JP2868941B2 - Tuyere powder injection method for vertical furnace - Google Patents

Tuyere powder injection method for vertical furnace

Info

Publication number
JP2868941B2
JP2868941B2 JP3288617A JP28861791A JP2868941B2 JP 2868941 B2 JP2868941 B2 JP 2868941B2 JP 3288617 A JP3288617 A JP 3288617A JP 28861791 A JP28861791 A JP 28861791A JP 2868941 B2 JP2868941 B2 JP 2868941B2
Authority
JP
Japan
Prior art keywords
tuyere
powder
blowing
granular material
vertical 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.)
Expired - Fee Related
Application number
JP3288617A
Other languages
Japanese (ja)
Other versions
JPH05125412A (en
Inventor
恒也 長谷川
恒雄 相原
洋一 渡辺
精祐 児子
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 Steel Corp
Original Assignee
Kawasaki 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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP3288617A priority Critical patent/JP2868941B2/en
Publication of JPH05125412A publication Critical patent/JPH05125412A/en
Application granted granted Critical
Publication of JP2868941B2 publication Critical patent/JP2868941B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacture Of Iron (AREA)
  • Blast Furnaces (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は高炉あるいは多段羽口を
有する溶融還元炉などの竪型炉の羽口粉粒体吹込方法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for injecting tuyere powder particles into a vertical furnace such as a blast furnace or a smelting reduction furnace having a multistage tuyere.

【0002】[0002]

【従来の技術】近年、高炉操業においては、安価な原燃
料の利用による銑鉄コストの低減や溶銑成分の制御を目
的として高炉羽口からの粉粒体吹込操業が実施されてい
る。また竪型のコークス充填層炉を用いたいわゆる溶融
還元炉の操業においても、原料として粉状の鉄鉱石もし
くはその他の金属酸化物粉を羽口から吹込むのが一般的
である。竪型炉の羽口への粉粒体吹込は、図2に示すよ
うに、羽口11に連接されたブローパイプ9から各羽口
につき1本の粉粒体吹込ランス13を挿入して行うのが
一般的である。また粉粒体の多量吹込を実現するため
に、羽口を上下2段に配置し、上段羽口と下段羽口との
両方から粉粒体を吹込む方法(特開平3−39407号
公報)や、各羽口に粉粒体吹込ランスを2本配設する方
法が提案されている。
2. Description of the Related Art In recent years, in the operation of a blast furnace, an operation of injecting powder and granules from a blast furnace tuyere has been carried out for the purpose of reducing pig iron cost by using inexpensive raw fuel and controlling hot metal components. Also in the operation of a so-called smelting reduction furnace using a vertical coke packed bed furnace, powdery iron ore or other metal oxide powder is generally blown from a tuyere as a raw material. As shown in FIG. 2, the powdery material is blown into the tuyere of the vertical furnace by inserting one powdery material blowing lance 13 for each tuyere from the blow pipe 9 connected to the tuyere 11. It is common. Also, in order to achieve a large amount of powder and granules, a tuyere is arranged in upper and lower stages, and powder and granules are blown from both upper and lower tuyeres (Japanese Patent Laid-Open No. 3-39407). Also, a method has been proposed in which two powder lances are arranged in each tuyere.

【0003】一方、迅速な炉調整のために粉粒体吹込ラ
ンスを二重管とし、一方の管から酸素を他方の管からは
炭材を同時に吹込む方法がある。(特開昭59−281
093号公報)。また、操業条件によっては吹込まれた
粉粒体の一部が未溶解となり、羽口先等に付着成長する
ことがあるため、この付着物の除去装置(実開平3−1
4138号公報)を装備する場合もある。
[0003] On the other hand, there is a method in which a powder and granule blowing lance is formed as a double pipe for rapid furnace adjustment, and oxygen is simultaneously blown from one pipe and carbonaceous material is blown from the other pipe. (JP-A-59-281
No. 093). Further, depending on the operating conditions, a part of the injected granular material becomes undissolved and may adhere to and grow on the tuyere tip or the like.
No. 4138).

