JP2963422B2 - Pulverized coal burner for blast furnace operation - Google Patents

Pulverized coal burner for blast furnace operation

Info

Publication number
JP2963422B2
JP2963422B2 JP9343646A JP34364697A JP2963422B2 JP 2963422 B2 JP2963422 B2 JP 2963422B2 JP 9343646 A JP9343646 A JP 9343646A JP 34364697 A JP34364697 A JP 34364697A JP 2963422 B2 JP2963422 B2 JP 2963422B2
Authority
JP
Japan
Prior art keywords
pulverized coal
tuyere
pipe
oxygen
burner
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
JP9343646A
Other languages
Japanese (ja)
Other versions
JPH111708A (en
Inventor
陽太郎 大野
武 古川
正博 松浦
雅之 渡部
三郎 桜井
博之 中村
雅男 川本
誠吾 玄蕃
尚武 山田
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 FUAANESU KOGYO KK
JFE Engineering Corp
Original Assignee
NIPPON FUAANESU KOGYO KK
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 NIPPON FUAANESU KOGYO KK, Nippon Kokan Ltd filed Critical NIPPON FUAANESU KOGYO KK
Priority to JP9343646A priority Critical patent/JP2963422B2/en
Publication of JPH111708A publication Critical patent/JPH111708A/en
Application granted granted Critical
Publication of JP2963422B2 publication Critical patent/JP2963422B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • Y02E20/322

Landscapes

  • Air Supply (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】この発明は高炉操業において使用
する微粉炭バーナの構造に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a structure of a pulverized coal burner used in blast furnace operation.

【0002】[0002]

【従来の技術】現在稼動している大型高炉の操業におい
ては、通常1100〜1300℃の熱風と共に還元剤と
してのコークスの一部を微粉炭で置換して羽口から吹き
込んでいる。酸素富化操業を行なう場合でも通常の酸素
富化率は数%に過ぎず、吹込まれる微粉炭も100kg/t
程度が限度とされていたが、近年炉頂から装入されるコ
ークスの原単位を更に低減せしめ低品質の微粉炭に代替
して羽口からより多くの微粉炭を吹込む技術が提案され
ている。これ等の技術においては従来の数倍もしくはそ
れ以上の酸素富化率において操業されるが、吹込まれる
微粉炭の量が多いために、通常、羽口前の送風支管の直
管部に斜め方向から吹き込む方式(図5)においては微
粉炭は羽口先レースウェイに到達する迄に燃焼して羽口
に溶融灰が堆積する等の障害がみられるようになった。
例えば特開昭62−263906号(図6)において
は、これらの障害を避けるために、微粉炭吹込みノズル
を送風支管に水平に設けて、バーナを微粉炭と酸素吹込
み用の2重構造とし、而も羽口先端と微粉炭吹込みノズ
ル間の距離を特定することが提案されている。
2. Description of the Related Art In the operation of a large blast furnace currently in operation, a part of coke as a reducing agent is usually replaced with pulverized coal along with hot air at 1100 to 1300 ° C. and blown from a tuyere. Even when performing oxygen-enriched operations, the normal oxygen enrichment rate is only a few percent, and the pulverized coal injected is 100 kg / t.
In recent years, a technique has been proposed in which the basic unit of coke charged from the furnace top is further reduced, and more pulverized coal is injected from tuyeres instead of low-quality pulverized coal. I have. These technologies operate at an oxygen enrichment rate several times or more than the conventional ones.However, due to the large amount of pulverized coal to be injected, usually, the straight pipe section of the blower branch pipe in front of the tuyere is inclined. In the method of injecting from the direction (FIG. 5), pulverized coal burns before reaching the tuyere raceway, and obstacles such as accumulation of molten ash at the tuyere have been observed.
For example, in Japanese Patent Application Laid-Open No. 62-263906 (FIG. 6), in order to avoid these obstacles, a pulverized coal injection nozzle is provided horizontally in a blower branch pipe, and a burner has a double structure for pulverized coal and oxygen injection. It has also been proposed to specify the distance between the tuyere tip and the pulverized coal injection nozzle.

