JP2627232B2 - Blast furnace operation method - Google Patents
Blast furnace operation methodInfo
- Publication number
- JP2627232B2 JP2627232B2 JP3255970A JP25597091A JP2627232B2 JP 2627232 B2 JP2627232 B2 JP 2627232B2 JP 3255970 A JP3255970 A JP 3255970A JP 25597091 A JP25597091 A JP 25597091A JP 2627232 B2 JP2627232 B2 JP 2627232B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- blast furnace
- core
- gas
- 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.)
- Expired - Lifetime
Links
Landscapes
- Manufacture Of Iron (AREA)
Description
【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 An object of the present invention is to ensure stable operation of a blast furnace by removing unburned char from the core of the furnace in the operation of blowing a large amount of pulverized coal from the tuyere of the blast furnace. It is assumed that.
【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 a blast furnace operation, a technique of injecting fuel from tuyere to replace coke charged from the furnace top has been developed (Japanese Patent Publication No. 40-23763) to reduce hot metal production cost and improve productivity. ing. Examples of the fuel include pulverized coal, petroleum, heavy oil, naphtha, and the like. Recently, pulverized coal has been 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。[0003] The pulverized coal blown from the tuyere burns in a region near the tuyere in the raceway, the carbon content becomes CO 2 , and H 2 O is also generated due to organic substances contained in part.
Further, when oxygen is depleted in a region outside the raceway, CO and H 2 are formed by reaction with coke, and this is supplied to the furnace as a reducing gas.
【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 pulverized coal is once completely oxidized to CO 2 , and CO is generated by a solution reaction. That is, an amount of oxygen exceeding the amount that finally forms CO gas is required in the middle of the reaction process, and the amount of air required for complete combustion of the pulverized coal, that is, the air ratio needs to be 1 or more. For this reason, if the pulverized coal blowing increases, the combustion efficiency of the pulverized coal decreases with a decrease in the air ratio. When the air ratio falls below about 1, the amount of unburned char generated in the raceway sharply increases. Blast furnace fuel ratio is 500
At the time of kg / t-pig, the blowing amount of pulverized coal at which the air ratio becomes 1 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 injected. However, if a large amount is blown beyond the above-mentioned limit, the unburned char generated accumulates on the furnace core and impairs air permeability and liquid permeability. This leads to a drop in tapping capacity, which does not result in profit.
An object of the present invention is to solve the above problems and eliminate the adverse effect of the accumulation of the unburned char on the furnace core, thereby enabling a large amount of pulverized coal to be blown.
【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、炉外より炉芯部に
挿入した管により、操業中に時々H2Oおよび/または
CO2を含むガスを炉芯部に吹き込み、炉芯部の末燃チ
ャーを除去することを特徴とするものである。もしくは
炉外より炉芯部に挿入した管により、操業中に時々H2
O、CO2の少なくとも一方とO2とを含むガスを炉芯
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、H2OおよびCO2との比率により前記ガスの吹
き込み前と同水準の熱収支のバランスに保つことを特徴
とするものである。またこれらの手段として、高炉炉腹
に設けた開口部からランスを炉芯部に挿入し、ガスを炉
芯部に吹き込むことも特徴とする。SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems. In a blast furnace operating method in which pulverized coal is blown together with hot air from a blowing tuyere of a blast furnace, a method for operating the blast furnace from outside the furnace to a furnace core portion is provided.
A gas containing H 2 O and / or CO 2 is sometimes blown into the furnace core by the inserted pipe during the operation to remove burnt char from the furnace core. Or
During operation, H 2 is sometimes used due to a tube inserted into the furnace core from outside the furnace.
A gas containing at least one of O and CO 2 and O 2 is blown into the furnace core to remove unburned char from the furnace core and to remove O 2.
2, blown of the gas by the ratio of H 2 O and CO 2
It is characterized by keeping the heat balance at the same level as before injection . In addition, as these means, a lance is inserted into the furnace core through an opening provided in the belly of the
It is also characterized by blowing into the core .
【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。According to the present invention, the pulverized coal ratio is greatly increased,
The operation is performed with a blowing amount of 00 kg / t-pig or more, and the unburned char deposited on the furnace core is sometimes removed during the operation, for example, by periodically removing the char.
【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
O 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 furnace core during operation by means of a pipe inserted from outside the blast furnace to react with unburned char and remove it. H 2 O (water vapor), C
O 2 or a gas containing them, 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 in the following chemical formula, it is preferable to use a heating means in combination.
