JPH09143520A - Method for injecting pulverized fine coal into blast furnace - Google Patents

Method for injecting pulverized fine coal into blast furnace

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Publication number
JPH09143520A
JPH09143520A JP32113295A JP32113295A JPH09143520A JP H09143520 A JPH09143520 A JP H09143520A JP 32113295 A JP32113295 A JP 32113295A JP 32113295 A JP32113295 A JP 32113295A JP H09143520 A JPH09143520 A JP H09143520A
Authority
JP
Japan
Prior art keywords
tuyere
pressure loss
blowing
furnace
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.)
Pending
Application number
JP32113295A
Other languages
Japanese (ja)
Inventor
Keiji Oshima
啓示 大島
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
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP32113295A priority Critical patent/JPH09143520A/en
Publication of JPH09143520A publication Critical patent/JPH09143520A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a pulverized fine coal blowing means which improves the ventilation in a blast furnace and can stably blow the pulverized fine coal, by independently controlling pressure losses at a blasting tuyere part and a raceway part. SOLUTION: In the method for blowing the pulverized fine coal into the furnace from the blasting tuyere together with the hot blast flowed in a blow pipe by projecting a pulverized fine coal blowing nozzle in the blow pipe by penetrating the wall of the blow pipe for blowing the hot blast connected to the blasting tuyere, when the pressure loss in the blasting tuyere exceeds a reference value, the tip position of the nozzle for blowing the pulverized fine coal is shifted into the furnace inner side to lower the pressure loss at the blast tuyere part. When the pressure loss at the raceway part exceeds a reference value, the coke strength is increased to lower the pressure loss at the raceway part.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】この発明は、高炉へ微粉炭を
吹込む技術に係り、より詳しくは羽口レベルの圧力損失
を適正に制御することによって高炉通気性を改善する高
炉への微粉炭吹込方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for injecting pulverized coal into a blast furnace, and more particularly, to injecting pulverized coal into a blast furnace for improving blast furnace air permeability by appropriately controlling pressure loss at the tuyere level. Regarding the method.

【0002】[0002]

【従来の技術】近年、高炉技術の発展により羽口から高
炉内へ補助燃料として重油が吹込まれるようになり、さ
らにその後のエネルギー事情を反映して、経済的観点か
ら重油に代えて安価な微粉炭を高炉に吹込む方法が実用
化されている。
2. Description of the Related Art In recent years, due to the development of blast furnace technology, heavy oil has been blown from the tuyere into the blast furnace as an auxiliary fuel, and further reflecting the energy situation thereafter, it is economical and economical to replace heavy oil. A method of blowing pulverized coal into a blast furnace has been put into practical use.

【0003】微粉炭を高炉に吹込む方法としては、周知
の通り、高炉の送風羽口に連設された熱風吹込用ブロー
パイプの壁を貫通して微粉炭吹込ノズルを該ブローパイ
プ内に突出させ、ブローパイプ内を流れる熱風と共に送
風羽口から炉内へ吹込む方法が一般的である。
As is well known, as a method for blowing pulverized coal into a blast furnace, a pulverized coal injection nozzle is projected into the blow pipe by penetrating through the wall of a hot air blowing blow pipe connected to the blowing tuyere of the blast furnace. Then, a method of blowing the blown air into the furnace together with the hot air flowing in the blow pipe is common.

【0004】このような微粉炭の吹込方法においては、
微粉炭が羽口やレースウェイ内で完全に燃焼し尽くさな
いと燃焼率が悪化する。かかる対策としては、例えば微
粉炭の吹込み位置を羽口と反対方向(上流側)に移動さ
せて微粉炭吹込用ノズルの先端位置と羽口との距離を大
きくして燃焼率を向上させる方法が知られている。しか
し、微粉炭の吹込み位置を上流側に移動させると、微粉
炭に含有されている灰分がブローパイプの内面に付着、
堆積し易くなり、微粉炭の安定吹込みが困難になるのみ
ならず、羽口からの熱風吹込みが不安定になるという問
題がある。
In such a pulverized coal blowing method,
If the pulverized coal is not completely burned in the tuyere or raceway, the burning rate will deteriorate. As a countermeasure, for example, a method of moving the pulverized coal blowing position in the direction opposite to the tuyere (upstream side) to increase the distance between the tip position of the pulverized coal blowing nozzle and the tuyere to improve the combustion rate. It has been known. However, when the blowing position of the pulverized coal is moved to the upstream side, the ash content contained in the pulverized coal adheres to the inner surface of the blow pipe,
There is a problem that not only the accumulation becomes easy and stable blowing of pulverized coal becomes difficult, but also the blowing of hot air from the tuyere becomes unstable.

