JPH0565516A - Method for operating blast furnace - Google Patents

Method for operating blast furnace

Info

Publication number
JPH0565516A
JPH0565516A JP25597091A JP25597091A JPH0565516A JP H0565516 A JPH0565516 A JP H0565516A JP 25597091 A JP25597091 A JP 25597091A JP 25597091 A JP25597091 A JP 25597091A JP H0565516 A JPH0565516 A JP H0565516A
Authority
JP
Japan
Prior art keywords
furnace
blast furnace
pulverized coal
core
blown
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.)
Granted
Application number
JP25597091A
Other languages
Japanese (ja)
Other versions
JP2627232B2 (en
Inventor
Morimasa Ichida
守政 一田
Kazuya Kunitomo
和也 国友
Kenji Yamane
健司 山根
Hisaaki Kamiyama
久朗 神山
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
Nippon 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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP3255970A priority Critical patent/JP2627232B2/en
Publication of JPH0565516A publication Critical patent/JPH0565516A/en
Application granted granted Critical
Publication of JP2627232B2 publication Critical patent/JP2627232B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

(57)【要約】 【目的】 本発明は、高炉炉芯部の未燃チャーを除去す
る方法を提供する。 【構成】 高炉の微粉炭多量吹込み操業において、操業
中にH 2O、CO 2またはこれらを含むガスを炉外より
挿入した管により炉芯部に吹込み、炉芯部の未燃チャー
を除去して微粉炭吹込み量の上限値を拡大する。
(57) [Summary] [Object] The present invention provides a method for removing unburned char in a blast furnace core. [Composition] In a blast furnace with a large amount of pulverized coal blowing operation, H 2 O, CO 2 or a gas containing these is blown into the furnace core through a pipe inserted from outside the furnace during operation to remove unburned char in the furnace core. Remove to increase the upper limit of pulverized coal injection.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は高炉の羽口から大量の微
粉炭を吹き込む操業において、未燃チャーが炉芯部に堆
積した場合にその除去を行ない安定した高炉操業を確保
することを目的とするものである。
BACKGROUND OF THE INVENTION The present invention aims to secure stable blast furnace operation by blowing out a large amount of pulverized coal from tuyere of a blast furnace when unburned char is deposited on the core of the furnace. It is what

【0002】[0002]

【従来の技術】高炉操業においては炉頂から装入するコ
ークスを代替するため羽口より燃料を吹き込む技術が開
発され(特公昭40−23763号)、溶銑製造コスト
の低減、生産性向上を図っている。前記燃料としては微
粉炭、石油、重油、ナフサ等があるが、最近では価格の
点から微粉炭吹き込みが主に採用されている。
2. Description of the Related Art In blast furnace operation, a technique of blowing fuel from tuyere to replace coke charged from the top of the furnace was developed (Japanese Patent Publication No. 40-23763) to reduce hot metal production costs and improve productivity. ing. Pulverized coal, petroleum, heavy oil, naphtha and the like are used as the fuel, but recently, pulverized coal injection is mainly used in terms of price.

【0003】羽口から吹き込まれた微粉炭はレースウェ
イ内の羽口に近い領域で燃焼し、炭素分はCO 2にな
り、一部含まれている有機物によりH2Oも発生する。
さらにレースウェイ内のその外側の領域で酸素が無くな
るとコークスとの反応によりCO、H 2を形成し、これ
が還元ガスとして炉内に供給される。
The pulverized coal blown from the tuyere burns in the area near the tuyere in the raceway, the carbon content becomes CO 2 , and H 2 O is also generated due to the organic matter partially contained.
Further, when oxygen disappears in the area outside the raceway, CO and H 2 are formed by reaction with coke, and these are supplied as reducing gas into the furnace.

