JPH08100208A - Tuyere structure for blast furnace pulverized coal injection - Google Patents
Tuyere structure for blast furnace pulverized coal injectionInfo
- Publication number
- JPH08100208A JPH08100208A JP23874694A JP23874694A JPH08100208A JP H08100208 A JPH08100208 A JP H08100208A JP 23874694 A JP23874694 A JP 23874694A JP 23874694 A JP23874694 A JP 23874694A JP H08100208 A JPH08100208 A JP H08100208A
- Authority
- JP
- Japan
- Prior art keywords
- pulverized coal
- tuyere
- blast furnace
- blowing
- blow pipe
- 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- Withdrawn
Links
Landscapes
- Manufacture Of Iron (AREA)
- Blast Furnaces (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、高炉に微粉炭を吹き
込む際の羽口構造、特に微粉炭の燃焼率を高めることの
できる羽口構造に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a tuyere structure for blowing pulverized coal into a blast furnace, and more particularly to a tuyere structure capable of increasing the burning rate of pulverized coal.
【0002】[0002]
【従来の技術】従来から高炉操業におけるコークス比を
低減するために、高炉の送風羽口に接続されたブローパ
イプに微粉炭吹込みランスを挿入して、ブローパイプと
接続する小羽口から高炉内に微粉炭を吹き込む操業が行
われている。2. Description of the Related Art Conventionally, in order to reduce the coke ratio in the operation of a blast furnace, a pulverized coal blowing lance is inserted into a blow pipe connected to a blast furnace tuyere, and the inside of the blast furnace is fed from a small tuyere connected to the blow pipe. The operation of blowing pulverized coal into is being carried out.
【0003】上述したような高炉の微粉炭吹込み操業に
おいて、図4に示す小羽口21の先端から微粉炭吹込み
ランス22までの距離Lと微粉炭の燃焼率(微粉炭中の
Cのうち、燃焼によりガス化する割合)との関係は、図
5のグラフのような関係となる。燃焼率が図5のグラフ
のような傾向を示すのは、高炉内には基本的には微粉炭
を燃焼させる酸素が存在しないからであり、微粉炭吹込
みランス22を小羽口21先端に近づければ近づけるほ
ど、燃焼率は低下することになる。In the pulverized coal blowing operation of the blast furnace as described above, the distance L from the tip of the small tuyere 21 to the pulverized coal blowing lance 22 shown in FIG. 4 and the burning rate of the pulverized coal (of C in pulverized coal) , The rate of gasification by combustion) is as shown in the graph of FIG. The reason why the combustion rate tends to be as shown in the graph of FIG. 5 is that basically there is no oxygen for burning pulverized coal in the blast furnace, and the pulverized coal injection lance 22 is brought close to the tip of the tuyere 21. The closer it is, the lower the combustion rate.
【0004】したがって、小羽口21の先端から微粉炭
吹込みランス22までの距離Lを大きくすると、微粉炭
の燃焼率が向上し、図6のグラフに示すように、置換率
{溶銑1トン当り微粉炭1kgを吹き込んだときに低下
する溶銑1トン当りのコークス量(kg)}が向上す
る。Therefore, when the distance L from the tip of the small tuyere 21 to the pulverized coal injection lance 22 is increased, the combustion rate of the pulverized coal is improved, and as shown in the graph of FIG. 6, the replacement rate {per 1 ton of hot metal] The coke amount (kg) per ton of hot metal, which decreases when 1 kg of pulverized coal is blown, is improved.
【0005】このため、従来ランス先端位置は、ブロー
パイプ先端位置に接近して配置せざるを得なかった。For this reason, conventionally, the tip end position of the lance must be arranged close to the tip end position of the blow pipe.
【0006】他の微粉炭吹込み方法としては、特開平5
−112806号公報に開示された方法がある。この微
粉炭吹込み方法は、図7に示すように、高炉の送風羽口
31に接続されたブローパイプ32内に、微粉炭吹込み
ランス33を挿入するとともに、酸素吹込み用ランス3
4を微粉炭吹込みランス33と対向して挿入し、かつ微
粉炭吹込みランス33と酸素吹込み用ランス34の軸線
が、ブローパイプ32の軸線と直交する直線に対して、
互いに同一角度だけ傾斜するようにした上で、それぞれ
のランス33および34から微粉炭と酸素を吹き込み、
旋回流を形成させるものである。この旋回流により、前
述した小羽口21の先端から微粉炭吹込みランス22ま
での距離Lを増大させなくても、ブローパイプ32内で
の微粉炭の滞留時間を長くすることができ、この結果微
粉炭の燃焼効率が向上するものである。Another method for blowing pulverized coal is disclosed in Japanese Patent Laid-Open No. Hei 5
There is a method disclosed in Japanese Patent Laid-Open No. 112806. In this pulverized coal blowing method, as shown in FIG. 7, the pulverized coal blowing lance 33 is inserted into the blow pipe 32 connected to the blast tuyere 31 of the blast furnace, and the oxygen blowing lance 3 is inserted.