【0005】そこで、例えば特公昭60−53081号
公報には、微粉炭吹込用ノズルの位置をある範囲内に設
定することにより、灰分の付着、堆積を防止しつつ微粉
炭の燃焼率を向上させる方法が提案されている。
Therefore, for example, in Japanese Patent Publication No. 60-53081, the position of the pulverized coal blowing nozzle is set within a certain range to improve the burning rate of pulverized coal while preventing ash deposition and deposition. A method has been proposed.

【0006】[0006]

【発明が解決しようとする課題】しかし、微粉炭の燃焼
率を向上させるため羽口前レースウェイ内で微粉炭を完
全燃焼させると、コークスのソリューションロスガス化
反応による劣化が進行し、炉下部のコークス粒径を低下
させることになるとともに、コークスの羽口前での消費
量が低下するため、羽口前へのコークスの供給速度が低
下し、高炉下部でのコークスの置換時間が延長され、そ
の結果、高炉内滞留コークスの劣化を促進し、炉下部コ
ークスの粒径低下をきたし、高炉の通気性を悪化させる
という問題が生ずる。
However, when the pulverized coal is completely burned in the front tuyere raceway in order to improve the burning rate of the pulverized coal, deterioration due to the solution loss gasification reaction of coke progresses and the lower part of the furnace is advanced. In addition to reducing the coke particle size of the coke, the consumption of coke in front of the tuyere decreases, so the coke supply speed to the front of the tuyere decreases, and the coke replacement time in the lower part of the blast furnace is extended. As a result, there is a problem that the deterioration of the coke staying in the blast furnace is promoted, the particle size of the coke in the lower part of the furnace is reduced, and the air permeability of the blast furnace is deteriorated.

【0007】この発明は、上記した高炉の通気性悪化の
問題を解決するためなされたもので、羽口部およびレー
スウェイ部での圧力損失を独立に制御することによって
炉内通気性を改善し、微粉炭を安定に吹込むことができ
る高炉への微粉炭吹込方法を提案しようとするものであ
る。
The present invention has been made to solve the above-mentioned problem of deterioration of air permeability in a blast furnace, and improves the air permeability in the furnace by independently controlling the pressure loss in the tuyere portion and the raceway portion. , A method for injecting pulverized coal into a blast furnace capable of stably injecting pulverized coal is proposed.

【0008】[0008]

【課題を解決するための手段】この発明は、送風羽口に
連設された熱風吹込用ブローパイプの壁を貫通して微粉
炭吹込ノズルを該ブローパイプ内に突出させ、ブローパ
イプ内を流れる熱風と共に送風羽口から炉内へ微粉炭を
吹込む方法において、送風羽口部およびレースウェイ部
の圧力損失を測定し、送風羽口部圧力損失が予め設定し
た基準値を超える場合には、前記微粉炭吹込ノズルの先
端位置を炉内側へ移動させて当該羽口部の圧力損失を低
下させ、レースウェイ部圧力損失が予め設定した基準値
を超える場合には、コークス強度を高めて当該レースウ
ェイ部圧力損失を低下させる方法を要旨とするものであ
る。
According to the present invention, a pulverized coal blowing nozzle is projected through the wall of a hot air blowing blow pipe connected to a blower tuyere, and flows through the blow pipe. In the method of blowing pulverized coal into the furnace from the blast tuyere with hot air, measuring the pressure loss of the blast tuyere and raceway part, if the blast tuyere pressure loss exceeds a preset reference value, When the tip position of the pulverized coal injection nozzle is moved to the inside of the furnace to reduce the pressure loss at the tuyere, and when the raceway pressure loss exceeds a preset reference value, the coke strength is increased to increase the race. The gist is a method of reducing the pressure loss in the way portion.