【0004】すなわち微粉炭中の炭素分は一旦完全酸化
してCO 2になり、ソリューション反応によりCOを生
成する。つまり最終的にCOガスを形成する以上の酸素
量が途中の反応過程で要求され、微粉炭が完全燃焼する
に必要な空気量、すなわち空気比1以上にする必要があ
る。このため微粉炭の吹き込みが増大すると空気比の低
下に伴って微粉炭の燃焼効率が低下する。そして空気比
が1近傍より下がるとレースウェイ内で未燃チャーの発
生量が急激に増加することになる。高炉燃料比が500
kg/t−pigのとき空気比が1になる微粉炭の吹き
込み量は170kg/t−pig程度とされ、これが吹
き込み量の限界となる。
That is, the carbon content in the pulverized coal is once completely oxidized to CO 2 and CO is produced by the solution reaction. That is, the amount of oxygen required to finally form CO gas is required in the course of the reaction, and the amount of air required for complete combustion of the pulverized coal, that is, the air ratio needs to be 1 or more. Therefore, if the blowing of the pulverized coal increases, the combustion efficiency of the pulverized coal decreases as the air ratio decreases. Then, when the air ratio falls below the vicinity of 1, the amount of unburned char generated in the raceway increases rapidly. Blast furnace fuel ratio is 500
The blowing amount of the pulverized coal that gives an air ratio of 1 at kg / t-pig is about 170 kg / t-pig, which is the limit of the blowing amount.

【0005】[0005]

【発明が解決しようとする課題】コークスを微粉炭でで
きるだけ置換するのがコスト的に有利であるので、微粉
炭吹き込み量を増大する試みがなされている。しかし前
記の限界を超えて大量に吹き込むと発生した未燃チャー
が炉芯部に堆積して通気性、通液性を害するようにな
る。このため出銑量の低下を招き結局利益にならない。
本発明は上記問題点を解決して上記未燃チャーの炉芯部
への堆積の悪影響を除き、微粉炭の大量吹き込みを可能
にしようとするものである。
Since it is cost effective to replace coke with pulverized coal as much as possible, attempts have been made to increase the amount of pulverized coal blown. However, if a large amount of the charcoal is blown in beyond the above-mentioned limit, the unburned char generated will be deposited on the core of the furnace, impairing air permeability and liquid permeability. For this reason, the amount of tapped iron is reduced, which is not profitable.
The present invention is intended to solve the above problems and eliminate the adverse effect of the accumulation of the above-mentioned unburned char on the core portion of the furnace, thereby making it possible to blow a large amount of pulverized coal.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題を解決
するものであって、高炉の送風羽口より熱風とともに微
粉炭を吹き込む高炉操業法において、操業中において時
々H 2O、CO 2またはこれらを含むガスを炉外より挿
入した管により炉芯部に吹き込み、炉芯部の未燃チャー
を除去することを特徴とするものである。もしくは操業
中において時々H 2O、CO 2の少なくとも一方とO 2
とを含むガスを炉外より挿入した管により炉芯部に吹き
込み、炉芯部の未燃チャーを除去すると共にO 2とH 2
OおよびCO 2との比率により熱収支のバランスを適正
に保つことを特徴とするものである。またこれらの手段
として、高炉炉腹に開口部を設けランスを挿入し、ガス
を吹き込むことも特徴とするものである。
Means for Solving the Problems The present invention is intended to solve the above problems, and in a blast furnace operating method in which pulverized coal is blown together with hot air from the blast tuyere of a blast furnace, H 2 O, CO 2 or A gas containing these is blown into the furnace core through a tube inserted from outside the furnace to remove unburned char in the furnace core. Alternatively, during operation, at least one of H 2 O and CO 2 and O 2
A gas containing and is blown into the furnace core through a tube inserted from outside the furnace to remove unburned char in the furnace core and to remove O 2 and H 2
The feature is that the balance of the heat balance is properly maintained by the ratio of O and CO 2 . Further, as a means for these, an opening is provided in the belly of the blast furnace, a lance is inserted, and gas is blown in.

