JPH05271728A - Method for preventing blowby in blast furnace - Google Patents
Method for preventing blowby in blast furnaceInfo
- Publication number
- JPH05271728A JPH05271728A JP6669392A JP6669392A JPH05271728A JP H05271728 A JPH05271728 A JP H05271728A JP 6669392 A JP6669392 A JP 6669392A JP 6669392 A JP6669392 A JP 6669392A JP H05271728 A JPH05271728 A JP H05271728A
- Authority
- JP
- Japan
- Prior art keywords
- blowby
- pressure
- blast furnace
- value
- furnace
- 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
Links
Landscapes
- Blast Furnaces (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、高炉の吹抜けを事前に
予知してそれを防止する方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for predicting blow-through in a blast furnace in advance and preventing it.
【0002】[0002]
【従来の技術】一般に、高炉操業において、装入原料の
降下状態を管理することが重要で、炉下部から一定量の
熱風を送り、炉上部から一定スピードで装入原料を降下
させ、熱バランスを保つことが必要である。即ち、高炉
内部では炉上部から装入された鉄鉱石等の装入原料が下
降する間に、段階的に昇温、還元、溶融等の各過程を経
て、全体の熱的バランスが保たれる。2. Description of the Related Art Generally, in blast furnace operation, it is important to control the falling state of the charged raw material. It is necessary to keep That is, in the blast furnace, while the charging raw material such as iron ore charged from the upper part of the furnace descends, the overall thermal balance is maintained through steps such as stepwise temperature increase, reduction, and melting. .
【0003】高炉炉内で吹抜けやスリップが発生する
と、装入原料が上記過程を経ずに落下し、また、ガスの
保有する熱エネルギーが利用されないまま炉外に放出さ
れるため、熱バランスがくずれ、高炉炉内が冷え炉況不
調の原因になることが多い。When blow-through or slip occurs in the furnace of the blast furnace, the charging raw material falls without going through the above process, and the thermal energy held by the gas is released outside the furnace, so that the heat balance is maintained. It often collapses and the inside of the blast furnace cools down, often causing a malfunction of the furnace.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、高炉で
発生するガスの吹抜けを事前に予知する方法は、確立さ
れていない。そのため、原料の悪化や送風量の変更時、
吹抜けが発生し炉内の原料の層構造を乱し、大幅な減産
を招いていた。However, a method for predicting in advance the blow-through of gas generated in the blast furnace has not been established. Therefore, when the raw material deteriorates or the air flow is changed,
A blow-through occurred and disturbed the layer structure of the raw materials in the furnace, resulting in a significant reduction in production.
【0005】[0005]
【課題を解決するための手段】本発明は上記のような問
題点を解決しようとするもので、高炉のシャフト部の円
周方向に均等に配設した複数の圧力センサー群をシャフ
ト部の高さ方向の複数段に配設して圧力を計測し、同一
高さレベルの圧力センサーの計測圧力値の最大値と最小
値の差のその高さレベルの平均圧力値に対する割合が設
定割合を越えたとき減風することを特徴とする高炉の吹
抜け防止方法である。SUMMARY OF THE INVENTION The present invention is intended to solve the above-mentioned problems, and a plurality of pressure sensor groups, which are evenly arranged in the circumferential direction of the shaft portion of a blast furnace, are installed in the shaft portion. The pressure is measured by arranging it in multiple stages in the vertical direction, and the ratio of the difference between the maximum and minimum pressure values measured by pressure sensors at the same height level to the average pressure value at that height level exceeds the set ratio. This is a method for preventing blow-through in a blast furnace, which is characterized by reducing the wind when the wind blows.
【0006】[0006]
【作用】高炉のシャフト部の円周方向に配設した複数の
圧力センサー群をシャフト部の高さ方向に複数段配設し
て炉内のガス圧力を計測することにより、吹抜け前に発
生する円周方向の圧力バランスのくずれを検知すること
ができる。円周方向の圧力バランスのくずれを検知後、
ただちに減風を実施することにより、吹抜けを防止する
ことができる。[Function] A plurality of pressure sensor groups arranged in the circumferential direction of the shaft portion of the blast furnace are arranged in a plurality of stages in the height direction of the shaft portion to measure the gas pressure in the furnace, which occurs before the blow-through. It is possible to detect the collapse of the pressure balance in the circumferential direction. After detecting the collapse of the pressure balance in the circumferential direction,
By immediately reducing the wind, it is possible to prevent blow through.
【0007】[0007]
【実施例】本発明の実施例を以下に詳細に説明する。図
1は本発明に係る円周方向のガス圧力バランスの異常を
検知するブロック図である。図1において、1は高炉、
2は、高炉1のシャフト部2の側壁に設けられ、炉内側
壁近くを流れるガスの圧力を計測する圧力センサー3で
ある。圧力センサー3は、シャフト部2の円周方向を4
等分した位置に4個配置され、これらの圧力センサー3
が、シャフト部2の高さ方向に10段配置されている。EXAMPLES Examples of the present invention will be described in detail below. FIG. 1 is a block diagram for detecting abnormality of gas pressure balance in the circumferential direction according to the present invention. In FIG. 1, 1 is a blast furnace,
Reference numeral 2 denotes a pressure sensor 3 which is provided on the side wall of the shaft portion 2 of the blast furnace 1 and measures the pressure of gas flowing near the inner side wall of the furnace. The pressure sensor 3 moves the shaft 2 in the circumferential direction 4
These four pressure sensors 3 are arranged at equal positions.