4 is inserted so as to face the pulverized coal injection lance 33, and the axes of the pulverized coal injection lance 33 and the oxygen injection lance 34 are perpendicular to the axis of the blow pipe 32.
After inclining each other by the same angle, pulverized coal and oxygen are blown from the respective lances 33 and 34,
A swirl flow is formed. Due to this swirling flow, the residence time of the pulverized coal in the blow pipe 32 can be lengthened without increasing the distance L from the tip of the small tuyere 21 to the pulverized coal injection lance 22. The combustion efficiency of pulverized coal is improved.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、小羽口
21の先端から微粉炭吹込みランス22までの距離Lを
増大させた場合、次のような問題がある。 (1)狭い空間で微粉炭が急激に燃焼しガス量が増加す
るため、ブローパイプ内での圧力損失が上昇し、高炉へ
の送風圧力が変動する。 (2)ブローパイプ内面に微粉炭燃焼時に発生する溶融
灰分が付着成長し、羽口が閉塞する。However, when the distance L from the tip of the tuyere 21 to the pulverized coal blowing lance 22 is increased, there are the following problems. (1) Since pulverized coal rapidly burns in a narrow space and the amount of gas increases, the pressure loss in the blow pipe increases, and the blowing pressure to the blast furnace fluctuates. (2) Molten ash generated during combustion of pulverized coal adheres and grows on the inner surface of the blow pipe, and the tuyere is closed.
【0008】一方、上述した特開平5−112806号
公報に開示された方法は、距離Lを増大させなくとも、
燃焼効率が向上できる技術であるが、酸素を吹き込む方
法であるため、酸素を供給する設備が必要であり、設備
費が高くつくという問題点があった。On the other hand, according to the method disclosed in the above-mentioned Japanese Patent Laid-Open No. 5-112806, even if the distance L is not increased,
Although this is a technique that can improve combustion efficiency, it is a method of blowing oxygen, so that there is a problem that equipment for supplying oxygen is required and the equipment cost is high.
【0009】この発明は、従来技術の上述のような問題
点を解消するためになされたものであり、高い設備費を
必要とすることなく微粉炭の燃焼率、ひいては燃焼効率
を向上させることのできる高炉微粉炭吹込み用羽口部構
造を提供することを目的とする。The present invention has been made in order to solve the above-mentioned problems of the prior art, and it is possible to improve the combustion rate of pulverized coal, and thus the combustion efficiency, without requiring a high equipment cost. An object of the present invention is to provide a tuyere structure for blowing blast furnace pulverized coal.
【0010】[0010]
【課題を解決するための手段】この発明に係る高炉微粉
炭吹込み用羽口部構造は、微粉炭吹込みランスを小羽口
に接続されたブローパイプ内に挿入して高炉へ微粉炭を
吹き込む際の羽口部構造であって、微粉炭を吹き込む部
分のブローパイプの内径を小羽口の内径の1.7倍以上
とするとともに、ブローパイプの微粉炭吹き込み部から
小羽口に接続される部分までの区間を水冷構造としたも
のである。The tuyere structure for blast furnace pulverized coal injection according to the present invention blows pulverized coal into a blast furnace by inserting a pulverized coal injection lance into a blow pipe connected to a small tuyere. In the tuyere structure at the time, the inner diameter of the blow pipe of the portion where the pulverized coal is blown is 1.7 times or more the inner diameter of the small tuyere, and the portion where the pulverized coal blowing portion of the blow pipe is connected to the small tuyere The section up to is a water-cooled structure.
【0011】[0011]
【作用】ブローパイプの内径を小羽口の内径の1.7倍
以上とすることにより、微粉炭燃焼時の急激なガス発生
量増加に起因する送風圧力の変動を、操業上許容される
範囲まで緩和することができる。 また、ブローパイプ
の微粉炭吹き込み部から小羽口に接続される部分までの
区間を水冷構造とするとにより、微粉炭が燃焼したとき
に発生する溶融灰分がブローパイプ内面に付着しようと
しても、溶融灰分が急冷されて凝固し剥離される。 し
たがって、ブローパイプの微粉炭吹き込み部から小羽口
に接続する部分までの距離を大きくすることができ、燃
焼率を向上させることができる。[Operation] By making the inner diameter of the blow pipe 1.7 times or more of the inner diameter of the small tuyere, the fluctuation of the blast pressure due to the sudden increase in the amount of gas generated during the combustion of pulverized coal can be kept within the allowable range for operation. Can be relaxed. In addition, the section from the pulverized coal blowing part of the blow pipe to the part connected to the small tuyere has a water-cooled structure, so even if the molten ash generated when the pulverized coal burns will adhere to the inner surface of the blow pipe, Is rapidly cooled, solidified and peeled off. Therefore, the distance from the pulverized coal blowing portion of the blow pipe to the portion connected to the tuyere can be increased, and the combustion rate can be improved.