【0009】この発明において、高炉の炉内通気性を改
善する方法として、送風羽口部およびレースウェイ部の
圧力損失に着目したのは、送風羽口部およびレースウェ
イ部の圧力損失と炉内通気性との間に相関があることを
知見したことによる。すなわち、羽口部およびレースウ
ェイ部の圧力損失が高い場合は、炉内通気抵抗が低くな
ることを知見した。
In the present invention, as a method for improving the in-furnace air permeability of the blast furnace, attention was paid to the pressure loss at the blast tuyere and the raceway portion because the pressure loss at the blast tuyere and the raceway portion and the inside of the furnace This is due to the finding that there is a correlation with breathability. That is, it was found that when the pressure loss at the tuyere and the raceway is high, the ventilation resistance in the furnace becomes low.

【0010】この発明はかかる知見より、微粉炭吹込み
時に羽口部での圧力損失が高くなって基準値を超える場
合には、微粉炭吹込ノズルの先端位置を炉内側へ移動さ
せて羽口部での圧力損失の上昇を抑制し、また、レース
ウェイ部での圧力損失が高くなって基準値を超える場合
には、装入コークス強度(DI、CSR)を上げてレー
スウェイにおけるコークス旋回による粉化を抑制するこ
とでレースウェイ部の圧力損失を低下させる手段をこう
じたのである。
According to the present invention, when the pressure loss at the tuyere becomes higher than the reference value when the pulverized coal is injected, the tip position of the pulverized coal injection nozzle is moved to the inside of the furnace and the tuyere is obtained. Suppresses an increase in pressure loss in the raceway section, and when the pressure loss in the raceway section rises above the standard value, the charging coke strength (DI, CSR) is increased to cause coke turning in the raceway. This is the means to reduce the pressure loss in the raceway part by suppressing the pulverization.

【0011】ここで、羽口部およびレースウェイ部の圧
力損失をそれぞれ△Pa[MPa]、△Pb[MPa]
とすると、△Paと△Pbの基準値(上限値)は、羽口
部圧力損失とレースウェイ部圧力損失との関係より、△
Paの基準値は0.0031[MPa]、△Pbの基準
値は0.0245[MPa]と設定することができる。
Here, the pressure loss at the tuyere portion and the raceway portion are ΔPa [MPa] and ΔPb [MPa], respectively.
Then, the reference value (upper limit value) of ΔPa and ΔPb is Δ based on the relationship between the tuyere pressure loss and the raceway pressure loss.
The reference value of Pa can be set to 0.0031 [MPa], and the reference value of ΔPb can be set to 0.0245 [MPa].

【0012】すなわち、羽口部圧力損失△Paが0.0
031[MPa]を超えると、送風量の低下、または送
風圧力上昇による送風動力コストアップ、微粉炭吹込量
の低下をきたし、他方、レースウェイ部圧力損失△Pb
が0.0245[MPa]を超えると、吹き抜け、棚吊
り、スリップ等による炉況異常が発生するため、△Pa
と△Pbの基準値(上限値)は、それぞれ0.0031
[MPa]、0.0245[MPa]とするのが望まし
い。
That is, the tuyere pressure loss ΔPa is 0.0
When it exceeds 031 [MPa], the amount of blast decreases, or the blast power cost increases due to the increase in blast pressure, and the amount of pulverized coal injection decreases, while the pressure loss on the raceway part ΔPb.
When the value exceeds 0.0245 [MPa], abnormal furnace conditions due to blow-through, hanging on the shelf, slipping, etc. occur.
And the reference value (upper limit) of ΔPb are 0.0031 respectively.
[MPa] and 0.0245 [MPa] are desirable.

【0013】[0013]

【発明の実施の形態】図1はこの発明方法を実施するた
めの装置構成例を示す概略図で、1は高炉、2は送風羽
口、3は熱風吹込用ブローパイプ、4は微粉炭吹込ノズ
ル、5は圧力測定用ランス、6は圧力分布測定装置、7
は比較器、8はノズル位置制御装置、9はコークス強度
制御系、10はレースウェイを示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 is a schematic view showing an example of the construction of an apparatus for carrying out the method of the present invention. Nozzle, 5 is a pressure measuring lance, 6 is a pressure distribution measuring device, 7
Is a comparator, 8 is a nozzle position control device, 9 is a coke strength control system, and 10 is a raceway.