【0003】[0003]

【発明が解決しようとする課題】前述の特開昭62−2
63906号等の高炉操業法は、その実施例からも明ら
かなように、通常の酸素富化率よりも遥かに高率ではあ
るが、O2濃度は37%程度を前提としており、O2濃度を
40%以上とする酸素高炉の操業条件においては前述の
改良程度では未だ不充分であり、高濃度酸素による操業
を安定に且つ永続的に続けるためには羽口先温度調整ガ
スの使用は不可欠であり、而も羽口先における燃焼状況
の把握が極めて重要である等、未解決の課題が多い。本
発明はこのような現状に鑑み創案されたものであり、大
量の微粉炭を炉況を悪化せしめることなく、而も羽口の
寿命を短くすることなしに安定して燃焼せしめることの
可能な装置を提供することを目的とする。
SUMMARY OF THE INVENTION The aforementioned Japanese Patent Laid-Open Publication No. Sho 62-2
Blast furnace operation method No. etc. 63 906, as is clear from the examples, there is a much higher rate than normal oxygen Tomikaritsu, O 2 concentration is assumed about 37%, O 2 concentration Under the operating conditions of an oxygen blast furnace in which the temperature is set to 40% or more, the above-mentioned degree of improvement is still insufficient, and the use of a tuyere temperature adjusting gas is indispensable in order to stably and permanently continue the operation with high-concentration oxygen. There are many unresolved issues such as grasping the combustion situation at the tuyere tip is extremely important. The present invention has been made in view of such a situation, and it is possible to stably burn a large amount of pulverized coal without deteriorating the furnace condition and without shortening the life of the tuyere. It is intended to provide a device.

【0004】[0004]

【課題を解決するための手段】(1) 微粉炭吹き込み
管と羽口先温度調整ガス吹き込み管および酸素吹き込み
管を配設したバーナの先端に羽口を連接し、前記微粉炭
と各種流体との混合流体が羽口の内面と接する位置を羽
口出口直径の1/2以下の長さだけ先端部から内側に入
った所となるようにノズルの噴出角度を決めたことを特
徴とする高炉操業用微粉炭バーナ。
Means for Solving the Problems (1) A tuyere is connected to a tip of a burner provided with a pulverized coal injection pipe, a tuyere temperature adjusting gas injection pipe, and an oxygen injection pipe, and the pulverized coal is mixed with various fluids. Blast furnace operation characterized in that the jetting angle of the nozzle is determined so that the position where the mixed fluid comes into contact with the inner surface of the tuyere is inward from the tip portion by a length equal to or less than 1/2 of the tuyere outlet diameter. For pulverized coal burners.

【0005】[0005]

【作用】本発明の微粉炭バーナは従来の高炉操業のよう
に熱風を用いず冷酸素を用いるため、構造上次の2点に
特徴を有している。 a) 微粉炭吹き込み管と羽口先温度調整ガス吹き込み管
および酸素吹き込み管を配設したバーナの先端に羽口を
連接したこと。 b) 前記微粉炭と各種流体との混合流体が羽口の内面と
接する位置を羽口出口直径の1/2以下の長さだけ先端
部から内側に入った所となるようにノズルの噴出角度を
決めたこと。
The pulverized coal burner of the present invention uses cold oxygen instead of hot air as in the conventional blast furnace operation, and therefore has the following two structural features. a) The tuyere was connected to the tip of the burner where the pulverized coal blowing pipe, the tuyere temperature adjusting gas blowing pipe and the oxygen blowing pipe were installed. b) The jet angle of the nozzle such that the mixed fluid of the pulverized coal and the various fluids comes into contact with the inner surface of the tuyere from the tip end by a length of 1/2 or less of the tuyere exit diameter. Decided.

【0006】a)は先端に羽口を設けたノズルが微粉炭吹
き込み管と羽口先温度調整ガス吹き込み管および酸素吹
き込み管から成ることであって、羽口先温度調整ガス吹
き込み管からの調整ガスによって吹き込まれた微粉炭の
燃焼拡大化を抑制して羽口の損傷を防止すると共に酸素
と微粉炭との混合を良好として効率的な微粉炭燃焼を図
る。前記した羽口先温度調整ガスとしては水蒸気、高炉
ガス、コークス炉ガス、又はN2ガス、CO2 ガス、等の不
活性ガスもしくは分解が吸熱反応を伴なうガスであり、
鉄鉱石の還元に悪影響がなければ特に限定はない。
A) The nozzle having a tuyere at the tip is composed of a pulverized coal blowing pipe, a tuyere-tip temperature adjusting gas blowing pipe and an oxygen blowing pipe, and is controlled by the adjusting gas from the tuyere-tip temperature adjusting gas blowing pipe. It is intended to suppress the expansion of combustion of the pulverized coal injected to prevent the tuyere from being damaged, and to improve the mixing of oxygen and pulverized coal for efficient pulverized coal combustion. The tuyere temperature control gas above the water vapor, a blast furnace gas, coke oven gas, or N 2 gas, CO 2 gas, accompanied gas inert gas or decomposition endothermic reaction of equal,
There is no particular limitation as long as there is no adverse effect on the reduction of iron ore.

