JPS5871310A - Blasting method for blast furnace - Google Patents

Blasting method for blast furnace

Info

Publication number
JPS5871310A
JPS5871310A JP16829881A JP16829881A JPS5871310A JP S5871310 A JPS5871310 A JP S5871310A JP 16829881 A JP16829881 A JP 16829881A JP 16829881 A JP16829881 A JP 16829881A JP S5871310 A JPS5871310 A JP S5871310A
Authority
JP
Japan
Prior art keywords
furnace
pressure
blasting
blast furnace
rate
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
JP16829881A
Other languages
Japanese (ja)
Other versions
JPH0120203B2 (en
Inventor
Koichi Kurita
栗田 興一
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 JP16829881A priority Critical patent/JPS5871310A/en
Publication of JPS5871310A publication Critical patent/JPS5871310A/en
Publication of JPH0120203B2 publication Critical patent/JPH0120203B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/006Automatically controlling the process

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Iron (AREA)
  • Blast Furnaces (AREA)

Abstract

PURPOSE:To stabilize the operations of a blast furnace and to prolong the life of the furnace through prevention of hanging, slipping or blowing-by by regulating the rate of blasting in accordance with the limit rate of blasting determined from the pressure drop values in the plural positions in the blast furnace where heights differ. CONSTITUTION:The static pressures of the wall of a blast furnace 1 in the various parts thereof are measured by the pressure gages 2a, 2b, 2c, 2d and 2e mounted in the upper, middle and lower parts of the shaft, berry part and bosh part of said blast furnace; at the same time the furnace top pressure is measured with a pressure gage 2f mounted at the furnace top. From these measured values, the pressure drops DELTAP' from the respective measuring positions up to the furnace top are determined with a measuring device 3 for pressure drops; further the limit rate (v) of blasting is calculated with a calculator 4 for the rate of blasting from the measured value (v') of the rate of blasting of hot wind blasted through tuyeres 1a into the furnace 1, the load of the charging materials determined from operating conditons, the set value of the limit pressure drop indices in accordance with actual data, etc., and in accordance with such calculated value, the rate of blasting of hot wind is regulated by a hot wind regulator 5.

Description

【発明の詳細な説明】 本発明は高炉操業を行う際に発生する棚吊り、スリップ
、吹抜は等を防止する高炉送風方法を提案した屯のであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention proposes a blast furnace ventilation method that prevents shelving, slipping, blow-out, etc. that occur during blast furnace operation.

高炉操業において炉内の圧力損失が増し、これが装入物
荷重、即ち装入物の降下す4力と釣り合つた状趨となる
と、所浦棚吊りが発生し、炉内に大きな空間ができて装
入物の供給ができないので人為的に棚落しを行う必要が
ある。またそれが軽度の場合は棚落しを行うまでもなく
自然に降下し、所!FWスリップが発生する。更に炉内
の圧力損失と装入物荷重との釣合いが著しく崩n、ると
装入物が炉頂に吹き上げ、所謂吹抜けが発生する。
During blast furnace operation, when the pressure loss inside the furnace increases and this becomes balanced with the charge load, that is, the force of the falling charge, Tokoroura shelf suspension occurs, creating a large space inside the furnace. Since it is not possible to supply the charge material by using the method, it is necessary to artificially shelve the material. Also, if it is mild, there is no need to drop the shelf and it will fall naturally. FW slip occurs. Furthermore, if the balance between the pressure loss in the furnace and the charge load is significantly disrupted, the charge will blow up to the top of the furnace, causing so-called blow-through.

これらの現象が発生すると溶銑温度、炉内状態の異常を
引起すこととなり、特に吹抜けが発生すると炉頂の温度
が極端に上昇し、設備的にも大きな事故を誘発しかねな
い。従って高炉操業に際してはこれらの現象が発生しな
いように適正な操業を行うことは非常に重要な課題であ
る。
When these phenomena occur, it causes abnormalities in the temperature of the hot metal and the conditions inside the furnace.In particular, when blow-through occurs, the temperature at the top of the furnace rises extremely, which can lead to a major equipment-related accident. Therefore, when operating a blast furnace, it is a very important issue to perform proper operation to prevent these phenomena from occurring.

