JPH049414A - Method for blowing pulverized coal to blast furnace - Google Patents
Method for blowing pulverized coal to blast furnaceInfo
- Publication number
- JPH049414A JPH049414A JP11024690A JP11024690A JPH049414A JP H049414 A JPH049414 A JP H049414A JP 11024690 A JP11024690 A JP 11024690A JP 11024690 A JP11024690 A JP 11024690A JP H049414 A JPH049414 A JP H049414A
- Authority
- JP
- Japan
- Prior art keywords
- pulverized coal
- tuyere
- projections
- flow
- hot wind
- 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
Links
- 239000003245 coal Substances 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims description 8
- 238000007664 blowing Methods 0.000 title abstract description 4
- 239000012159 carrier gas Substances 0.000 claims abstract description 9
- 238000002347 injection Methods 0.000 claims description 21
- 239000007924 injection Substances 0.000 claims description 21
- 238000002485 combustion reaction Methods 0.000 abstract description 14
- 230000002093 peripheral effect Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229910052681 coesite Inorganic materials 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 229910052906 cristobalite Inorganic materials 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 229910052682 stishovite Inorganic materials 0.000 description 2
- 229910052905 tridymite Inorganic materials 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 229910000805 Pig iron Inorganic materials 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000010420 art technique Methods 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Manufacture Of Iron (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
本発明は、高炉への微粉炭吹込技術に関し、特に羽口先
での燃焼性を改善することで多量の微粉炭吹込みを可能
ならしめ、もっでコークス比、あるいは銑鉄製造コスト
の大幅低減を図ることのできる高炉への微粉炭吹込方法
に関するものである。[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a technology for injecting pulverized coal into a blast furnace, and in particular, by improving the combustibility at the tip of the tuyere, it is possible to inject a large amount of pulverized coal, The present invention relates to a method of injecting pulverized coal into a blast furnace that can significantly reduce the coke ratio or the cost of producing pig iron.
〈従来の技術〉
高炉への微粉炭多量吹込を可能とするためには、ブロー
パイプ、羽口、あるいは羽口先(レースウェイ)での微
わ)炭の燃焼率を高めることが不可欠である。もし燃焼
率が低下すれば、未燃微粉炭の高炉内蓄積による通気阻
害、あるいはダストとしての傾角排出によってコークス
と微粉炭とのW換率が低下するなどの様々な問題を引き
起こす。<Prior Art> In order to make it possible to inject a large amount of pulverized coal into a blast furnace, it is essential to increase the combustion rate of the pulverized coal at the blowpipe, tuyere, or tuyere tip (raceway). If the combustion rate decreases, various problems will occur, such as ventilation obstruction due to the accumulation of unburned pulverized coal in the blast furnace, or a decrease in the W conversion rate between coke and pulverized coal due to oblique discharge as dust.
このような問題を回避すべく、以下に示すような微粉炭
の燃焼性改善策がとられている。In order to avoid such problems, the following measures have been taken to improve the combustibility of pulverized coal.
■ 揮発分が多(着火性の良い炭種の選定、■ 微粉炭
粒度の低下、
■ 送風空気への酸素富化率の上昇、
■ 送風温度の上昇。■ High volatile content (selecting a type of coal with good ignitability, ■ Decreasing the particle size of pulverized coal, ■ Increasing the oxygen enrichment rate of the blast air, ■ Increasing the blast temperature.
また、特開昭61−124510号公報には羽口、また
はブローパイプの内面に突起物を設け、その羽口先端側
に燃料吹込ノズルを臨ませ、燃料を吹込んで燃料と熱風
との混合を促進する方法が開示されている。Furthermore, in Japanese Patent Application Laid-Open No. 61-124510, a protrusion is provided on the inner surface of the tuyere or blowpipe, and a fuel injection nozzle is placed at the tip of the tuyere to inject fuel and mix the fuel and hot air. A method of promoting is disclosed.
一般的な微粉炭吹込の模式図を第4図に参考までに示す
。A schematic diagram of general pulverized coal injection is shown in Figure 4 for reference.
〈発明が解決しようとする課題〉
前に示した従来技術の内、■〜■は通常操業においてと
られている対策であり、それなりの効果を有している。<Problems to be Solved by the Invention> Among the prior art techniques shown above, (1) to (2) are measures taken during normal operation, and have certain effects.
