶銑製造コ
スト低減、生産性向上をはかってきており、特公昭40
−23763号公報にその技術が開示されている。とく
に直近では価格の点から微粉炭吹込みが主流となってお
り、燃料比低減(コスト低減)、生産性向上に大きく寄
与している。
[Prior art] In blast furnace operation, cheap, combustible, high calorific fuel (pulverized coal, petroleum, heavy oil, naphtha, etc.) is injected from the tuyeres as a substitute for coke, reducing hot metal production costs. , and has been working to improve productivity.
The technique is disclosed in Japanese Patent No.-23763. Particularly recently, pulverized coal injection has become mainstream due to price considerations, and it greatly contributes to reducing the fuel ratio (cost reduction) and improving productivity.

【0003】このようにして吹込まれた微粉炭は高炉内
で一部のコークスの代りに燃焼し、その燃焼性の良さと
高い発熱量のために、高温で多量の還元ガスを生成し効
率的な還元反応を行う。したがって炉頂より装入された
鉄鉱石はすばやく金属状態に還元されるとともに、溶融
して高温の溶銑となり、高炉の炉熱が高く生産性が向上
する。
The pulverized coal injected in this way burns in place of some of the coke in the blast furnace, and because of its good combustibility and high calorific value, it generates a large amount of reducing gas at high temperatures and is efficient. Performs a reduction reaction. Therefore, the iron ore charged from the top of the furnace is quickly reduced to a metallic state and melts into high-temperature molten pig iron, which increases the furnace heat of the blast furnace and improves productivity.

【0004】0004

【発明が解決しようとする課題】ところで従来の高炉操
業において、羽口部から吹込まれる微粉炭は、そのとき
の需給状況から設定される操業条件によって決まる一定
値を維持しており、高炉の炉熱の変動に合わせて微調整
する程度である。しかし、吹込まれる微粉炭の種類(灰
分の組成)によって、レースウェイに流入するスラグ(
ボッシュスラグと称する)の流動性が変化し、流動性が
悪化すると高炉の通気性が不良となり、送風量を一定に
維持できず生産量は低下する。また炉頂から装入する鉄
鉱石中のAl2 O3 、塩基度(CaO/SiO2 
)が増加すると、やはりボッシュスラグの流動性が悪化
し、高炉の通気性が不良となる。このとき通気性不良を
解消するために、炉頂から装入する鉄鉱石とコークスの
比率(以下O/Cと略す)を減少させる、あるいは羽口
部から吹込まれる微粉炭の量を減少させて、炉頂から装
入するコークスを増加するため、燃料比(コークス比)
が上昇し、この結果生産量がさらに低下する。
[Problems to be Solved by the Invention] In conventional blast furnace operation, the pulverized coal injected from the tuyere maintains a constant value determined by the operating conditions set based on the supply and demand situation at that time. It is only a matter of fine adjustment according to fluctuations in furnace heat. However, depending on the type of pulverized coal (ash composition) injected, the slag flowing into the raceway (
When the fluidity of the blast furnace (called Bosch slag) changes and the fluidity deteriorates, the ventilation of the blast furnace becomes poor, and the amount of air blown cannot be maintained constant, resulting in a decrease in production. Also, the Al2O3 and basicity (CaO/SiO2) in the iron ore charged from the top of the furnace are
) increases, the fluidity of Bosch slag deteriorates and the ventilation of the blast furnace becomes poor. At this time, in order to eliminate poor ventilation, the ratio of iron ore to coke charged from the top of the furnace (hereinafter abbreviated as O/C) should be reduced, or the amount of pulverized coal injected from the tuyere should be reduced. In order to increase the amount of coke charged from the top of the furnace, the fuel ratio (coke ratio)
increases, resulting in a further decline in production.

【0005】このように従来の高炉操業は安定性に乏し
く、生産性は向上せず燃料比も低下できない。
[0005] As described above, the conventional blast furnace operation has poor stability, and the productivity cannot be improved and the fuel ratio cannot be lowered.

【0006】そこで本発明は羽口部から吹込まれる微粉
炭の種類(灰分の組成)、あるいは炉頂から装入する鉄
鉱石中のAl2 O3 、塩基度(CaO/SiO2 
)が変化しても、ボッシュスラグの流動性を確保して通
気性不良を回避し、高炉操業を安定化させることを目的
とする。
Therefore, the present invention aims to improve the type of pulverized coal (ash composition) injected from the tuyere, or the Al2O3 and basicity (CaO/SiO2) in iron ore charged from the top of the furnace.
), the purpose is to ensure the fluidity of Bosch slag, avoid poor ventilation, and stabilize blast furnace operation.