【0004】[0004]

【発明が解決しようとする課題】粉粒体吹込ランス1本
あたりの粉粒体吹込量が増加した場合、あるいは熱風の
量や温度の変動(低下)が生じた場合などに、吹込まれ
た粉粒体の一部が未溶解となり、粉粒体吹込ランスの周
囲あるいは羽口先に未溶解の粉粒体が付着、成長するこ
とがあり、甚しい場合には粉粒体の吹込を中断せざるを
得なくなることがあった。
SUMMARY OF THE INVENTION When the amount of powder injected per one lance for blowing powder increases, or when the amount or temperature of hot air fluctuates (decreases), the injected powder can be used. Part of the granules may not be dissolved, and the undissolved granules may adhere and grow around the lance or tuyere tip of the granules. In severe cases, the blowing of the granules must be interrupted. In some cases.

【0005】これを解決するために、羽口先の付着物を
機械的に除去する技術が実開平3−14138号公報に
開示されているが、装置化が必要である上に、粉粒体の
吹込を1時的に中断した上で付着物を除去しなければな
らないという問題があった。一方、機械によらない付着
物の除去方法として、2重管ランスを用いて一方の管か
ら酸素を他方の管から粉粒体を吹込むことを利用するこ
ともできるが、粉粒体吹込ランスの構造が複雑となる
上、ランスの重量が重くなり、取扱いにくいという問題
があった。
In order to solve this problem, a technique for mechanically removing deposits on the tuyere tip is disclosed in Japanese Utility Model Laid-Open Publication No. Hei 3-14138. There is a problem that the adhering matter must be removed after the blowing is temporarily stopped. On the other hand, as a method of removing deposits without using a machine, it is possible to use a method in which oxygen is blown from one tube and granules are blown from another tube using a double tube lance. However, there is a problem that the structure of the lance becomes complicated, the weight of the lance becomes heavy, and it is difficult to handle.

【0006】本発明は、これらの問題点を解決した羽口
粉粒体吹込方法を提供することを目的とする。
[0006] It is an object of the present invention to provide a tuyere powder granule blowing method which solves these problems.

【0007】[0007]

【課題を解決するための手段】本発明は、竪型炉の羽口
に羽口1個につきそれぞれ2本の粉粒体吹込ランスを配
設し、一方の粉粒体吹込ランスから酸化鉄粉又は微粉炭
を吹込みながら、他方の粉粒体吹込ランスから支燃性ガ
と粉粒体とを定期的に交互に切替えて供給することを
特徴とする竪型炉の羽口粉粒体吹込方法である。
According to the present invention, two powder lances are provided for each tuyere in a tuyere of a vertical furnace, and iron oxide powder is supplied from one of the powder lances. Alternatively, while injecting pulverized coal, the combustion supporting gas and the granular material are periodically and alternately switched and supplied from the other granular material blowing lance , and the tuyere powder granular material is injected into the vertical furnace. Is the way.

【0008】ここで竪型炉としては、高炉あるいは多段
羽口を有する溶融還元炉等を指称する。また酸化鉄粉と
しては酸化鉄分を含む粉粒体、例えば鉄鉱石粉や、高
炉、転炉、圧延工程で発生したダストなどを指してい
る。また支撚性ガスとは酸素、酸素富化空気などをい
う。
Here, the vertical furnace refers to a blast furnace or a smelting reduction furnace having a multistage tuyere. In addition, the iron oxide powder refers to a powder containing iron oxide, for example, iron ore powder, dust generated in a blast furnace, a converter, and a rolling process. The twisting gas refers to oxygen, oxygen-enriched air, and the like.

【0009】[0009]

【作用】本発明によれば、羽口にそれぞれ粉粒体吹込ラ
ンスを2本配設し、一方のランスから粉粒体を吹込みな
がら他方のランスから酸素等の支燃性ガスを供給するよ
うにしたので、粉粒体の吹込みを中断することなく支燃
性ガスによって容易に羽口先に付着した粉粒体の付着物
を除去することができる。
According to the present invention, two powder lances are provided at each tuyere, and while one of the lances blows the powder, flammable gas such as oxygen is supplied from the other lance. With this configuration, it is possible to easily remove the particles attached to the tuyere tip by the combustible gas without interrupting the blowing of the particles.

【0010】[0010]

【実施例】図3は本発明による2段羽口を有する溶融還
元炉における羽口粉粒体吹込方法を示すブロック図であ
る。酸化鉄粉は酸化鉄粉貯槽1に貯蔵された後、計量ホ
ッパ3に投入され、フラックスはフラックス貯槽2に貯
蔵された後、同様に計量ホッパ3に投入される。計量ホ
ッパ3では酸化鉄粉とフラックスの各々を秤量した後、
混合用ガス4で2種の原料を混合する。この混合物は吹
込タンク5に導入される。
FIG. 3 is a block diagram showing a method of blowing tuyere powder in a smelting reduction furnace having two-stage tuyeres according to the present invention. After the iron oxide powder is stored in the iron oxide powder storage tank 1, it is put into the measuring hopper 3, and the flux is stored in the flux storage tank 2 and then put into the measuring hopper 3. In the weighing hopper 3, after weighing each of the iron oxide powder and the flux,
The two kinds of raw materials are mixed with the mixing gas 4. This mixture is introduced into the blowing tank 5.