しかしさらに燃焼性を改善するためには微粉炭と熱風(
酸素)との混合をハード的に促進することが必要である
が、この意味において特開昭61−124510号公報
の方法は有効であるが、突起物の後方に形成される局所
的なガス流れの乱れを利用して微粉炭と熱風との混合促
進を図ることを目的としており、羽口またはブローパイ
プの全断面にわたって微粉炭と熱風とを混合するために
は、少なくとも複数本のランス(ノズル)が必要と考え
られ、また公報の図面にもそのように表現されている。However, to further improve combustibility, pulverized coal and hot air (
It is necessary to harden the mixing with oxygen), and in this sense, the method of JP-A-61-124510 is effective, but the local gas flow that is formed behind the protrusion is The purpose is to promote mixing of pulverized coal and hot air by utilizing the turbulence of the tuyere or blowpipe. ) is considered necessary, and is also expressed as such in the drawings of the official gazette.
本発明は、前記問題点を解決し、かつ1本の微粉炭吹込
ランスでも熱風と微粉炭の十分な混合状態が羽口および
/またはブローパイプ内でえられる技術を提供するため
になされたものである。The present invention has been made in order to solve the above-mentioned problems and to provide a technology in which a sufficient mixing state of hot air and pulverized coal can be obtained in the tuyere and/or blowpipe even with a single pulverized coal injection lance. It is.
〈課題を解決するための手段〉
微粉炭の燃焼率を向上させるためには、熱風として吹込
まれる酸素とランスから吹込まれる微粉炭との接触混合
を促進することが必要である。<Means for Solving the Problems> In order to improve the combustion rate of pulverized coal, it is necessary to promote contact mixing between oxygen blown in as hot air and pulverized coal blown in from a lance.
もし、羽口および/またはブローパイプ内を流れる熱風
のうち、量的にその大部分を占める外周部に1本の微粉
炭吹込ランスから吹込まれた微粉炭を分散させることが
できれば、飛躍的に燃焼率を高めることができると考え
、これを達成するための微粉炭吹込方法について検討し
た結果、本発明をなすに至った。If it were possible to disperse the pulverized coal injected from a single pulverized coal injection lance into the outer periphery, which accounts for the majority of the hot air flowing through the tuyere and/or blowpipe, it would be possible to dramatically increase the We thought that the combustion rate could be increased, and as a result of studying a method for injecting pulverized coal to achieve this, we came up with the present invention.
本発明は、羽口および/またはブローパイプの内面にら
せん状または逆ハ字状の突起物を設け、この突起物に微
粉炭吹込ランスから吹込まれた微粉炭とその搬送ガスの
混相流が吹当たるようにしたことを特徴とする高炉への
?Il′PA炭吹込方法である。The present invention provides a spiral or inverted V-shaped protrusion on the inner surface of the tuyere and/or blowpipe, and a multiphase flow of pulverized coal and its carrier gas is blown into the protrusion from a pulverized coal injection lance. To the blast furnace characterized by making it hit? This is the Il'PA charcoal injection method.
〈作 用〉
本発明によれば、羽口1および/またはブローパイプ2
の内面に第1図、第2図に示すような、らせん状または
逆ハ字状、さらにそれを組合せた形状の突起物6を設け
、この突起物に微粉炭吹込ランス3から吹込まれた微粉
炭とその搬送ガスの混相流4が当たるように微粉炭吹込
ランス3を配置する。<Function> According to the present invention, the tuyere 1 and/or the blow pipe 2
As shown in FIGS. 1 and 2, a protrusion 6 in the shape of a spiral, an inverted V-shape, or a combination thereof is provided on the inner surface of the pulverized coal injection lance 3. The pulverized coal injection lance 3 is arranged so as to be hit by the multiphase flow 4 of coal and its carrier gas.