【0007】b)について言うならば通常の酸素富化操業
の羽口に比較すればかなり大量の微粉炭が高酸素濃度の
雰囲気で燃焼されるから羽口への障害は厳しく調べてお
く必要がある。障害としては未燃焼の微粉炭を含む混合
流体が羽口内面に衝突し内面が摩耗するトラブル、もし
くは燃焼し溶融したAsh が羽口内面もしくは先端部に堆
積することにより生ずるトラブルがある。従って微粉炭
吹き込み管、羽口先温度調整ガス吹き込み管、酸素吹き
込み管を配設したバーナの先端に突出連接された羽口に
対し微粉炭と前記した各種流体との混合流体の外縁が接
する位置を羽口先端部から特定の位置として、前記した
ようなトラブルを有効に防止する。
As for b), since a considerably large amount of pulverized coal is burned in an atmosphere having a high oxygen concentration as compared with a tuyere of a normal oxygen-enriched operation, it is necessary to strictly examine the obstacle to the tuyere. is there. As an obstacle, there is a problem that the mixed fluid containing unburned pulverized coal collides with the inner surface of the tuyere and wears the inner surface, or a problem that occurs due to accumulation of burned and molten Ash on the inner surface or the tip of the tuyere. Therefore, the position where the outer edge of the mixed fluid of the pulverized coal and the various fluids described above comes into contact with the tuyere projecting and connected to the tip of the burner provided with the pulverized coal blowing pipe, the tuyere tip temperature adjusting gas blowing pipe, and the oxygen blowing pipe. The above-mentioned trouble is effectively prevented at a specific position from the tuyere tip.

【0008】また上記のようにされることにより微粉炭
と温度調整ガスおよび酸素の混合を有効に図り多量の微
粉炭を適切に燃焼せしめる。なおバーナ本体とガスの漏
洩を防止し且つ小羽口を炉体に固定する機構を別々にし
て小羽口にかかる応力がバーナ本体に及ばないようにバ
ーナ本体と摺動管は気密に接触されてはいるが摺動でき
るようにすることが好ましく、また常温の高濃度酸素が
用いられるから必ずしも微粉炭バーナの外側を冷却水管
とする必要はなく、摺動外はSUS等の耐蝕性鋼管を使
用することができる。更に小羽口の後端部に気密に接す
る微粉炭バーナの先端部もしくは摺動管の先端に形成さ
れる摺動座17の面は球面もしくは円錐体の曲面で形成
され小羽口の動きに追従できるようにしておくことが好
ましい。
[0008] In addition, the above-described method effectively mixes the pulverized coal with the temperature control gas and oxygen, thereby appropriately burning a large amount of the pulverized coal. The burner body and the sliding tube must be kept in airtight contact with each other so that the burner body and the mechanism for preventing gas leakage and fixing the small tuyere to the furnace body are separated so that the stress applied to the small tuyere does not reach the burner body. However, it is preferable to be able to slide, and since high-concentration oxygen at room temperature is used, it is not always necessary to provide a cooling water pipe outside the pulverized coal burner, and use a corrosion-resistant steel pipe such as SUS outside the slide. be able to. Further, the surface of the sliding seat 17 formed at the end of the pulverized coal burner or at the end of the sliding pipe which is in air-tight contact with the rear end of the small tuyere is formed as a spherical or conical curved surface and can follow the movement of the small tuyere. It is preferable to do so.