従来これらの現象を防止する方法として、送風圧と炉m
圧との差を求め、これと装入物荷重との比、即ち吹抜は
指数が一定値を越えないように送風圧を設定することが
行われているが、棚吊り、スリップ、吹抜は等の桿象は
炉内温度分布、炉内装入物の高温性状等K111合的に
起因することが知られており、上述の吹抜は指数ではこ
れらを十分把握することができないために棚吊り、スリ
ップ、吹抜は等の発生を完全に防止することができない
O本発明は斯かる事情に鑑みてなさ11だものであり、
炉内に棚吊り、スリップ、吹抜は等が発生するのを防止
する高炉送風方法を提案し、高炉操菓の安定化及び高炉
の長寿命化を図ることを目的とする。
Conventionally, as a method to prevent these phenomena, blowing pressure and furnace m
The difference between the pressure and the charge load is determined, and the blowing pressure is set so that the index does not exceed a certain value, that is, the ratio of this to the charge load. It is known that this phenomenon is caused by K111 combinations such as the temperature distribution inside the furnace and the high temperature properties of the contents inside the furnace. It is not possible to completely prevent the occurrence of such problems as in the case of stairwells, etc. The present invention was developed in view of such circumstances.
The purpose of this paper is to propose a blast furnace ventilation method that prevents the occurrence of shelf hanging, slipping, blow-out, etc. in the furnace, and to stabilize the blast furnace operation and extend the life of the blast furnace.

本発明に係る高炉送風方法に、高炉炉頂圧を測定すると
共に、炉壁における高さが異なる複数の位@にて炉壁静
圧を測定し、これらの測定値に工9各炉壁靜圧測定位置
から炉頂までの圧力損失を求める一方、操業条件により
炉頂から各炉壁靜圧測定位wrtでの装入物荷重との比
を求め、この比が、棚吊り、スリップ又は吹抜けを発生
させないように予め規定しである条件を満たすように送
風条件を設定することを特徴とするO 先ず本発明の基本的な考えについて収明するO第1図は
炉壁における高さが異なる複数の位@VCて測定された
炉壁静圧と炉頂圧との差、即ち各炉壁静圧測定位置から
炉頂までの圧力損失と炉高さとの関係を示し友グラフで
あるか、その圧力損失は炉高さの低下と共に比例的に増
m しており、送風羽口近くになると急激に増加してい
ることが分かる。一方第2図は炉頂から各炉壁静圧測定
位置までの単位面噴当りの装入物荷重と炉高さとの関係
を示したグラフであるが、炉妊近くになるまでは、装入
物荷重が炉高さの低下と共に略比例的に増加しているこ
とが分かる。この圧力損失と装入物荷重との比、即ち圧
損指数は、荷下り現象を把握する上で有効な指標となる
。理論的tlc、はこの圧損指数が1以上になると棚吊
り、スリップ又は吹抜けを起こすことになるが、実炉に
おいては装入物性状のバラツキ、壁面摩擦力、高炉半径
方向の装入物荷重分布、ガスの偏流等の影響により、棚
吊り、スリップ又は吹抜けが発生する圧損指数の限界値
(限界圧損指数という)は1以下の値をとる。何えは第
3図は高炉の操業実績から求めたベリーsvcおける圧
損指数とスリップ(棚吊りも含む)の発生回数との関係
を示したグラフであるが、スリップの発生を防止するた
めvcF′i、この圧損指数を0.3より小さく保持す
ればよいことが分かる。
In the blast furnace air blowing method according to the present invention, the blast furnace top pressure is measured, and the furnace wall static pressure is measured at a plurality of positions at different heights on the furnace wall. While determining the pressure loss from the pressure measurement position to the furnace top, the ratio to the burden load from the furnace top to each furnace wall static pressure measurement position wrt is determined depending on the operating conditions. First, the basic idea of the present invention will be explained. Figure 1 shows the different heights on the furnace wall. Is it a friend graph that shows the difference between the furnace wall static pressure and the furnace top pressure measured at multiple positions @VC, that is, the relationship between the pressure loss from each furnace wall static pressure measurement position to the furnace top and the furnace height? It can be seen that the pressure loss increases proportionally as the furnace height decreases, and increases rapidly near the blast tuyeres. On the other hand, Figure 2 is a graph showing the relationship between the charge load per unit surface injection and the furnace height from the furnace top to each furnace wall static pressure measurement position. It can be seen that the material load increases approximately proportionally as the furnace height decreases. The ratio of this pressure loss to the charge load, that is, the pressure loss index, is an effective index for understanding the unloading phenomenon. Theoretically, when this pressure drop index exceeds 1, shelf hanging, slipping, or blow-through will occur, but in actual furnaces, variations in the properties of the charge, wall surface friction, and load distribution of the charge in the radial direction of the blast furnace occur. The limit value of the pressure loss index (referred to as the critical pressure loss index) at which shelving, slipping, or blow-through occurs due to the influence of gas drift, etc. takes a value of 1 or less. After all, Fig. 3 is a graph showing the relationship between the pressure drop index in Berry svc and the number of occurrences of slip (including shelf hanging), which was obtained from the operating results of blast furnaces.In order to prevent slip occurrence, vcF' i. It can be seen that this pressure loss index should be kept smaller than 0.3.