【0007】[0007]

【課題を解決するための手段および作用】本発明の高炉
操業法は、その目的を達成するために、羽口部から微粉
炭を高炉の内部に吹込み、炉頂から鉄鉱石とコークスを
交互に装入する操業法において、微粉炭、コークス、鉄
鉱石などから生成するボッシュスラグの流動性を確保す
るように、微粉炭とともにCaF2系フラックスを羽口
部から高炉の内部に吹込むことを特徴とする。
[Means and effects for solving the problems] In order to achieve the object, the blast furnace operating method of the present invention injects pulverized coal into the inside of the blast furnace from the tuyere, and alternately injects iron ore and coke from the top of the furnace. In the operation method for charging the blast furnace, CaF2-based flux is injected into the blast furnace from the tuyere along with the pulverized coal to ensure the fluidity of Bosch slag produced from pulverized coal, coke, iron ore, etc. shall be.

【0008】ここでボッシュスラグとは、炉頂から装入
される鉄鉱石、フラックス中の脈石、炉頂から装入され
るコークスのうち、羽口部より吹込まれる空気、O2 
、蒸気等により消費される分のコークス中の灰分、羽口
部より吹込まれる微粉炭中の灰分、フラックス(CaF
2 系)中の脈石で生成されるスラグをいう。
[0008] Here, Bosch slag refers to iron ore charged from the top of the furnace, gangue in flux, coke charged from the top of the furnace, air blown from the tuyere, O2
, ash in coke consumed by steam, ash in pulverized coal injected from the tuyere, flux (CaF
2) Refers to the slag generated from the gangue in the system.

【0009】鉄鋼業においては、転炉で脱燐効率向上を
目的に、CaF2系フラックス(蛍石)を一般的に使用
しているが、本発明のように、安定した高炉操業を目的
としたものではない。
In the steel industry, CaF2-based flux (fluorite) is generally used in converter furnaces for the purpose of improving dephosphorization efficiency. It's not a thing.

【0010】本発明においては、ボッシュスラグの流動
性を確保するために、微粉炭中にCaF2 系フラック
スをあらかじめ混合して羽口部から吹込む。CaF2 
系フラックスの混合量は、ボッシュスラグ中に占めるC
aF2 の濃度が2〜10%となるように調整を行う。 CaF2の濃度が2%未満のときは、濃度が低すぎて流
動性改善の効果がない。CaF2 の濃度が2%以上で
は、濃度が高いほど流動性が改善されるが、次に述べる
理由により10%以下に制限される。すなわち、濃度が
10%を越えると、吹込まれたCaF2 の分解熱のた
め、羽口部での燃焼ガス温度が低下し、ボッシュスラグ
の温度が低下して流動性が悪化する。CaF2 の濃度
が2〜10%のときは、ボッシュスラグの流動性は良好
であり、生成したボッシュスラグはレースウェイ周辺を
円滑に降下し、コークス層中にホールドされることがな
く、高炉操業上通気性不良に陥ることはない。
In the present invention, in order to ensure the fluidity of Bosch slag, CaF2-based flux is mixed in advance with pulverized coal and blown into the tuyere. CaF2
The mixing amount of the system flux is the C occupied in Bosch slag.
The concentration of aF2 is adjusted to 2 to 10%. When the concentration of CaF2 is less than 2%, the concentration is too low to have any effect of improving fluidity. When the concentration of CaF2 is 2% or more, the higher the concentration, the better the fluidity is, but it is limited to 10% or less for the following reason. That is, when the concentration exceeds 10%, the temperature of the combustion gas at the tuyere decreases due to the decomposition heat of the injected CaF2, and the temperature of the Bosch slag decreases, resulting in poor fluidity. When the concentration of CaF2 is 2 to 10%, the fluidity of Bosch slag is good, and the generated Bosch slag smoothly descends around the raceway and is not held in the coke layer, making it suitable for blast furnace operation. There will be no problem with poor ventilation.

【0011】なお本発明においては、ボッシュスラグの
流動性を確保するために、CaF2系フラックス(蛍石
)を使用するが、そのほか流動性を確保できるフラック
スであれば、それを使用できる。
In the present invention, a CaF2-based flux (fluorite) is used to ensure the fluidity of Bosch slag, but any other flux that can ensure fluidity may be used.

【0012】0012

【実施例】以下実施例により本発明の特徴を具体的に説
明する。表1に示すように、実施例1は微粉炭を吹込ん
でいるときに、ボッシュスラグ中に占めるCaF2 の
濃度が2〜4%となるように、CaF2 系のフラック
スを微粉炭中にあらかじめ混合して吹込んだ操業例であ
る。
[Examples] The features of the present invention will be explained in detail with reference to Examples below. As shown in Table 1, in Example 1, when the pulverized coal was being injected, CaF2-based flux was mixed in advance into the pulverized coal so that the concentration of CaF2 in the Bosch slag was 2 to 4%. This is an example of operation using

【0013】実施例2は微粉炭を吹込んでいるときに、
ボッシュスラグ中に占めるCaF2の濃度が4〜6%と
なるように、CaF2 系のフラックスを微粉炭中にあ
らかじめ混合して吹込んだ操業例である。
[0013] In Example 2, when blowing pulverized coal,
This is an example of an operation in which CaF2-based flux was mixed in advance into pulverized coal and injected so that the concentration of CaF2 in Bosch slag was 4 to 6%.