そのために羽口あるいはブローパイプ内には熱風8の軸
方向流れの他に突起物に沿った流れが形成される。微粉
炭吹込ランスから吹込まれた微粉炭とその搬送ガスの混
相流は主に突起物に沿った熱風の流れに巻き込まれ、第
1図、第2図に示すように、その一部を放出しながら羽
口および/またはブローパイプの内面の突起物に沿って
移動し、結果として羽口あるいはブローパイプ内を流れ
る熱風のうち、量的に多い外周部に微粉炭を分散させる
ことが可能となり、飛躍的な燃焼率の向上が可能となる
。Therefore, in addition to the axial flow of the hot air 8, a flow along the protrusions is formed within the tuyere or blowpipe. The multiphase flow of pulverized coal and its carrier gas injected from the pulverized coal injection lance is mainly caught in the flow of hot air along the protrusions, and some of it is released as shown in Figures 1 and 2. The pulverized coal moves along the protrusions on the inner surface of the tuyere and/or the blowpipe, and as a result, it becomes possible to disperse the pulverized coal in the outer circumference of the hot air flowing through the tuyere or blowpipe, where the amount is larger. This makes it possible to dramatically improve the combustion rate.
なお、突起物の上流側で、かつ羽口あるいはブローパイ
プの断面中央に微粉炭吹込ランスをセットしても、吹込
まれた微粉炭とその搬送ガスの混相流は第4図に示すよ
うに、下流に行くほど拡散により拡がるため、一部は突
起物に衝突しそれに沿った流れをとる。また、突起物の
設置区間が長ければ、その区間内に微粉炭吹込ランス先
端をセントしても同様の理由により、その効果はある程
度期待できる。Even if the pulverized coal injection lance is set upstream of the protrusion and at the center of the cross section of the tuyere or blowpipe, the multiphase flow of the injected pulverized coal and its carrier gas will occur as shown in Figure 4. As it spreads further downstream, some of it collides with protrusions and flows along them. Further, if the installation section of the protrusion is long, even if the tip of the pulverized coal injection lance is placed within that section, the effect can be expected to some extent for the same reason.
また突起物の形状はらせん状、逆へ字状、その組合せに
限るものではな(、微粉炭吹込ランスがら吹込まれた微
粉炭とその搬送ガスの混相流を熱風量の多い外周部に分
散させることができる形状であればよい。In addition, the shape of the protrusion is not limited to a spiral shape, an inverted F-shape, or a combination thereof. Any shape that can be used will suffice.
〈実施例〉
本発明の効果を確認すべく高炉の羽口部をシミュレート
した微粉炭tP8焼炉にて実験を行った。<Example> In order to confirm the effects of the present invention, an experiment was conducted in a pulverized coal tP8 furnace that simulates the tuyere of a blast furnace.
炉形状および送風条件は以下のとおりである。The furnace shape and air blowing conditions are as follows.
羽口径:56wφ、炉内径: 600mφ、炉長:4
000騙、送風量:3Nd/m、0□:23−%、送風
温度:1100℃、微粉炭:TC73wt%、VM32
wt%、微粉炭吹込量: 0.4kg/sm (実1!
150kg/ tpig相当)、微粉炭搬送用空気量
:5ONZ/+m。Tuyere diameter: 56wφ, Furnace inner diameter: 600mφ, Furnace length: 4
000 deception, air flow rate: 3Nd/m, 0□:23-%, air temperature: 1100℃, pulverized coal: TC73wt%, VM32
wt%, pulverized coal injection amount: 0.4kg/sm (actual 1!
(equivalent to 150kg/tpig), air amount for conveying pulverized coal: 5ONZ/+m.
微粉炭の吹込ランス先端と羽口先端との距離を200−
に固定し、微粉炭吹込ランスを通常の高炉操業と同様に
羽日中夫にセットした場合、および本発明のように羽口
内壁面に沿ってセットした場合について、それぞれ第2
図のタイプの突起物が有る場合、および無い場合につい
ての微粉炭燃焼実験を行った。The distance between the tip of the pulverized coal injection lance and the tip of the tuyere is 200-
The second case is fixed at
Pulverized coal combustion experiments were conducted with and without protrusions of the type shown in the figure.
突起物を設けた羽口の展開図と断面図を第3図に示す9
図示したように、突起物は微粉炭吹込ランス3の先端よ
り45m下流の位置を分岐点として左・右にそれぞれ4
5°の角度で高さ10mm、厚さ20酵の突起を全周角
320° (片側160°)にわたって設けたものであ
る。Figure 3 shows a developed view and a cross-sectional view of a tuyere with protrusions9.
As shown in the diagram, the protrusions are located 45 meters downstream from the tip of the pulverized coal injection lance 3, and the protrusions extend 45 meters to the left and right.