このように高炉操業において棚吊り、スリップ又は吹抜
けの発生を防止するため&Ctj圧損指数を上述の限界
圧損指数以下とすべく送風条件を設定して高炉操業を行
うとよい。なお圧損指数とスリップの発生回数との関係
は第3図に示したベリ一部におけるデータが最も相関が
強いことが実験的に明らかにされた。
As described above, in order to prevent the occurrence of shelving, slipping, or blow-through during blast furnace operation, it is preferable to perform blast furnace operation by setting air blowing conditions so that the &Ctj pressure loss index is equal to or less than the above-mentioned critical pressure loss index. It has been experimentally revealed that the relationship between the pressure loss index and the number of slip occurrences is the strongest in the data for the part of the verge shown in Figure 3.

次に本発明方法を実施例に基いて詳述する。第4図は本
発明方法の実施状態を示す模式図であり、高炉lにはそ
のシャフト上部、シャフト中部、シャフト下部、ベリ一
部、ボッシュs#c夫々圧力計2a、2b、2c、2d
、2eが取り付けられており、各部分における炉壁静圧
が測定されるよう罠なっている。このようにして得られ
る各部分における炉壁静圧のデータは圧力損失測定値w
13へ入力され、一方炉頂に取り付けられた圧力計2f
により測定−される炉頂圧のデータも圧力損失測定値f
ll13へ入力され、両データより各炉壁靜圧側′1ど
位置から炉頂までの圧力損失が求められる。送風量算出
装置4 flc u 、この圧力損失のデータが入力さ
れるが、他にも羽口1aより高炉l内へ送風される熱風
の送風量測定値、炉内装入物比重及び過去のデータに基
いて予め設定しである炉高さごとの限界圧損指数に関す
るデータも入力され、これらのデータに基いて送風算出
装hlr4t;t、第6図の算出フロー図に示す如く限
界送風量を算出する。
Next, the method of the present invention will be explained in detail based on examples. FIG. 4 is a schematic diagram showing the implementation state of the method of the present invention, and the blast furnace 1 includes the upper shaft, middle shaft, lower shaft, part of the burr, and Bosch S#C pressure gauges 2a, 2b, 2c, and 2d, respectively.
, 2e are installed to form a trap so that the furnace wall static pressure at each section can be measured. The data of the furnace wall static pressure in each part obtained in this way is the measured pressure loss w
13, and a pressure gauge 2f installed on the top of the furnace.
The data of the furnace top pressure measured by the pressure loss measurement value f
ll13, and from both data, the pressure loss from each furnace wall quiet pressure side position '1' to the furnace top is determined. The air flow calculation device 4 flc u inputs this pressure loss data, but also inputs the measured air flow amount of the hot air blown into the blast furnace l from the tuyere 1a, the specific gravity of the contents in the furnace, and past data. Based on this, data regarding the limit pressure drop index for each furnace height, which has been set in advance, is also input, and based on these data, the air blast calculation device calculates the limit air blast amount as shown in the calculation flow diagram of Figure 6. .

そしてこの限界送風量に基いて熱風調整器6により羽口
1aからの熱風送風量が調整される。斯くして限界送風
−以下で熱風が送風されることにより棚吊り、スリップ
又は吹抜けの発生を防止することができる。
The amount of hot air blown from the tuyere 1a is adjusted by the hot air regulator 6 based on this limit amount of air blown. In this way, by blowing hot air below the air blowing limit, it is possible to prevent shelf hanging, slipping, or blow-through.

次に第5図の算出フロー図の内容について詳しく述べる
。一般に圧損指数dは王妃(1)式にて求められる。
Next, the contents of the calculation flow diagram shown in FIG. 5 will be described in detail. Generally, the pressure loss index d is determined by the Queen's formula (1).