【0014】実施例3は微粉炭を吹込んでいるときに、
ボッシュスラグ中に占めるCaF2の濃度が6〜8%と
なるように、CaF2 系のフラックスを微粉炭中にあ
らかじめ混合して吹込んだ操業例である。
In Example 3, when blowing pulverized coal,
This is an example of operation in which CaF2-based flux was mixed in advance into pulverized coal and injected so that the concentration of CaF2 in Bosch slag was 6 to 8%.

【0015】実施例4は微粉炭を吹込んでいるときに、
ボッシュスラグ中に占めるCaF2の濃度が8〜10%
となるように、CaF2 系のフラックスを微粉炭中に
あらかじめ混合して吹込んだ操業例である。
In Example 4, when blowing pulverized coal,
The concentration of CaF2 in Bosch slag is 8-10%
This is an example of operation in which CaF2-based flux was mixed in advance into pulverized coal and blown into it.

【0016】いずれのケースの場合も、ボッシュスラグ
の流動性が確保される結果として、比較例に対比すると
、送風圧力が低く、出銑量が多く、燃料比が低い。
In either case, as a result of ensuring the fluidity of the Bosch slag, compared to the comparative example, the blowing pressure is lower, the amount of pig iron tapped is larger, and the fuel ratio is lower.

【0017】比較例は微粉炭を吹込んでいるだけで、そ
の他のフラックス類を吹込んでいない場合であり、実施
例1〜4に比べると、送風圧力が高く、出銑量が少なく
、燃料比が高い。
[0017] The comparative example is a case where only pulverized coal is injected and no other fluxes are injected, and compared to Examples 1 to 4, the blowing pressure is higher, the amount of pig iron tapped is smaller, and the fuel ratio is lower. expensive.

【0018】[0018]

【表1】[Table 1]

【0019】[0019]

【発明の効果】以上説明したように、本発明においては
、炉頂から装入される鉄鉱石、コークスと羽口から吹込
まれる微粉炭、CaF2 系フラックスから生成するボ
ッシュスラグの流動性を確保することにより、高炉操業
上通気性不良を回避し、生産性を安定させることができ
るため、生産量を一定に維持し、安定した溶銑供給が可
能である。
As explained above, in the present invention, the fluidity of the iron ore charged from the top of the furnace, the coke, the pulverized coal injected from the tuyere, and the Bosch slag generated from the CaF2-based flux is ensured. By doing so, poor ventilation during blast furnace operation can be avoided and productivity can be stabilized, so production volume can be maintained constant and hot metal can be supplied stably.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  羽口部から微粉炭を高炉の内部に吹込
み、炉頂から鉄鉱石とコークスを交互に装入する操業法
において、微粉炭、コークス、鉄鉱石などから生成する
ボッシュスラグの流動性を確保するように、微粉炭とと
もにCaF2系フラックスを羽口部から高炉の内部に吹
込むことを特徴とする高炉操業法。
Claim 1: In an operating method in which pulverized coal is injected into the blast furnace from the tuyere and iron ore and coke are alternately charged from the top of the furnace, Bosch slag produced from pulverized coal, coke, iron ore, etc. A blast furnace operating method characterized by injecting CaF2-based flux together with pulverized coal into the blast furnace through the tuyere to ensure fluidity.
JP2722591A 1991-02-21 1991-02-21 Method for operating blast furnace Withdrawn JPH04268001A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2722591A JPH04268001A (en) 1991-02-21 1991-02-21 Method for operating blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2722591A JPH04268001A (en) 1991-02-21 1991-02-21 Method for operating blast furnace

Publications (1)

Publication Number Publication Date
JPH04268001A true JPH04268001A (en) 1992-09-24

Family

ID=12215151

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2722591A Withdrawn JPH04268001A (en) 1991-02-21 1991-02-21 Method for operating blast furnace

Country Status (1)

Country Link
JP (1) JPH04268001A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030054972A (en) * 2001-12-26 2003-07-02 주식회사 포스코 Operational method of blast furnace
KR100442638B1 (en) * 2000-10-09 2004-08-02 주식회사 포스코 Fabrication method of fines cleaning substance and Fines cleaning method in blast furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100442638B1 (en) * 2000-10-09 2004-08-02 주식회사 포스코 Fabrication method of fines cleaning substance and Fines cleaning method in blast furnace
KR20030054972A (en) * 2001-12-26 2003-07-02 주식회사 포스코 Operational method of blast furnace

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