【0007】[0007]

【作用】本発明は微粉炭比を大幅に増やし、たとえば2
00kg/t−pig以上の吹き込み量で操業を行なう
が、これにより炉芯部に堆積した未燃チャーは操業中に
おいて時々、たとえば定期的に除去することで対処す
る。
The present invention significantly increases the pulverized coal ratio, for example, 2
The operation is performed with a blowing amount of 00 kg / t-pig or more, whereby the unburned char accumulated on the core of the furnace is removed from time to time, for example, periodically during the operation.

【0008】この手段として高炉炉外より挿入した管に
より操業中に炉芯部にガスを吹き込んで未燃チャーと反
応させて除去する。ガスとしてはH 2O(水蒸気)、C
2またはこれらを含むガス、たとえば熱風炉排ガス等
も用いられる。H 2O、CO2は下記の化学式のように
吸熱反応によって炭素を除去することになるので、加熱
手段を併用することが好ましい。
As a means for this, gas is blown into the core of the furnace during operation by a pipe inserted from the outside of the blast furnace to react with the unburned char and remove it. As gas, H 2 O (steam), C
O 2 or a gas containing these, for example, hot-blast stove exhaust gas or the like is also used. Since H 2 O and CO 2 remove carbon by an endothermic reaction as shown by the following chemical formula, it is preferable to use heating means together.

【0009】 H 2O+C=CO+H 2−28.4(kcal/mo
l) CO 2+C=2CO−38.2(kcal/mol)
H 2 O + C = CO + H 2 −28.4 (kcal / mo
l) CO 2 + C = 2CO-38.2 (kcal / mol)

【0010】加熱手段としては一般に用いられる燃焼熱
によるものの他にプラズマ加熱も用い得る。プラズマ加
熱の場合プラズマトーチ自体を後に述べるガス吹き込み
ランスと兼ねさせることもできる。
As heating means, plasma heating may be used in addition to the generally used combustion heat. In the case of plasma heating, the plasma torch itself can also serve as a gas blowing lance described later.

【0011】本発明が適用されるのは正常な操業状態に
おいて未燃チャーの除去を定期的に行なうためのもので
あり、炉芯が冷え込んで不活性部分ができたときに加熱
するためのものではない。したがっていたずらに加熱す
る方法は炉内の熱バランスを崩すことになり好ましくな
い。
The present invention is applied to periodically remove unburned char in a normal operating condition, and to heat when the core cools and an inactive portion is formed. is not. Therefore, the method of unnecessarily heating undesirably destroys the heat balance in the furnace.

【0012】したがって未燃チャーは除去するが、熱的
にはほぼ収支がバランスした条件にするのがよい。熱収
支をバランスさせる方法としては上記のガスを加熱する
方法の他にガス自体の組成によりバランスをとる方法も
とれる。すなわちO 2は下式のように炭素と反応して発
熱する。
Therefore, although the unburned char is removed, it is preferable that the thermal condition is such that the balance is balanced. As a method for balancing the heat balance, in addition to the method for heating the above-mentioned gas, a method for balancing by the composition of the gas itself can be used. That is, O 2 reacts with carbon to generate heat as shown in the following formula.

【0013】 O 2+2C=2CO+58.8(kcal/mol)O 2 + 2C = 2CO + 58.8 (kcal / mol)

【0014】このためH 2OまたはCO 2を含むガスに
2や空気を添加して熱収支のバランスをとることがで
きる。たとえばH 2OとO 2とを含むガスを使用する場
合、O 21モル当りの発熱量はH 2O1モル当りの吸熱
量のほぼ2倍であるから、H2OとO 2の比率を2対1
とすれば熱的には影響を与えずに未燃チャーを除去でき
ることになる。実際には送給するガスの温度も勘案して
温度が低いときにはO2を多くして発熱を大にするなど
調節をすればよい。
Therefore, it is possible to balance the heat balance by adding O 2 or air to the gas containing H 2 O or CO 2 . For example when using a gas containing between H 2 O and O 2, because the amount of heat generated O 2 1 mole per is approximately twice the amount of heat absorption per H 2 O1 moles, the ratio of between H 2 O and O 2 2 to 1
If so, unburned char can be removed without thermally affecting. Actually, when the temperature of the gas to be fed is taken into consideration, when the temperature is low, the amount of O 2 may be increased to increase heat generation.