【0011】吹込タンク5では図示しない配管によりタ
ンク内を加圧して、吹込タンク5内の粉粒体を流動化す
る。流動化された粉粒体はキャリアガス6、7により吹
込タンク5内から送出される。キャリアガス6、7によ
り輸送された酸化鉄粉とフラックスとの混合粉は、粉粒
体吹込ランス13a、13bから羽口11内に噴出し、
上段ブローパイプ9と上段羽口11内を通過する熱風と
共に上段羽口11より溶融還元炉14内に吹込まれる。
ここで熱風は加熱した空気又は加熱した酸素富化空気で
ある。また酸素8を供給する配管がキャリアガス6、7
の配管に結合されている。
In the blow tank 5, the inside of the tank is pressurized by a pipe (not shown) to fluidize the granular material in the blow tank 5. The fluidized granular material is sent out of the blowing tank 5 by the carrier gas 6, 7. The mixed powder of the iron oxide powder and the flux transported by the carrier gases 6 and 7 is ejected into the tuyere 11 from the powder blowing lances 13a and 13b,
It is blown into the smelting reduction furnace 14 from the upper tuyere 11 together with the hot air passing through the upper blow pipe 9 and the upper tuyere 11.
Here, the hot air is heated air or heated oxygen-enriched air. In addition, a pipe for supplying oxygen 8 is provided with carrier gases 6 and 7.
Is connected to the piping.

【0012】本実施例では、図1に示すように、内径2
5mmの粉粒体吹込ランス13a、13bを上段羽口1
1にそれぞれ2本配設して通常は両方のランスから粉粒
体を吹込み、羽口前レースウェイ15内にて溶融させて
いる。粉粒体吹込中に上段羽口での吹込状況を監視し、
付着物17が生成した時には、一方のランス13aから
の粉粒体の供給を停止すると同時にキャリアガス6を停
止し、支燃性ガスである酸素8を供給した。このとき、
他方のランス13bの粉粒体吹込は継続した。この結
果、付着物17及び吹込粉粒体16の溶融が促進され、
付着物17が除去されるのが確認された。また、定期的
に粉粒体吹込と酸素供給を切替えることにより、付着物
17の生成を防止することができる。
In this embodiment, as shown in FIG.
5 mm powder and granular material lances 13a and 13b are connected to upper tuyere 1
In general, two powders are blown from both lances and melted in the tuyere raceway 15. Monitor the blowing condition at the upper tuyere during powder and granular material blowing,
When the deposit 17 was generated, the supply of the granular material from one of the lances 13a was stopped, and at the same time, the carrier gas 6 was stopped, and oxygen 8 as a combustion supporting gas was supplied. At this time,
The blowing of the granular material into the other lance 13b was continued. As a result, melting of the deposit 17 and the blowing powder 16 is promoted,
It was confirmed that the deposit 17 was removed. Further, by periodically switching the supply of the granular material and the supply of oxygen, the generation of the deposit 17 can be prevented.

【0013】[0013]

【発明の効果】本発明では、羽口にそれぞれ2本配設し
た粉粒体吹込ランスの一方から粉粒体を吹込みながら、
他方から酸素等の支燃性ガスを供給するようにしたの
で、未溶解の粉粒体による付着物を粉粒体吹込を停止す
ることなく容易に除去することができるようになった。
According to the present invention, the powder and granules are blown from one of the powder and granule blowing lances respectively arranged in the tuyere.
Since the combustion supporting gas such as oxygen is supplied from the other side, it is possible to easily remove the deposits due to undissolved particles without stopping the blowing of the particles.

【0014】また、粉粒体吹込と酸素供給とを定期的に
切替えることにより、粉粒体の溶解が促進され、付着物
の生成を防止できるだけでなく、粉粒体の多量吹込もで
きるようになる。
Further, by periodically switching between the injection of the granular material and the supply of oxygen, the dissolution of the granular material is promoted, so that not only the generation of the deposit can be prevented but also the large amount of the granular material can be blown. Become.