【0014】上記装置において、微粉炭は高炉1の送風
羽口2に連設された熱風吹込用ブローパイプ3の壁を貫
通して該ブローパイプ内に突出させた微粉炭吹込ノズル
4より、ブローパイプ3内を流れる熱風と共に送風羽口
2から炉内へ吹込まれる。
In the above apparatus, the pulverized coal is blown from the pulverized coal injection nozzle 4 which penetrates the wall of the hot air blowing blow pipe 3 connected to the blowing tuyere 2 of the blast furnace 1 and projects into the blow pipe. It is blown into the furnace from the blower tuyere 2 together with the hot air flowing in the pipe 3.

【0015】送風羽口2部およびレースウェイ10部の
圧力損失の測定方法としては、例えば送風羽口2より挿
入した圧力測定用ランス5の先端から炉内へ常時N
ージを行い、その一部を回収して、そのパージ圧と回収
圧より求める方法を用いる。
As a method for measuring the pressure loss in the blast tuyere 2 part and the raceway 10 part, for example, N 2 purge is always performed from the tip of the pressure measuring lance 5 inserted from the blast tuyere 2 into the furnace. A method is used in which a part is recovered and the purge pressure and the recovery pressure are used.

【0016】すなわち、この発明では、圧力分布測定装
置6により送風羽口2部およびレースウェイ10部の圧
力分布を測定し、羽口部圧力損失△Paとレースウェイ
部圧力損失△Pbを比較器7に入力する。比較器7で
は、前記実測の△Paと△Pbと、予め設定された△P
aと△Pbの基準値(上限値)とがそれぞれ比較され、
羽口部圧力損失△Paがその基準値0.0031[MP
a]を超える場合は、ノズル位置制御装置8に制御指令
が送られ微粉炭吹込ノズル4を炉内側に移動させ、ま
た、レースウェイ部圧力損失△Pbがその基準値0.0
245[MPa]を超える場合は、コークス強度制御系
9に制御指令が送られコークス強度を高める。なお、微
粉炭吹込ノズル4を炉内側に移動させる量は、羽口部圧
力損失△Pa値に応じて適宜設定する。通常は50mm
前後である。
That is, in the present invention, the pressure distribution measuring device 6 measures the pressure distribution in the blower tuyere 2 part and the raceway 10 part, and the tuyere pressure loss ΔPa and the raceway part pressure loss ΔPb are compared. Type in 7. In the comparator 7, the actually measured ΔPa and ΔPb, and the preset ΔP
a and the reference value (upper limit value) of ΔPb are respectively compared,
Tuyere pressure loss ΔPa is the standard value 0.0031 [MP
a] is exceeded, a control command is sent to the nozzle position control device 8 to move the pulverized coal injection nozzle 4 to the inside of the furnace, and the raceway portion pressure loss ΔPb is the reference value 0.0.
If it exceeds 245 [MPa], a control command is sent to the coke strength control system 9 to increase the coke strength. The amount of the pulverized coal blowing nozzle 4 moved to the inside of the furnace is appropriately set according to the tuyere pressure loss ΔPa value. Usually 50 mm
Before and after.

【0017】羽口部圧力損失△Paがその基準値0.0
031[MPa]を超えた場合に微粉炭吹込ノズル4を
炉内側に移動させると、羽口部での燃焼フレームがレー
スウェイ内に移動するため羽口部での圧力損失が低下す
る。また、レースウェイ部圧力損失△Pbがその基準値
0.0245[MPa]を超えた場合にコークス強度を
高めると、レースウェイ10内におけるコークス旋回に
よる粉化が抑制されるので、レースウェイ部の圧力損失
が低下する。
The tuyere pressure loss ΔPa is a reference value of 0.0
When the pulverized coal injection nozzle 4 is moved to the inside of the furnace when the pressure exceeds 031 [MPa], the combustion frame at the tuyere moves into the raceway, and the pressure loss at the tuyere decreases. Further, if the coke strength is increased when the pressure loss ΔPb of the raceway portion exceeds the reference value 0.0245 [MPa], powdering due to coke turning in the raceway 10 is suppressed. Pressure loss decreases.