A projection with a height of 10 mm and a thickness of 20 mm is provided at an angle of 5 degrees over the entire circumferential angle of 320 degrees (160 degrees on one side).
第1表に実験条件および微粉炭燃焼率を示したが、ここ
に示した微粉炭燃焼率は羽口先端より炉内側へ700m
の羽口軸芯位置でサンプラーにより未燃焼チャーをサン
プリングし、その化学組成から次式によって求めたもの
である。Table 1 shows the experimental conditions and pulverized coal combustion rate.
The unburned char was sampled by a sampler at the tuyere axis position, and its chemical composition was determined by the following formula.
(SiO2%”+A/、O,%0)
ここで、
α:燃焼率(%)、
C,、SiO2%、JV z O* %:微粉炭のC
,Sto!、 Nt(h含有量(wt%)、C” 、
Si島%” 、NtOx %“ :サンプリングし
た未燃焼チャーのC,Sin!。(SiO2%”+A/, O,%0) Here, α: Combustion rate (%), C,, SiO2%, JV z O* %: C of pulverized coal
, Sto! , Nt (h content (wt%), C'',
Si Island %", NtOx %": C, Sin! of sampled unburned char! .
A1.O,含有量(11E%)
なお、羽口先端より700m5の距離は、実高炉ではレ
ースウェイの深さに概ね相当しており、この位置で少な
くとも80%以上の燃焼率が得られれば、実高炉では問
題なく微粉炭吹込操業が実施可能であり、70%以下に
なると通気阻害などの悪影響を及ぼすことが経験的にわ
かっている。A1. O, content (11E%) Note that the distance of 700 m5 from the tip of the tuyere roughly corresponds to the raceway depth in an actual blast furnace, and if a combustion rate of at least 80% or more can be obtained at this position, In a blast furnace, pulverized coal injection operation can be carried out without any problems, and it has been empirically known that if the ratio is less than 70%, there will be adverse effects such as ventilation obstruction.
第1表の実験結果に示すように、羽口内にらせん状突起
物を設け、かつこの突起物に微粉炭とその搬送ガスの混
相流が当たるように微粉炭吹込ランスをセットした場合
に飛躍的に燃焼率が向上している。なお、突起物があれ
ば微粉炭吹込ランスを羽口中央にセットした場合(実験
No、2)でも燃焼率の向上効果は得られているが、混
相流が突起物に当たるように微粉炭吹込ランスをセット
した場合(実験階4)に比べるとその効果は小さい。As shown in the experimental results in Table 1, when a spiral protrusion is provided in the tuyere and the pulverized coal injection lance is set so that the multiphase flow of pulverized coal and its carrier gas hits this protrusion, a dramatic increase in The combustion rate has been improved. In addition, if there is a protrusion, the effect of improving the combustion rate can be obtained even when the pulverized coal injection lance is set in the center of the tuyere (Experiment No. 2). The effect is smaller than when set (Experimental floor 4).
〈発明の効果〉
本発明方法によると、高炉レースウェイ内での微粉炭の
燃焼率を飛躍的に高めることができ、これによって従来
技術では達成できなかった150kg/[−ρig以上
の微粉炭吹込ができた。<Effects of the Invention> According to the method of the present invention, the combustion rate of pulverized coal in the blast furnace raceway can be dramatically increased, thereby achieving a pulverized coal injection rate of 150 kg/[-ρig or more, which could not be achieved with the conventional technology. was completed.
第1図、第2図は、本発明に係る突起物およびW!粉炭
とその搬送ガスの混相流の流れの説明図で、(a)は羽
口断面図、(b)は(a)の展開図、(C)は(a)の
側断面図、第3図は、実施例に用いた突起物の説明図で
、(a)は羽口断面図、(b)は(a)の展開図、第4
図は、高炉への微粉炭吹込状況を示す模式図である。
・・・羽 目、 2・・・フローパイプ、・
・・微粉炭吹込ランス、
・・・微粉炭とその搬送ガスの混相流、・・・レースウ
ェイ、 6・・・突起物、・・・炉内壁面、
8・・・熱 風。
特許出願人 川崎製鉄株式会社FIGS. 1 and 2 show protrusions and W! according to the present invention. An explanatory diagram of the flow of a multiphase flow of powdered coal and its carrier gas, (a) is a cross-sectional view of the tuyere, (b) is a developed view of (a), (C) is a side cross-sectional view of (a), and Fig. 3 are explanatory diagrams of the protrusions used in the examples, where (a) is a cross-sectional view of the tuyere, (b) is a developed view of (a), and the fourth
The figure is a schematic diagram showing the state of pulverized coal injection into a blast furnace. ...Wings, 2...Flow pipe,...