【0012】[0012]
【実施例】本発明の実施例である高炉微粉炭吹込み用羽
口部構造を図1に基づき説明する。EXAMPLE A tuyere structure for blowing blast furnace pulverized coal, which is an example of the present invention, will be described with reference to FIG.
【0013】この高炉微粉炭吹込み用羽口部構造は、小
羽口1に接続されるブローパイプ2の内径Dを、小羽口
1の内径dの1.7倍以上とするとともに、ブローパイ
プ2の微粉炭吹込みランス3挿入部から小羽口1に接続
される部分を水冷部4としている。なお、図1中の符号
5は大羽口である。In this blast furnace pulverized coal blowing tuyere structure, the inner diameter D of the blow pipe 2 connected to the small tuyere 1 is 1.7 times or more the inner diameter d of the small tuyere 1, and the blow pipe 2 The part connected from the pulverized coal blowing lance 3 insertion part to the tuyere 1 is the water cooling part 4. Reference numeral 5 in FIG. 1 is a large tuyere.
【0014】図2は、微粉炭比{溶銑1トン当りの微粉
炭量(kg)}と燃焼率との関係を示すグラフであり、
実線が従来の小羽口の先端から微粉炭吹込みランス先端
までの距離Lが400mmのもの、点線が本発明に基づ
く小羽口の先端から微粉炭吹込みランス先端までの距離
Lが900mmのものである。いずれも、微粉炭比が大
きくなるほど燃焼率は低下するが、低下率は本発明に基
づく場合のほうが従来よりも小さいことが分かる。FIG. 2 is a graph showing the relationship between the pulverized coal ratio {amount of pulverized coal per ton of hot metal (kg)} and burning rate.
The solid line indicates that the distance L from the tip of the conventional tuyere to the tip of the pulverized coal injection lance is 400 mm, and the dotted line indicates that the distance L from the tip of the small tuyere to the tip of the pulverized coal injection lance based on the present invention is 900 mm. is there. In each case, the combustion rate decreases as the pulverized coal ratio increases, but it can be seen that the reduction rate is smaller in the case of the present invention than in the conventional case.
【0015】図3は、40個の羽口を有する内容積42
88m3 の高炉の全羽口を、図1に示した構造とし、微
粉炭200kg/tの割合で吹き込んで操業した場合
の、(a)はコークス比(kg/溶銑t)の、(b)は
送風圧力(kg/cm3 )の時系列的な変動を従来法で
操業した場合と比較して示したグラフである(○は本発
明の実施例、●は従来法を示す)。FIG. 3 shows an internal volume 42 having 40 tuyeres.
When all the tuyere of the 88 m 3 blast furnace has the structure shown in FIG. 1 and is operated by blowing in pulverized coal at a rate of 200 kg / t, (a) is the coke ratio (kg / hot metal t), (b) is Is a graph showing time-series fluctuations of the blowing pressure (kg / cm 3 ) in comparison with the case where the conventional method is operated (∘ indicates the example of the present invention, ● indicates the conventional method).
【0016】このグラフから明らかなように、微粉炭比
を双方とも200kg/溶銑tとしたとき、コークス比
は従来340kg/溶銑tであったものが、本発明の実
施例においては320kg/溶銑tと20kg/溶銑t
低減されている。また、送風圧力も従来法が経時的に変
動しているのに対して、本発明の実施例においてはほと
んど変動していない。As is apparent from this graph, when both the pulverized coal ratios were 200 kg / hot metal t, the conventional coke ratio was 340 kg / hot metal t, but in the embodiment of the present invention 320 kg / hot metal t. And 20 kg / hot metal t
Has been reduced. Further, the blast pressure also fluctuates with time in the conventional method, but hardly changes in the embodiment of the present invention.
【0017】表1に本発明を実施後の効果を従来法と比
較して示す。Table 1 shows the effect after the present invention is carried out in comparison with the conventional method.
【0018】[0018]
【表1】 [Table 1]
【0019】[0019]
【発明の効果】本発明により、微粉炭の燃焼効率の向上
が図れ、200kg/溶銑tの高微粉炭操業で安定して
吹き込みができるので、燃料比が低減でき、溶銑の製造
コストを低下させることができる。EFFECTS OF THE INVENTION According to the present invention, the combustion efficiency of pulverized coal can be improved, and stable blowing can be performed in a high pulverized coal operation of 200 kg / molt t, so that the fuel ratio can be reduced and the manufacturing cost of molten pig iron can be reduced. be able to.