【0018】[0018]

【実施例】炉内容積4800mの高炉において、図1
に示す方法で微粉炭(揮発分20〜45重量%)を吹込
んで操業したときの羽口部の圧力損失△Pa[MP
a]、レースウェイ部の圧力損失△Pb[MPa]と炉
内通気抵抗の関係を調べた結果を図2に示す。本実施例
における操業条件を表1に示す。
[Example] In a blast furnace having an inner volume of 4800 m 3 , FIG.
Pressure loss at the tuyere when operating by blowing pulverized coal (volatile content 20 to 45% by weight) by the method shown in
[a], the pressure loss ΔPb [MPa] in the raceway and the relationship between the ventilation resistance in the furnace are shown in FIG. Table 1 shows the operating conditions in this example.

【0019】本実施例では、図1に示すごとく、送風羽
口2より圧力測定用ランス5を挿入し、炉内へ常時N
パージを行い、そのときのパージ圧力と回収したガスの
圧力を利用して送風羽口部およびレースウェイ部の圧力
分布を測定した。図2は炉内通気抵抗が低い(1130
0〜11600[l/m])時の羽口部の圧力損失△P
a[MPa]およびレースウェイ部の圧力損失△Pb
[MPa]を黒丸で、炉内通気抵抗が高い場合(120
00〜12300[l/m])を白丸でそれぞれプロッ
トしたものである。
In the present embodiment, as shown in FIG. 1, a pressure measuring lance 5 is inserted from the blower tuyere 2 and N 2 is constantly fed into the furnace.
Purging was performed, and the pressure distribution at the blast tuyere and raceway was measured using the purge pressure and the pressure of the recovered gas at that time. 2 shows that the ventilation resistance in the furnace is low (1130
Pressure loss ΔP at the tuyere at 0-11600 [l / m])
a [MPa] and pressure loss in raceway part ΔPb
When [MPa] is a black circle and the ventilation resistance in the furnace is high (120
00-12300 [l / m]) are plotted by white circles.

【0020】図2のデータより明らかなごとく、羽口部
での圧力損失△Pa[MPa]が基準値(0.0031
MPa)を超えた場合は、微粉炭吹込ノズル4の先端位
置を炉内側に50mm移動させることで羽口部での圧力
損失を0.0008MPa下げることが可能となり、ま
た、レースウェイ部の圧力損失△Pb[MPa]が基準
値(0.0245MPaを超えた場合は、コークス強度
を高める(CSR:2.0→64.4、DI:184.
0→84.5)ことでレースウェイ部の圧力損失を0.
0054〜0.0073MPa下げることができた。そ
の結果、炉内通気抵抗が400〜1000[l/m]改
善され、微粉炭を安定に吹込むことができた。
As is clear from the data of FIG. 2, the pressure loss ΔPa [MPa] at the tuyere is the reference value (0.0031).
When the pressure exceeds 500 MPa, it is possible to reduce the pressure loss at the tuyere by 0.00008 MPa by moving the tip position of the pulverized coal blowing nozzle 4 to the inside of the furnace by 50 mm, and the pressure loss at the raceway portion. When ΔPb [MPa] exceeds the reference value (0.0245 MPa, the coke strength is increased (CSR: 2.0 → 64.4, DI: 184.
0 → 84.5) reduces the pressure loss in the raceway part to 0.
It was possible to reduce the pressure by 0054 to 0.0073 MPa. As a result, the ventilation resistance in the furnace was improved by 400 to 1000 [l / m], and the pulverized coal could be blown in stably.