但し、ΔP1′:各位置1から炉頂までの圧力損失測定
値、(炉内圧力損失測定値) γ8=装入物比重 L:各位置1から炉頂までの距離 また棚吊り、スリップ又は吹抜けが発生する限界におけ
る圧損指数(限界圧損指数)αは下記(2)式にて求め
られるので、 但し ΔP1:棚吊り、スリップ又は吹抜けが発生する
限界における圧力損失(限 界炉内圧力損失) 限界炉内圧力損失ΔP1は下記(3)式にて求めらnる
0ΔPl=α×γ8XL     −・・(3)また炉
内圧力損失測定値ΔP1′及び送風量測定+i1V’を
用いると炉内装入物の通気抵抗に□は下記(4)式にて
求められる。
However, ΔP1': Measured value of pressure loss from each position 1 to the top of the furnace, (measured value of pressure loss inside the furnace) γ8 = Specific gravity of the charge L: Distance from each position 1 to the top of the furnace, as well as shelf suspension, slip, or blow-through The pressure drop index α at the limit where this occurs (limit pressure drop index) is determined by the following formula (2), where: ΔP1: Pressure loss at the limit where shelving, slipping, or blow-through occurs (limit furnace pressure loss) Limit furnace The internal pressure loss ΔP1 is calculated using the following formula (3) n0ΔPl=α×γ8XL - (3) Also, using the measured value ΔP1' of the pressure loss in the furnace and the air flow measurement +i1V', the The ventilation resistance □ is determined by the following equation (4).

但し C6:炉内装入物のガス密度 β:定数(例えば0.58) これらの値を用いることに工9、棚吊り、スリップ又は
吹抜けが発生する限界における送風量(限界送風量) 
Vは、下記ti1式にて求められる0斯くして各測定位
置土ごとに炉内装入物の通気抵抗−を求めながら限界送
風量Vを算出する。そして送風量測定値V′を下記(6
)式に示す如く限。拝送風量V (各測定値f111の
中で最小値をとる)以下に設定して高炉操業を行う。
However, C6: Gas density β of the contents in the furnace: constant (for example, 0.58) By using these values, the air flow rate at the limit at which shelving, slipping, or blow-through occurs (limit air flow rate)
V is determined by the equation ti1 below.Thus, the limit ventilation amount V is calculated while determining the ventilation resistance of the contents in the furnace for each measurement position soil. Then, the measured air flow rate V' is shown below (6
) as shown in the formula. Blast furnace operation is performed by setting the airflow volume to V (the minimum value is taken among the measured values f111) or less.

(6)式Fiil1式、(3)弐及び(4)式を用いて
変形すると下記())式のようになる。
When the equation (6) is transformed using the Fiil1 equation, (3) II, and (4) equation, it becomes the following equation ()).

即ち(6)式に示す送風条件にて高炉操業を行う場合に
、圧損指数α′を限界圧損指数α以下に保持することが
でき、棚吊り、スリップ又は吹抜けを防止することがで
きるのである。
That is, when operating the blast furnace under the air blowing conditions shown in equation (6), the pressure loss index α' can be kept below the critical pressure loss index α, and hanging, slipping, or blow-through can be prevented.

以1詳述した如く本発明による高炉送風方法は、高炉炉
頂圧を測定すると共に炉壁における高さが異なる複数の
位ltにて炉壁静圧を測定し、これらの測定値により各
炉壁静圧−1定位を直から炉r14までの圧力損失を求
め、一方操業条件により炉頂から各炉壁靜圧測定位li
1までの装入物荷重を求め、各炉壁静圧測定位置につい
て前記圧力損失と装入物荷重との比、即ち圧損指数を求
め、各測定値1i1についてこの圧損指数が棚吊り、ス
リップ又は吹抜けが発生する限界値(限界圧損指数)以
下となるように送風条件を設定するので、高炉内各部分
における異常を把握することができる。従って吹抜は指
数が一定値を越えないように送風圧f股+iVする従来
の方法では防止しきれない異常の発生、即ち炉内の温度
、装入物性状等の分布に起因する異常の発生をも防止す
ることができ、高炉操業の安定化及び高炉の長寿命化を
図る上で多大の効果を奏する。
As described in detail below, in the blast furnace air blowing method according to the present invention, the blast furnace top pressure is measured, and the furnace wall static pressure is measured at a plurality of positions at different heights on the furnace wall. The pressure loss from the wall static pressure -1 position directly to the furnace r14 is determined, and on the other hand, depending on the operating conditions, each furnace wall static pressure measurement position li is determined from the furnace top.
1, the ratio of the pressure loss to the charge load, that is, the pressure drop index, is determined for each furnace wall static pressure measurement position, and for each measurement value 1i1, this pressure drop index is Since the blowing conditions are set to be below the limit value (limit pressure drop index) at which blow-through occurs, abnormalities in each part of the blast furnace can be ascertained. Therefore, in the atrium, the occurrence of abnormalities that cannot be prevented by the conventional method of increasing the blowing pressure f + iV so that the index does not exceed a certain value, that is, the occurrence of abnormalities due to the distribution of the temperature inside the furnace, the properties of the charged materials, etc. It is also possible to prevent this, which is highly effective in stabilizing blast furnace operation and extending the life of the blast furnace.