【0015】ガスの吹き込み手段としては羽口部、羽口
間、羽口上、炉腹等から吹き込みランスを炉芯部まで挿
入して行なう。図1はこの状況を示す高炉1の一部分の
断面図である。近年ゾンデを羽口等から挿入する技術が
発達しつつあるが、図1に示すように本発明はこれと同
様の手段で操業中に予め設けた開口部から水冷の吹き込
みランス6を挿入して吹き込みを行なうものである。
As a gas blowing means, a blowing lance is inserted from the tuyere, between the tuyere, on the tuyere, and the furnace belly to the core of the furnace. FIG. 1 is a sectional view of a part of the blast furnace 1 showing this situation. In recent years, a technique for inserting a sonde from a tuyere or the like has been developed, but as shown in FIG. 1, the present invention inserts a water-cooling blow-in lance 6 from an opening provided in advance by the same means as this. It is to blow.

【0016】このうち羽口2からの吹き込みランス6挿
入はレースウェイの高温部を通ってランスを挿入するこ
とになるのでランスの耐久性から吹き込み時間の制約を
受けるが、既存の設備が利用できて新たに開口部を設け
る必要がない利点がある。また羽口間に開口部を設ける
方法(図示せず)はレースウェイの高温部を避けること
ができるので好ましい。しかし羽口間は強度上の問題か
ら高炉の鉄皮の厚さが最も厚い部分であり、開口部を設
けることはかなり困難という問題がある。またこのため
羽口の上部に開口部を設ける方法(図示せず)もあるが
この部分は羽口送風のための環状管7や送風支管8があ
り、邪魔になることがあるので吹き込みランスの設備の
取り合いが難しい場合がある。
Of these, when the blowing lance 6 is inserted from the tuyere 2, the lance is inserted through the high temperature portion of the raceway, so the blowing time is restricted by the durability of the lance, but existing equipment can be used. There is an advantage that there is no need to newly provide an opening. Further, a method (not shown) in which openings are provided between the tuyere is preferable because the high temperature portion of the raceway can be avoided. However, the space between the tuyere is the thickest part of the iron shell of the blast furnace due to strength problems, and there is the problem that it is quite difficult to provide openings. For this reason, there is also a method (not shown) of providing an opening on the upper part of the tuyere, but this part has an annular pipe 7 and a blower branch pipe 8 for blowing the tuyere, which may be an obstacle, and thus the blowing lance There is a case where it is difficult to have equipment.

【0017】これらの点から炉腹3の部分に開口部を設
けるのが最も好ましい。図1に示すように炉腹3の部分
から斜め下方に炉芯4に達するまで吹き込みランス6を
挿入する。この方法によれば、炉芯4までの距離はやや
長くなるが、途中高温部を通らずランスを炉芯に到達さ
せることができ、ランスの耐久上好ましく長時間続けて
作業ができる。
From these points, it is most preferable to provide an opening in the furnace belly 3. As shown in FIG. 1, the blowing lance 6 is inserted obliquely downward from the furnace belly 3 until reaching the furnace core 4. According to this method, although the distance to the furnace core 4 is slightly long, the lance can reach the furnace core without passing through the high temperature part in the middle, and the work can be continued for a long time preferably in terms of durability of the lance.

【0018】[0018]

【実施例】以下表1により実施例を説明する。EXAMPLES Examples will be described below with reference to Table 1.

【表1】 [Table 1]

【0019】内容積3900立方メートルの高炉におい
て微粉炭吹き込み量を変化させて、ランスによる炉芯部
へのガス吹き込みの効果を試験した。ガス吹き込みは図
1に示したように炉腹3に開口部を設けてランス6を挿
入して操業中行なった。吹き込みの時間は1回15分間
で高炉の周囲6箇所について順次場所を変えて行なっ
た。1箇所についてのガス吹き込み回数は1日1回であ
る。
In a blast furnace with an internal volume of 3900 cubic meters, the amount of pulverized coal blown was changed to test the effect of blowing gas into the furnace core by a lance. Gas blowing was performed during operation by providing an opening in the furnace belly 3 and inserting the lance 6 as shown in FIG. The blowing time was once for 15 minutes, and the locations were sequentially changed at six locations around the blast furnace. The gas is blown into one place once a day.