【0009】[0009]

【実施例】図1は本発明の高炉操業用微粉炭バーナにお
ける基部側の縦断面を示すものである。中央部に炉内監
視管1が配置されており、この管はバーナの基部から先
端部まで延びている。該炉内監視管1の内側には空気入
口2より管内に舞い込んだ微粉炭等を吹払う清浄用空気
が間欠的に導入されるようになっている。またこの炉内
監視管1は仕切弁3を介して覗窓4と連通されており、
ここから肉眼によりもしくは計測器により炉内より情報
を得ることができる。上記のような監視用管1の外側に
同心円状に微粉炭吹き込み管5が設けられており、微粉
炭供給口6より吹き込み管5内に微粉炭が送り込まれ
る。同様にその外側に羽口先温度調整ガス吹き込み管7
が配設され羽口先温度調整ガス供給口8よりガス(この
実施例では水蒸気)が供給されるようになっている。羽
口先温度調整ガス吹き込み管7の外側には酸素管9が設
けられ、酸素供給口10から酸素が送り込まれるが、バ
ーナの最も外側は冷却水管11であって冷却水供給口1
2、冷却水排出口13が設けられている。
FIG. 1 shows a vertical section of a base side of a pulverized coal burner for blast furnace operation according to the present invention. An in-furnace monitoring tube 1 is arranged at the center, and extends from the base to the tip of the burner. Cleaning air for blowing off pulverized coal and the like blown into the pipe from the air inlet 2 is intermittently introduced into the inside of the furnace monitoring pipe 1. The furnace monitoring pipe 1 is communicated with a viewing window 4 through a gate valve 3.
From here, information can be obtained from inside the furnace with the naked eye or with a measuring instrument. A pulverized coal blowing pipe 5 is provided concentrically outside the monitoring pipe 1 as described above, and pulverized coal is fed into the blowing pipe 5 from a pulverized coal supply port 6. Similarly, a tuyere temperature adjusting gas injection pipe 7
And a gas (steam in this embodiment) is supplied from the tuyere temperature adjusting gas supply port 8. An oxygen pipe 9 is provided outside the tuyere tip temperature adjusting gas blowing pipe 7 and oxygen is supplied from an oxygen supply port 10. The outermost burner is a cooling water pipe 11 and a cooling water supply port 1 is provided.
2. A cooling water outlet 13 is provided.

【0010】図2は図1に記載した微粉炭バーナの先端
部の縦断面を示すもので、炉内監視用管1、微粉炭吹き
込み管5、羽口先温度調整ガス吹き込み管7、酸素吹き
込み管9、が同心円状に図示されている。この実施例に
おいてはバーナの軸線に平行な噴出口を有する微粉炭吹
出ノズル14の外側に、先端開口部がバーナの軸線方向
に対し内側に傾斜している羽口先温度調整ガス吹出ノズ
ル15、酸素吹出ノズル16が設けられており、バーナ
を出た混合流体が羽口18に影響を与えることのないよ
うに配慮されている。バーナの先端外周部には羽口18
の後端部と気密に接するための摺動座17が形成されて
いる。
FIG. 2 shows a longitudinal section of the tip of the pulverized coal burner shown in FIG. 1. The furnace monitoring pipe 1, the pulverized coal injection pipe 5, the tuyere temperature adjusting gas injection pipe 7, the oxygen injection pipe. 9 are shown concentrically. In this embodiment, outside the pulverized coal blowing nozzle 14 having a discharge port parallel to the axis of the burner, a tuyere temperature adjusting gas blowing nozzle 15 having a tip opening inclined inward with respect to the axial direction of the burner, oxygen, An outlet nozzle 16 is provided to prevent the mixed fluid exiting the burner from affecting the tuyere 18. Tuyere 18 at the outer periphery of the tip of the burner
A sliding seat 17 is formed for hermetically contacting the rear end.

【0011】図3は前述の水冷ジャケットを使用する代
りに耐熱鋼からなる摺動管19を摺動自在に設けたもの
であるが、先端部には同様に摺動座17が形成されてい
る。
FIG. 3 shows a sliding pipe 19 made of heat-resistant steel slidably provided instead of using the above-mentioned water-cooled jacket. A sliding seat 17 is similarly formed at the tip end. .