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

第1図は圧力損失と炉高さとの関係を示す、グラフ、第
2図は装入物荷重と炉高さとの関係を示すグラフ、第3
図はベリー都における圧損用9とスリップ発生回数との
関係を示すグラフ、第4図は本発明方法の実施状態を示
す模式図、第5図は限界送風量の算出フロー図である。 l・・・高炉 2a、−b・・・f・・・圧力計3・・
・圧力損失測定装@ 4・・・送風量算出装前5・・・
熱風a4紮器 特許出願人 住友金稿工業株式会社 代理人 弁理士 河  野  登  夫雛 4 閃 俸 !513!1 特許庁長官 殿 /、 事件の表示  唱和56牛特許願第168298
号2 発明の名称  高炉送風方法 J、補正をする者 事件との陶体  特許出−人 ダ代理人 j、補正の対象 明細書の「発明の詳細な説明」の欄
Figure 1 is a graph showing the relationship between pressure loss and furnace height. Figure 2 is a graph showing the relationship between burden load and furnace height.
The figure is a graph showing the relationship between the pressure loss 9 and the number of slip occurrences in Berry City, FIG. 4 is a schematic diagram showing the implementation state of the method of the present invention, and FIG. 5 is a flowchart for calculating the critical air flow rate. l...Blast furnace 2a, -b...f...Pressure gauge 3...
・Pressure loss measurement device @ 4...Before air flow rate calculation device 5...
Hot air A4 rig patent applicant Sumitomo Kinko Kogyo Co., Ltd. agent Patent attorney Noboru Kono 4 Sensai! 513!1 Mr. Commissioner of the Japan Patent Office/, Case Indication Recitation 56 Cattle Patent Application No. 168298
No. 2 Title of the invention Blast furnace air blowing method J, Ceramic body with the case of the person making the amendment Patent originator's agent J, "Detailed description of the invention" column of the specification subject to the amendment

Claims (1)

【特許請求の範囲】[Claims] 1・高炉炉頂圧を測定すると共に、炉壁における高さが
異なる複数の位置にて炉壁静圧を測定し、これらの測定
値により各炉壁静圧測定位置から炉頂までの圧力損失を
求める一方、操業条件により炉頂から各炉壁靜圧測定位
厘までの装入物荷重を求め、各炉壁静圧611定位置に
ついて前記圧力損失と装入物荷重との比を求め、この比
が、棚吊り、スリップ又は吹抜けを発生させないように
予め規定しである条件を満たすように送風条件を設定す
ることを特徴とする高炉送風方法。
1. In addition to measuring the blast furnace top pressure, the furnace wall static pressure is also measured at multiple positions at different heights on the furnace wall, and these measured values are used to calculate the pressure loss from each furnace wall static pressure measurement position to the furnace top. At the same time, determine the charge load from the furnace top to each furnace wall static pressure measurement position according to the operating conditions, and determine the ratio of the pressure loss to the charge load for each furnace wall static pressure 611 fixed position, A method for blowing air in a blast furnace, characterized in that the blowing conditions are set so that this ratio satisfies a predetermined condition so as not to cause shelving, slipping, or blow-through.
JP16829881A 1981-10-20 1981-10-20 Blasting method for blast furnace Granted JPS5871310A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16829881A JPS5871310A (en) 1981-10-20 1981-10-20 Blasting method for blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16829881A JPS5871310A (en) 1981-10-20 1981-10-20 Blasting method for blast furnace

Publications (2)

Publication Number Publication Date
JPS5871310A true JPS5871310A (en) 1983-04-28
JPH0120203B2 JPH0120203B2 (en) 1989-04-14

Family

ID=15865417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16829881A Granted JPS5871310A (en) 1981-10-20 1981-10-20 Blasting method for blast furnace

Country Status (1)

Country Link
JP (1) JPS5871310A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2572096A1 (en) * 1984-10-19 1986-04-25 Usinor METHOD AND INSTALLATION FOR THE CONTINUOUS MONITORING OF BLAST FURNACES

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2572096A1 (en) * 1984-10-19 1986-04-25 Usinor METHOD AND INSTALLATION FOR THE CONTINUOUS MONITORING OF BLAST FURNACES

Also Published As

Publication number Publication date
JPH0120203B2 (en) 1989-04-14

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