【0020】比較例1は基準となる条件であって、微粉
炭吹き込み量は150kg/t−pigで炉芯部へのガ
ス吹き込みを行なわない通常の操業である。実施例1か
ら4は微粉炭吹き込み量を200kg/t−pigに増
やし、ガス吹き込みにより炉芯の未燃チャーを除去した
ものである。実施例1から3はO 2を含まないガスを高
温に加熱しているが、実施例4では空気を入れてO 2
発熱反応を利用することでガスの加熱温度を下げてい
る。これら実施例では微粉炭によるコークスの置換比は
変わらず燃料比の増加はない。また出銑量も順調であ
る。一方微粉炭吹き込み量を200kg/t−pigに
増やしたが、炉芯部へのガス吹き込みを行なわなかった
比較例2においては燃料比の増加の傾向、出銑量の低下
の傾向がみられる。
Comparative Example 1 is a standard condition, in which the amount of pulverized coal blown is 150 kg / t-pig and normal operation is performed without blowing gas into the furnace core. In Examples 1 to 4, the amount of pulverized coal blown was increased to 200 kg / t-pig and the unburned char in the furnace core was removed by blowing gas. In Examples 1 to 3, the gas containing no O 2 was heated to a high temperature, but in Example 4, the heating temperature of the gas was lowered by introducing air and utilizing the exothermic reaction of O 2 . In these examples, the coke substitution ratio by the pulverized coal does not change and the fuel ratio does not increase. In addition, the amount of tapped metal is good. On the other hand, in the comparative example 2 in which the amount of pulverized coal blown was increased to 200 kg / t-pig, but gas was not blown into the furnace core, the fuel ratio tended to increase and the amount of tapped metal tended to decrease.

【0021】さらに微粉炭の吹き込み量を250kg/
t−pigに増やしたが、実施例5から7でみるように
炉芯部にガス吹き込みを行なった場合には実施例1から
4の場合と同様に燃料比の増加はほとんどなく、出銑量
も順調である。なお実施例5および6は実施例1から3
と同様にO 2を含まないガスを用いた例、実施例7は実
施例4と同様にO 2を含むガスを用いた例である。一方
比較例3では微粉炭吹き込み量を230kg/tまで増
やしたが、炉芯部へのガス吹き込みを行なわないため未
燃チャーの堆積があり、このため炉芯の通気性、通液性
が害されて燃料比の増加、出銑量の低下がみられる。
Further, the amount of pulverized coal blown is 250 kg /
Although the amount was increased to t-pig, when gas was blown into the furnace core as seen in Examples 5 to 7, there was almost no increase in the fuel ratio as in Examples 1 to 4, and the amount of tapped metal was increased. Is also going well. Note that Examples 5 and 6 are Examples 1 to 3.
An example using a gas containing no O 2 as in the above, and Example 7 is an example using a gas containing O 2 as in Example 4. On the other hand, in Comparative Example 3, the amount of pulverized coal blown was increased to 230 kg / t, but unburned char was accumulated because gas was not blown into the core, which impaired air permeability and liquid permeability of the core. As a result, the fuel ratio increases and the amount of tapping metal decreases.

【0022】[0022]

【発明の効果】高炉操業において、羽口からの微粉炭吹
き込み量を増大した場合に炉芯部に堆積する未燃チャー
を本発明の方法によって操業中に除去することができ
る。これにより炉況を悪化させることなしに微粉炭吹き
込み量の増加をすることができ、コークス使用量を低減
してコスト低下をすることができる。
In the operation of the blast furnace, unburned char accumulated on the core of the furnace when the amount of pulverized coal blown from the tuyere is increased can be removed by the method of the present invention during the operation. As a result, the amount of pulverized coal injected can be increased without deteriorating the furnace condition, the amount of coke used can be reduced, and the cost can be reduced.