【0012】図4は前図の場合と異なり、微粉炭吹出ノ
ズル14の先端開口部はバーナの軸線より外側に傾斜し
て設けられた例を示すもので、微粉炭と各種流体との混
合流体最外縁が羽口18の内面と接する位置を示したも
のであり、羽口出口直径Dの1/2以下の長さHだけ先
端部から内側に入った所が混合流体の最外縁となるよう
にノズル14の噴出角度を決め、その外側をノズル15
および16からの流体で抑制するようにしたものであ
る。
FIG. 4 shows an example in which the tip opening of the pulverized coal blowing nozzle 14 is provided to be inclined outside the axis of the burner, unlike the case of the previous figure, and is a mixed fluid of pulverized coal and various fluids. The position where the outermost edge is in contact with the inner surface of the tuyere 18 is shown, and the portion entering the inside from the tip portion by a length H which is 1 / or less of the tuyere outlet diameter D becomes the outermost edge of the mixed fluid. The ejection angle of the nozzle 14 is determined at
And the fluid from 16.

【0013】[0013]

【発明の効果】以上詳細に説明したように、酸素高炉に
おいて本発明の微粉炭バーナを使用する場合には送風と
して、純酸素あるいは高濃度の酸素にて操業する際にお
いて炉況を損うことなく大量の微粉炭を安全に且つ小羽
口への影響も殆んどなく燃焼せしめることができ、微粉
炭吹き込み管と羽口先温度調整ガス吹き込み管、酸素吹
き込み管を有効に組み合わせ、微粉炭吹き込み管から吹
き込まれた微粉炭の拡大化を抑制して羽口の損傷を防止
すると共に微粉炭との混合を良好として効率的な微粉炭
燃焼を図らしめるなどの特質を有し、工業的にその効果
を高く期待することができる。
As described in detail above, when the pulverized coal burner of the present invention is used in an oxygen blast furnace, the furnace condition is impaired when operating with pure oxygen or high-concentration oxygen as the air blow. A large amount of pulverized coal can be burned safely and with little effect on the small tuyere, and a pulverized coal injection pipe is effectively combined with a pulverized coal injection pipe, a tuyere temperature adjusting gas injection pipe, and an oxygen injection pipe. It has characteristics such as preventing the tuyere from being damaged by preventing the pulverized coal injected from the tank from expanding and improving mixing with the pulverized coal for efficient pulverized coal combustion. Can be expected to be high.

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

【図1】本発明の高炉操業用微粉炭バーナの基部側縦断
面図である。
FIG. 1 is a vertical sectional view of a base side of a pulverized coal burner for blast furnace operation of the present invention.

【図2】前記バーナの先端部縦断面図である。FIG. 2 is a longitudinal sectional view of a tip portion of the burner.

【図3】冷却水管の代りに摺動管を使用した本発明の他
の実施例(先端部の縦断面)の図である。
FIG. 3 is a view of another embodiment (longitudinal section at the tip) of the present invention using a sliding pipe instead of a cooling water pipe.

【図4】本発明における小羽口に対する混合流体の接触
点を示す説明図である。
FIG. 4 is an explanatory diagram showing a contact point of a mixed fluid with a small tuyere in the present invention.

【図5】従来の送風支管の図である。FIG. 5 is a view of a conventional ventilation branch pipe.

【図6】高酸素富化時の送風支管の従来例を示す図であ
る。
FIG. 6 is a view showing a conventional example of a ventilation branch pipe at the time of high oxygen enrichment.

【符号の説明】[Explanation of symbols]