【0021】[0021]

【表1】 [Table 1]

【0022】[0022]

【発明の効果】以上説明したごとく、この発明方法によ
れば、送風羽口部およびレースウェイ部の圧力損失を独
立に制御することにより高炉通気性を改善することがで
きるので、微粉炭を常に安定して吹き込むことができ、
高炉の微粉炭吹込操業に多大な効果を奏するものであ
る。
As described above, according to the method of the present invention, the blast furnace air permeability can be improved by independently controlling the pressure loss in the blast tuyere and the raceway, so that the pulverized coal is always used. I can blow in stably,
It has a great effect on the pulverized coal blowing operation of the blast furnace.

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

【図1】この発明方法を実施するための装置構成例を示
す概略図である。
FIG. 1 is a schematic diagram showing an example of the configuration of an apparatus for carrying out the method of the present invention.

【図2】この発明の実施例における羽口部の圧力損失△
Pa[MPa]、レースウェイ部の圧力損失△Pb[M
Pa]と炉内通気抵抗の関係を調べた結果を示す図であ
る。
FIG. 2 is a pressure loss Δ at a tuyere in an embodiment of the present invention.
Pa [MPa], pressure loss in raceway part ΔPb [M
It is a figure which shows the result of having investigated the relationship between Pa] and ventilation resistance in a furnace.

【符号の説明】[Explanation of symbols]

1 高炉 2 送風羽口 3 熱風吹込用ブローパイプ 4 微粉炭吹込ノズル 5 圧力測定用ランス 6 圧力分布測定装置 7 比較器 8 ノズル位置制御装置 9 コークス強度制御系 10 レースウェイ 1 Blast Furnace 2 Blow Tuyers 3 Blow Pipe for Hot Air Injection 4 Pulverized Coal Injection Nozzle 5 Lance for Pressure Measurement 6 Pressure Distribution Measurement Device 7 Comparator 8 Nozzle Position Control Device 9 Coke Strength Control System 10 Raceway

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 送風羽口に連設された熱風吹込用ブロー
パイプの壁を貫通して微粉炭吹込ノズルを該ブローパイ
プ内に突出させ、ブローパイプ内を流れる熱風と共に送
風羽口から炉内へ微粉炭を吹込む方法において、送風羽
口部およびレースウェイ部の圧力損失を測定し、送風羽
口部圧力損失が予め設定した基準値を超える場合には、
前記微粉炭吹込ノズルの先端位置を炉内側へ移動させて
当該羽口部の圧力損失を低下させ、レースウェイ部圧力
損失が予め設定した基準値を超える場合には、コークス
強度を高めて当該レースウェイ部圧力損失を低下させる
ことにより、高炉通気性を改善することを特徴とする高
炉への微粉炭吹込方法。
1. A pulverized coal blowing nozzle is projected into the blow pipe through a wall of a hot air blowing blow pipe connected to the blowing tuyere, and the hot air flowing in the blow pipe is blown into the furnace from the blowing tuyere. In the method of blowing pulverized coal into, the pressure loss of the blast tuyere and raceway portion is measured, and if the blast tuyere pressure loss exceeds a preset reference value,
When the tip position of the pulverized coal injection nozzle is moved to the inside of the furnace to reduce the pressure loss at the tuyere, and when the raceway pressure loss exceeds a preset reference value, the coke strength is increased to increase the race. A method for injecting pulverized coal into a blast furnace, which is characterized by improving the air permeability of the blast furnace by reducing the pressure loss in the way section.
JP32113295A 1995-11-15 1995-11-15 Method for injecting pulverized fine coal into blast furnace Pending JPH09143520A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32113295A JPH09143520A (en) 1995-11-15 1995-11-15 Method for injecting pulverized fine coal into blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32113295A JPH09143520A (en) 1995-11-15 1995-11-15 Method for injecting pulverized fine coal into blast furnace

Publications (1)

Publication Number Publication Date
JPH09143520A true JPH09143520A (en) 1997-06-03

Family

ID=18129167

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32113295A Pending JPH09143520A (en) 1995-11-15 1995-11-15 Method for injecting pulverized fine coal into blast furnace

Country Status (1)

Country Link
JP (1) JPH09143520A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006336086A (en) * 2005-06-03 2006-12-14 Jfe Steel Kk Method for blowing synthetic resin material into blast furnace

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006336086A (en) * 2005-06-03 2006-12-14 Jfe Steel Kk Method for blowing synthetic resin material into blast furnace

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