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

【図1】本発明方法の実施に用いる2本の粉粒体吹込ラ
ンスを配設した羽口の断面図である。
FIG. 1 is a cross-sectional view of a tuyere provided with two powder and granular lances used for carrying out the method of the present invention.

【図2】従来の一般的羽口粉粒体吹込を示す図である。FIG. 2 is a view showing a conventional general tuyere powder granule injection.

【図3】本発明の実施例に用いた粉粒体吹込ブロック図
である。
FIG. 3 is a block diagram of a granular material blowing used in an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 酸化鉄粉貯槽 2 フラックス貯槽 3 計量ホッパ 4 混合用ガス 5 吹込タンク 6、7 キャリアガス 8 酸素 9 上段ブローパイプ 10 下段ブローパイプ 11 上段羽口 12 下段羽口 13 粉粒体吹込ランス 14 溶融還元炉 15 レースウェイ 16 粉粒体 17 付着物 REFERENCE SIGNS LIST 1 Iron oxide powder storage tank 2 Flux storage tank 3 Measuring hopper 4 Mixing gas 5 Blow tank 6, 7 Carrier gas 8 Oxygen 9 Upper blow pipe 10 Lower blow pipe 11 Upper tuyere 12 Lower tuyere 13 Granule blowing lance 14 Melt reduction Furnace 15 Raceway 16 Granules 17 Deposits

フロントページの続き (72)発明者 児子 精祐 千葉市川崎町1番地 川崎製鉄株式会社 千葉製鉄所内 (56)参考文献 特開 昭62−192509(JP,A) 特開 平5−112806(JP,A) (58)調査した分野(Int.Cl.6,DB名) C21B 5/00 319 - 320 C21B 7/00 308 - 311 Continuing from the front page (72) Inventor Seiko Kozi 1 Kawasaki-cho, Chiba-shi Kawasaki Steel Corp. Chiba Works (56) References JP-A-62-192509 (JP, A) JP-A-5-112806 (JP, A) (58) Field surveyed (Int. Cl. 6 , DB name) C21B 5/00 319-320 C21B 7/00 308-311

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 竪型炉の羽口に羽口1個につき2本の粉
粒体吹込ランスを配設し、一方の粉粒体吹込ランスから
酸化鉄粉又は微粉炭を吹込みながら、他方の粉粒体吹込
ランスから支燃性ガスと粉粒体とを定期的に交互に切替
えて供給することを特徴とする竪型炉の羽口粉粒体吹込
方法。
1. A tuyere of a vertical furnace is provided with two powder lances for each tuyere, and while one of the powder lances blows iron oxide powder or pulverized coal, the other lance. Switching between the combustion supporting gas and the granular material from the granular lance
A method for injecting tuyere powder and granular material into a vertical furnace, characterized in that it is supplied.
JP3288617A 1991-11-05 1991-11-05 Tuyere powder injection method for vertical furnace Expired - Fee Related JP2868941B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3288617A JP2868941B2 (en) 1991-11-05 1991-11-05 Tuyere powder injection method for vertical furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3288617A JP2868941B2 (en) 1991-11-05 1991-11-05 Tuyere powder injection method for vertical furnace

Publications (2)

Publication Number Publication Date
JPH05125412A JPH05125412A (en) 1993-05-21
JP2868941B2 true JP2868941B2 (en) 1999-03-10

Family

ID=17732521

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3288617A Expired - Fee Related JP2868941B2 (en) 1991-11-05 1991-11-05 Tuyere powder injection method for vertical furnace

Country Status (1)

Country Link
JP (1) JP2868941B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8535410B1 (en) * 2012-04-24 2013-09-17 John D. Lynn Blast furnace cooling method to increase steel production and reduce cost in a basic oxygen furnace
KR101693136B1 (en) * 2013-04-03 2017-01-04 제이에프이 스틸 가부시키가이샤 Blast furnace operation method
CN105074014A (en) 2013-04-03 2015-11-18 杰富意钢铁株式会社 Blast furnace operation method and lance

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62192509A (en) * 1986-02-17 1987-08-24 Kobe Steel Ltd Method for blowing pulverized carbon into blast furnace
JPH05112806A (en) * 1991-10-21 1993-05-07 Nkk Corp Method for blowing pulverized coal into blast furnace

Also Published As

Publication number Publication date
JPH05125412A (en) 1993-05-21

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