1 炉内監視管 2 空気入口 3 仕切弁 4 覗窓 5 微粉炭吹き込み管 6 微粉炭供給口 7 羽口先温度調整ガス吹き込み管 8 羽口先温度調整ガス供給口 9 酸素吹き込み管 10 酸素供給口 11 冷却水管 12 冷却水供給口 13 冷却水排出口 14 微粉炭吹出ノズル 15 羽口先温度調整ガス吹出ノズル 16 酸素吹出ノズル 17 摺動座 18 羽口 19 摺動管 DESCRIPTION OF SYMBOLS 1 Furnace monitoring pipe 2 Air inlet 3 Gate valve 4 Viewing window 5 Pulverized coal injection pipe 6 Pulverized coal supply port 7 Tuyere tip temperature adjustment gas injection pipe 8 Tuyere tip temperature adjustment gas supply port 9 Oxygen injection pipe 10 Oxygen supply port 11 Cooling Water pipe 12 Cooling water supply port 13 Cooling water discharge port 14 Pulverized coal blowing nozzle 15 Tuyere temperature adjusting gas blowing nozzle 16 Oxygen blowing nozzle 17 Sliding seat 18 Tuyere 19 Sliding pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 松浦 正博 東京都千代田区丸の内一丁目1番2号 日本鋼管株式会社内 (72)発明者 渡部 雅之 東京都千代田区丸の内一丁目1番2号 日本鋼管株式会社内 (72)発明者 桜井 三郎 東京都千代田区丸の内一丁目1番2号 日本鋼管株式会社内 (72)発明者 中村 博之 神奈川県横浜市南区別所2−18−37 (72)発明者 川本 雅男 神奈川県横浜市磯子区磯子5−10−1− 206 (72)発明者 玄蕃 誠吾 神奈川県横浜市旭区中尾町47−67 (72)発明者 山田 尚武 神奈川県三浦郡葉山町一色748−6 (56)参考文献 特開 昭63−171818(JP,A) (58)調査した分野(Int.Cl.6,DB名) C21B 7/00 309 F23D 1/00 F23L 7/00 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Masahiro Matsuura 1-1-2 Marunouchi, Chiyoda-ku, Tokyo Nippon Kokan Co., Ltd. (72) Inventor Masayuki Watanabe 1-1-2 Marunouchi, Chiyoda-ku, Tokyo Nippon Kokan Incorporated (72) Inventor Saburo Sakurai 1-1-2 Marunouchi, Chiyoda-ku, Tokyo Nippon Kokan Co., Ltd. (72) Inventor Hiroyuki Nakamura 2-18-37, Minami-Doshibori, Yokohama-shi, Kanagawa (72) Inventor Masao Kawamoto 5-10-1-206 Isogo, Isogo-ku, Yokohama-shi, Kanagawa Prefecture (72) Inventor Seigo Genban 47-67, Nakao-cho, Asahi-ku, Yokohama-shi, Kanagawa Prefecture (72) Naototake Yamada 748- Isshiki, Hayamacho, Miura-gun, Kanagawa 6 (56) References JP-A-63-171818 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) C21B 7/00 309 F23D 1/00 F23L 7/00

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 微粉炭吹き込み管と羽口先温度調整ガス
吹き込み管および酸素吹き込み管を配設したバーナの先
端に羽口を連接し、前記微粉炭と各種流体との混合流体
が羽口の内面と接する位置を羽口出口直径の1/2以下
の長さだけ先端部から内側に入った所となるようにノズ
ルの噴出角度を決めたことを特徴とする高炉操業用微粉
炭バーナ。
1. A tuyere is connected to a tip of a burner provided with a pulverized coal injection pipe, a tuyere tip temperature adjusting gas injection pipe and an oxygen injection pipe, and a mixed fluid of the pulverized coal and various fluids is supplied to an inner surface of the tuyere. The pulverized coal burner for blast furnace operation , characterized in that the jetting angle of the nozzle is determined such that the position in contact with the inside of the tuyere outlet is not more than 1/2 of the tuyere outlet diameter.
JP9343646A 1997-12-01 1997-12-01 Pulverized coal burner for blast furnace operation Expired - Fee Related JP2963422B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9343646A JP2963422B2 (en) 1997-12-01 1997-12-01 Pulverized coal burner for blast furnace operation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9343646A JP2963422B2 (en) 1997-12-01 1997-12-01 Pulverized coal burner for blast furnace operation

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP63096853A Division JP2761885B2 (en) 1988-04-21 1988-04-21 Pulverized coal burner

Publications (2)

Publication Number Publication Date
JPH111708A JPH111708A (en) 1999-01-06
JP2963422B2 true JP2963422B2 (en) 1999-10-18

Family

ID=18363147

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9343646A Expired - Fee Related JP2963422B2 (en) 1997-12-01 1997-12-01 Pulverized coal burner for blast furnace operation

Country Status (1)

Country Link
JP (1) JP2963422B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4537602B2 (en) * 2001-03-08 2010-09-01 新日鉄エンジニアリング株式会社 Combustible dust injection method in waste melting furnace
JP6053295B2 (en) * 2012-02-23 2016-12-27 三菱重工業株式会社 Biomass burning burner and combustion apparatus equipped with the same

Also Published As

Publication number Publication date
JPH111708A (en) 1999-01-06

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