...Pulverized coal injection lance, ...Multiphase flow of pulverized coal and its carrier gas, ...Raceway, 6.Protrusions, ...Furnace inner wall surface,
8...Hot wind. Patent applicant: Kawasaki Steel Corporation
Claims (1)
は逆ハ字状の突起物を設け、この突起物に微粉炭吹込ラ
ンスから吹込まれた微粉炭とその搬送ガスの混相流が吹
当たるようにしたことを特徴とする高炉への微粉炭吹込
方法。A spiral or inverted V-shaped protrusion is provided on the inner surface of the tuyere and/or blowpipe, so that the multiphase flow of pulverized coal and its carrier gas blown from the pulverized coal injection lance is blown onto the protrusion. A method for injecting pulverized coal into a blast furnace, which is characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11024690A JPH049414A (en) | 1990-04-27 | 1990-04-27 | Method for blowing pulverized coal to blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11024690A JPH049414A (en) | 1990-04-27 | 1990-04-27 | Method for blowing pulverized coal to blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH049414A true JPH049414A (en) | 1992-01-14 |
Family
ID=14530820
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11024690A Pending JPH049414A (en) | 1990-04-27 | 1990-04-27 | Method for blowing pulverized coal to blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH049414A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014047390A (en) * | 2012-08-31 | 2014-03-17 | Jfe Steel Corp | Pulverized coal injection device for blast furnace and pulverized coal injection method into blast furnace |
-
1990
- 1990-04-27 JP JP11024690A patent/JPH049414A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014047390A (en) * | 2012-08-31 | 2014-03-17 | Jfe Steel Corp | Pulverized coal injection device for blast furnace and pulverized coal injection method into blast furnace |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES8405138A1 (en) | Method and apparatus for injecting pulverized fuel into a blast furnace | |
JP2012188743A (en) | Method for operating blast furnace | |
CN105838845A (en) | Supersonic circulating combustion coherent arbon-oxygen lance of electric arc furnace and spray head structure | |
Dong et al. | Research on nozzle design and application of single‐flow postcombustion oxygen lance in a 120 t top‐blown converter | |
JP3450205B2 (en) | How to inject auxiliary fuel into the blast furnace | |
JPH049414A (en) | Method for blowing pulverized coal to blast furnace | |
US3758090A (en) | Combustion apparatus for blast furnaces | |
JPS62192509A (en) | Method for blowing pulverized carbon into blast furnace | |
JPH0192304A (en) | Nozzle for blowing finely powdered coal in blast furnace | |
CN107406895B (en) | Method for operating blast furnace | |
US3793002A (en) | Method of introducing a combustible auxiliary liquid into blast furnace and a tuyere for carrying out the method | |
JPH049415A (en) | Method for blowing pulverized coal to blast furnace | |
JP2953255B2 (en) | Method and apparatus for injecting solid fuel into blast furnace | |
JP3493937B2 (en) | How to blow pulverized coal into the blast furnace | |
KR20140109964A (en) | Blast furnace operation method | |
CN2191864Y (en) | Spray gun for jetting coal powder in blast furnace | |
JPH08157916A (en) | Blowing of pulverized fine coal into blast furnace and lance for blowing pulverized fine coal | |
CN201873702U (en) | Belly pipe with pulverized coal burning function | |
JP4779272B2 (en) | Method of injecting pulverized coal into the blast furnace | |
JP3492929B2 (en) | Pulverized coal injection tuyere structure in blast furnace | |
JPH08303756A (en) | Melting and combustion device | |
JP3644862B2 (en) | Auxiliary fuel injection operation method to blast furnace | |
KR20030005779A (en) | A pulverized solid fuel injecting apparatus | |
JP3644856B2 (en) | Auxiliary fuel injection operation method to blast furnace | |
JP2004285425A (en) | Method for blowing pulverized coal into blast furnace |