【図1】本発明の実施例の高炉微粉炭吹込み用羽口部構
造の説明図である。FIG. 1 is an explanatory diagram of a tuyere structure for blowing blast furnace pulverized coal according to an embodiment of the present invention.
【図2】微粉炭比と燃焼率との関係を示すグラフであ
る。FIG. 2 is a graph showing a relationship between a pulverized coal ratio and a burning rate.
【図3】微粉炭比を200kg/溶銑tとしたときの操
業実績の時系列的な変動を示したグラフであり、(a)
はコークス比を、(b)は送風圧力を示す。FIG. 3 is a graph showing a time-series variation of the operation results when the pulverized coal ratio is 200 kg / molt pig t, (a)
Indicates the coke ratio, and (b) indicates the blowing pressure.
【図4】小羽口と微粉炭吹込みランスとの位置関係を示
す説明図である。FIG. 4 is an explanatory view showing a positional relationship between a small tuyere and a pulverized coal blowing lance.
【図5】小羽口の先端から微粉炭吹込みランスまでの距
離と微粉炭の燃焼率との関係を示すグラフである。FIG. 5 is a graph showing the relationship between the distance from the tip of the tuyere to the pulverized coal injection lance and the burning rate of the pulverized coal.
【図6】微粉炭の燃焼率と置換率との関係を示すグラフ
である。FIG. 6 is a graph showing a relationship between a combustion rate and a substitution rate of pulverized coal.
【図7】従来の微粉炭吹込み方法を示す説明図である。FIG. 7 is an explanatory view showing a conventional pulverized coal blowing method.
1 小羽口 2 ブローパイプ 3 微粉炭吹込みランス 4 水冷部 5 大羽口 1 Small tuyere 2 Blow pipe 3 Pulverized coal injection lance 4 Water cooling part 5 Large tuyere
Claims (1)
粉炭吹込みランスを挿入して高炉へ微粉炭を吹き込む際
の羽口部の構造であって、微粉炭を吹き込む部分のブロ
ーパイプの内径を小羽口の内径の1.7倍以上とすると
ともに、ブローパイプの微粉炭吹き込み部から小羽口に
接続される部分までの区間を水冷構造としたことを特徴
とする高炉微粉炭吹込み用羽口部構造。1. A tuyere structure when a pulverized coal blowing lance is inserted into a blow pipe connected to a small tuyere to blow pulverized coal into a blast furnace. For blast furnace pulverized coal injection, characterized in that the inner diameter is 1.7 times or more the diameter of the small tuyere, and the section from the pulverized coal injection part of the blow pipe to the part connected to the small tuyere has a water cooling structure. Tuyere structure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23874694A JPH08100208A (en) | 1994-10-03 | 1994-10-03 | Tuyere structure for blast furnace pulverized coal injection |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23874694A JPH08100208A (en) | 1994-10-03 | 1994-10-03 | Tuyere structure for blast furnace pulverized coal injection |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08100208A true JPH08100208A (en) | 1996-04-16 |
Family
ID=17034650
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23874694A Withdrawn JPH08100208A (en) | 1994-10-03 | 1994-10-03 | Tuyere structure for blast furnace pulverized coal injection |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08100208A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014045947A1 (en) * | 2012-09-20 | 2014-03-27 | 三菱重工業株式会社 | Slag removal device |
WO2014045949A1 (en) * | 2012-09-20 | 2014-03-27 | 三菱重工業株式会社 | Slag removal device and slag removal method |
-
1994
- 1994-10-03 JP JP23874694A patent/JPH08100208A/en not_active Withdrawn
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2014045947A1 (en) * | 2012-09-20 | 2014-03-27 | 三菱重工業株式会社 | Slag removal device |
WO2014045949A1 (en) * | 2012-09-20 | 2014-03-27 | 三菱重工業株式会社 | Slag removal device and slag removal method |
JP2014062293A (en) * | 2012-09-20 | 2014-04-10 | Mitsubishi Heavy Ind Ltd | Slag removal device and slag removal method |
JP2014062289A (en) * | 2012-09-20 | 2014-04-10 | Mitsubishi Heavy Ind Ltd | Slag removal apparatus |
CN104411839A (en) * | 2012-09-20 | 2015-03-11 | 三菱重工业株式会社 | Slag removal device |
CN104641003A (en) * | 2012-09-20 | 2015-05-20 | 三菱重工业株式会社 | Slag removal device and slag removal method |
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Legal Events
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Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20020115 |