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

【図1】本発明の炉芯へのガス吹き込み方法を説明する
FIG. 1 is a diagram illustrating a method for blowing gas into a furnace core according to the present invention.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 神山 久朗 愛知県東海市東海町5−3 新日本製鐵株 式会社名古屋製鐵所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Hisaro Kamiyama 5-3 Tokai-cho, Tokai-shi, Aichi Nippon Steel Co., Ltd. Nagoya Steel Works

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 高炉の送風羽口より熱風とともに微粉炭
を吹き込む高炉操業法において、操業中において時々H
2O、CO 2またはこれらを含むガスを炉外より挿入し
た管により炉芯部に吹き込み、炉芯部の未燃チャーを除
去することを特徴とする高炉操業法。
1. In a blast furnace operating method in which pulverized coal is blown together with hot air from a blast tuyere of a blast furnace, H
A blast furnace operating method characterized by removing unburned char in the furnace core by blowing 2 O, CO 2 or a gas containing these from the outside of the furnace through a tube inserted into the furnace core.
【請求項2】 高炉の送風羽口より熱風とともに微粉炭
を吹き込む高炉操業法において、操業中において時々H
2O、CO 2の少なくとも一方とO 2とを含むガスを炉
外より挿入した管により炉芯部に吹き込み、炉芯部の未
燃チャーを除去すると共にO 2とH 2OおよびCO 2
の比率により熱収支のバランスを適正に保つことを特徴
とする高炉操業法。
2. In a blast furnace operation method in which pulverized coal is blown together with hot air from a blast furnace tuyere, sometimes H
Gas containing at least one of 2 O and CO 2 and O 2 is blown into the furnace core through a tube inserted from outside the furnace to remove unburned char in the furnace core and to remove O 2 and H 2 O and CO 2 . The blast furnace operating method is characterized by maintaining a proper balance of heat balance depending on the ratio.
【請求項3】 高炉炉腹に開口部を設けランスを挿入
し、ガスを吹き込むことを特徴とする請求項1または請
求項2記載の高炉操業法。
3. The blast furnace operating method according to claim 1, wherein an opening is provided in the blast furnace belly, a lance is inserted, and gas is blown into the blast furnace.
JP3255970A 1991-09-09 1991-09-09 Blast furnace operation method Expired - Lifetime JP2627232B2 (en)

Priority Applications (1)

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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3255970A JP2627232B2 (en) 1991-09-09 1991-09-09 Blast furnace operation method

Publications (2)

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JPH0565516A true JPH0565516A (en) 1993-03-19
JP2627232B2 JP2627232B2 (en) 1997-07-02

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2025164229A1 (en) * 2024-01-31 2025-08-07

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59107009A (en) * 1982-12-11 1984-06-21 Nisshin Steel Co Ltd Method for operating blast furnace at high productivity coefficient in all-coke operation
JPS62270709A (en) * 1986-05-19 1987-11-25 Kobe Steel Ltd Method for blowing powdery fuel into blast furnace
JPH0356611A (en) * 1989-07-26 1991-03-12 Sumitomo Metal Ind Ltd Method for charging carbonaceous material to blast furnace

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59107009A (en) * 1982-12-11 1984-06-21 Nisshin Steel Co Ltd Method for operating blast furnace at high productivity coefficient in all-coke operation
JPS62270709A (en) * 1986-05-19 1987-11-25 Kobe Steel Ltd Method for blowing powdery fuel into blast furnace
JPH0356611A (en) * 1989-07-26 1991-03-12 Sumitomo Metal Ind Ltd Method for charging carbonaceous material to blast furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2025164229A1 (en) * 2024-01-31 2025-08-07
WO2025164229A1 (en) * 2024-01-31 2025-08-07 日本製鉄株式会社 Method for blowing reducing gas into blast furnace, and blast furnace

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