【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 the heating means, plasma heating can be used in addition to the generally used means of 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 for the purpose of periodically removing unburned char under normal operating conditions, and for heating when the furnace core cools down and an inert portion is formed. is not. Therefore, the method of unnecessarily heating is not preferable because the heat balance in the furnace is lost.
【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, the unburned char is removed, but it is preferable to make the thermal condition that the balance is almost balanced. As a method of balancing the heat balance, there is a method of balancing by the composition of the gas itself, in addition to the above-described method of heating the gas. 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
O 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 a 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
In this case, the unburned char can be removed without affecting the heat. Actually, in consideration of the temperature of the gas to be fed, when the temperature is low, adjustment may be made such as increasing O 2 and increasing 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 means for blowing gas, a blowing lance is inserted from the tuyere portion, between the tuyere, on the tuyere, from the furnace belly, etc. to the furnace core. 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 uses a similar means to insert a water-cooled blowing lance 6 from an opening provided in advance during operation. A blow is performed.
【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。The insertion of the blowing lance 6 from the tuyere 2 involves insertion of the lance through the high-temperature portion of the raceway, so that the blowing time is restricted by the durability of the lance, but existing equipment can be used. Therefore, there is an advantage that it is not necessary to newly provide an opening. Also, a method of providing an opening between the tuyeres (not shown) is preferable because a high temperature portion of the raceway can be avoided. However, the space between the tuyere is the thickest part of the steel shell of the blast furnace due to the problem of strength, and there is a problem that it is quite difficult to provide an opening. For this reason, there is a method (not shown) of providing an opening at the upper part of the tuyere. However, this part has an annular pipe 7 and a blower branch pipe 8 for the tuyere ventilation, which may be an obstacle. It may be difficult to arrange the 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 to the furnace core 4. According to this method, the distance to the furnace core 4 is slightly increased, but the lance can reach the furnace core without passing through the high-temperature portion on the way, and work can be continued for a long time, which is preferable in terms of lance durability.
【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 having an internal volume of 3900 cubic meters, the effect of gas injection into the furnace core by a lance was tested by changing the amount of pulverized coal injected. As shown in FIG. 1, the gas was blown during the operation by providing an opening in the furnace belly 3 and inserting a lance 6 therein. The blowing time was 15 minutes at a time, and the places were sequentially changed at six places around the blast furnace. The number of gas injections for one location is 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の
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 reference condition, in which the pulverized coal is blown at a rate of 150 kg / t-pig, and is a normal operation in which gas is not blown into the furnace core. In Examples 1 to 4, the amount of pulverized coal injected was increased to 200 kg / t-pig, and the unburned char of the furnace core was removed by gas injection. In the first to third embodiments, the gas containing no O 2 is heated to a high temperature. In the fourth embodiment, the heating temperature of the gas is lowered by introducing air and utilizing the exothermic reaction of O 2 . In these examples, the replacement ratio of coke by pulverized coal does not change and the fuel ratio does not increase. Also, tapping capacity is on track. On the other hand, in Comparative Example 2 in which the pulverized coal injection amount was increased to 200 kg / t-pig but gas was not injected into the furnace core, a tendency of an increase in the fuel ratio and a decrease in the tapping amount were observed.
【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 to be blown is 250 kg /
Although it 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 Is also going well. Examples 5 and 6 correspond to Examples 1 to 3
Example 7 is an example using a gas containing no O 2, and Example 7 is an example using a gas containing O 2 , as in Example 4. On the other hand, in Comparative Example 3, although the pulverized coal injection rate was increased to 230 kg / t, unburned char was deposited because gas was not injected into the furnace core, and this impaired gas permeability and liquid permeability of the furnace core. As a result, an increase in fuel ratio and a decrease in tapping rate are observed.
【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。According to the present invention, in the blast furnace operation, unburned char deposited on the furnace core when the amount of pulverized coal blown from the tuyere is increased can be removed during the operation by the method of the present invention. This makes it possible to increase the amount of pulverized coal injected without deteriorating the furnace condition, and reduce the amount of coke used to reduce costs.
【図1】本発明の炉芯へのガス吹き込み方法を説明する
図FIG. 1 is a diagram for explaining a method of 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 (56)参考文献 特開 平4−268005(JP,A) 特開 平3−291312(JP,A) 特開 平3−56611(JP,A) 特開 昭62−270709(JP,A) 特開 昭59−107009(JP,A) ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Hisao Kamiyama 5-3 Tokai-cho, Tokai-shi, Aichi Prefecture Nippon Steel Corporation Nagoya Works (56) References JP-A-4-268005 (JP, A) JP-A-3-291312 (JP, A) JP-A-3-56611 (JP, A) JP-A-62-270709 (JP, A) JP-A-59-107009 (JP, A)
Claims (3)
を吹き込む高炉操業法において、炉外より炉芯部に挿入
した管により、操業中に時々H2Oおよび/またはCO
2を含むガスを炉芯部に吹き込み、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 blowing tuyere of a blast furnace, the blast furnace is inserted into the core from outside the furnace.
By the tube, sometimes during operation H 2 O and / or CO
2. A blast furnace operating method comprising blowing a gas containing 2 into a furnace core to remove unburned char in the furnace core.
を吹き込む高炉操業法において、炉外より炉芯部に挿入
した管により、操業中に時々H2O、CO2の少なくと
も一方とO2とを含むガスを炉芯部に吹き込み、炉芯部
の未燃チャーを除去すると共にO2と、H2OおよびC
O2との比率により前記ガスの吹き込み前と同水準の熱
収支のバランスに保つことを特徴とする高炉操業法。2. In a blast furnace operating method in which pulverized coal is blown together with hot air from a blowing tuyere of a blast furnace, the blast furnace is inserted into the core from outside the furnace.
During the operation, a gas containing at least one of H 2 O and CO 2 and O 2 is sometimes blown into the furnace core during the operation to remove unburned char in the furnace core and to remove O 2 , H 2 O and C
The same level of heat as before the gas injection due to the ratio with O 2
A blast furnace operating method characterized by maintaining a good balance .
芯部に挿入し、ガスを炉芯部に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. A lance is connected to a blast furnace through an opening provided on the belly of the blast furnace.
Insert the core portion, blast furnace operation method according to claim 1 or claim 2, wherein the blowing gas into the furnace core section.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3255970A JP2627232B2 (en) | 1991-09-09 | 1991-09-09 | Blast furnace operation method |
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)
Publication Number | Publication Date |
---|---|
JPH0565516A JPH0565516A (en) | 1993-03-19 |
JP2627232B2 true JP2627232B2 (en) | 1997-07-02 |
Family
ID=17286106
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3255970A Expired - Lifetime JP2627232B2 (en) | 1991-09-09 | 1991-09-09 | Blast furnace operation method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2627232B2 (en) |
Family Cites Families (3)
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 |
-
1991
- 1991-09-09 JP JP3255970A patent/JP2627232B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH0565516A (en) | 1993-03-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3771728B2 (en) | Blowing pulverized coal and reducing gas into the blast furnace | |
JPH11199907A (en) | Injection system for high temperature oxygen into blast furnace | |
JP3176680B2 (en) | Blast furnace operation method | |
JP3796021B2 (en) | Method of blowing pulverized coal from blast furnace tuyere and blowing lance | |
JP4650226B2 (en) | Melting reduction method | |
JP2627232B2 (en) | Blast furnace operation method | |
US5437706A (en) | Method for operating a blast furnace | |
JP4392100B2 (en) | Method of injecting reducing gas into the blast furnace | |
JPS6038443B2 (en) | Iron ore reduction processing method | |
JP3964963B2 (en) | Pulverized coal injection method in blast furnace | |
JP2006312756A (en) | Injection lance for gaseous reducing material, blast furnace and blast furnace operation method | |
JPH06128614A (en) | Operation of blast furnace | |
JP5526614B2 (en) | Melting reduction method | |
JPH08260010A (en) | Operation for blowing large quanty of pulverized coal in blast furnace | |
JP4325401B2 (en) | Manufacturing method of low silicon hot metal | |
JPH0565515A (en) | Method for operating blast furnace | |
JPH11241108A (en) | Method for injecting pulverized fine coal into blast furnace | |
JP2933809B2 (en) | Operating method of moving bed type scrap melting furnace | |
JP2004091921A (en) | Method for blowing solid fuel into blast furnace and blown lance | |
JPH062020A (en) | Method for blowing powdery fuel into blast furnace | |
JPH06108125A (en) | Operation of blast furnace | |
JP2560667B2 (en) | Hot metal production method | |
JPS63176407A (en) | Production of molten iron | |
JP4325128B2 (en) | Low silicon operation method in blast furnace mass injection into blast furnace. | |
JPS6357704A (en) | Operation of blast furnace |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 19970107 |