Are arranged in 10 steps in the height direction of the shaft portion 2.
【0008】圧力センサー3の計測値は、A/D変換器
4を介して演算器5に送信される。演算器5には、各段
の円周方向の圧力偏差演算手段と各段の円周方向各位置
の圧力推移グラフ作成手段を有している。The measured value of the pressure sensor 3 is transmitted to the calculator 5 via the A / D converter 4. The calculator 5 has a pressure deviation calculating means in the circumferential direction of each stage and a pressure transition graph creating means in each position in the circumferential direction of each stage.
【0009】圧力偏差演算手段では、次の演算が行われ
る。 (1)測定時刻毎に各段の円周方向の最大圧力値
Pmax ,最小圧力値Pmin の差ΔP=Pmax −Pmin を
求める。 (2)測定時刻毎に各段の円周方向の圧力の平均値P
ave を求める。 (3)(ΔP/Pave )×100%≧5%について、YE
S かNOの判定を行う。 (4)YES であれば、表示器6に減風%の表示と警報が
出される。または、図示しない送風制御弁に減風の指示
が出される。なお、減風%は、そのときの炉況によって
3〜5%の間の数値が設定される。減風の表示と警報が
出された場合は、オペレータが送風制御弁を手動で操作
し減風を行う。The pressure deviation calculating means performs the following calculations. (1) The difference ΔP = P max −P min between the maximum pressure value P max and the minimum pressure value P min in the circumferential direction of each stage is calculated for each measurement time. (2) The average value P of the pressure in the circumferential direction of each stage at each measurement time
ask for ave . (3) For (ΔP / P ave ) × 100% ≧ 5%, YE
Judge S or NO. (4) If the answer is YES, the display 6 displays the reduced wind% and gives an alarm. Alternatively, an instruction to reduce air is issued to a blower control valve (not shown). Note that the wind reduction% is set to a value between 3 and 5% depending on the furnace conditions at that time. When the display and warning of the wind reduction are issued, the operator manually operates the blow control valve to reduce the wind.
【0010】圧力推移グラフ作成手段では、各段につい
て円周方向各位置別の推移が同一のグラフに作画され
る。作画されたグラフは表示器6に表示することがで
き、必要あれば図示しないプリンターでプリントアウト
することができる。In the pressure transition graph creating means, the transition for each position in the circumferential direction for each stage is drawn on the same graph. The graph thus drawn can be displayed on the display 6 and can be printed out by a printer (not shown) if necessary.
【0011】図2は、ある段の通常の安定操業時の円周
方向圧力の推移グラフの例であり、図3は、ある段の吹
抜けの兆候が現れた時の円周方向圧力の推移グラフの例
である。図3の例では、20分頃に(ΔP/Pave )×
100%≧5%となったので、3%の減風を実施し、吹
抜けを防止している。FIG. 2 is an example of a circumferential pressure transition graph during normal stable operation of a certain stage, and FIG. 3 is a circumferential pressure transition graph when there is an indication of blow-through of a certain stage. Is an example of. In the example of FIG. 3, about 20 minutes (ΔP / P ave ) ×
Since 100% ≧ 5%, a 3% wind reduction is implemented to prevent blow through.
【0012】[0012]
【発明の効果】本発明は上記のように構成されているか
ら、吹抜け発生前の兆候を確実に検知できるので、吹抜
けを防止することができる。従って、吹抜けによる減産
を防ぎ、安定な炉況を維持することができる。Since the present invention is constructed as described above, the sign before the occurrence of blow-through can be detected with certainty, so that blow-through can be prevented. Therefore, it is possible to prevent production decrease due to blow-through and maintain a stable furnace condition.
【図1】本発明に係る円周方向のガス圧力バランスの異
常を検知するブロック図である。FIG. 1 is a block diagram for detecting an abnormal gas pressure balance in a circumferential direction according to the present invention.
【図2】本発明に係る安定操業時の円周方向圧力の推移
例を示すグラフである。FIG. 2 is a graph showing an example of changes in circumferential pressure during stable operation according to the present invention.
【図3】本発明に係る吹抜けの兆候が現れた時の円周方
向圧力の推移例を示すグラフである。FIG. 3 is a graph showing an example of changes in circumferential pressure when a sign of blow-through according to the present invention appears.
1 高炉 2 シャフト部 3 圧力センサー 4 A/D変換器 5 演算器 6 表示器 1 Blast furnace 2 Shaft part 3 Pressure sensor 4 A / D converter 5 Computing unit 6 Indicator
───────────────────────────────────────────────────── フロントページの続き (72)発明者 岸本 純幸 東京都千代田区丸の内1丁目1番2号 日 本鋼管株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Sumiyuki Kishimoto 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Nihon Steel Pipe Co., Ltd.
Claims (1)
設した複数の圧力センサー群をシャフト部の高さ方向の
複数段に配設して圧力を計測し、同一高さレベルの圧力
センサーの計測圧力値の最大値と最小値の差のその高さ
レベルの平均圧力値に対する割合が設定割合を越えたと
き減風することを特徴とする高炉の吹抜け防止方法。1. A plurality of pressure sensor groups, which are evenly arranged in the circumferential direction of the shaft portion of a blast furnace, are arranged in a plurality of stages in the height direction of the shaft portion to measure the pressure, and the pressure at the same height level is measured. A method for preventing blow-through in a blast furnace, which comprises reducing air flow when the ratio of the difference between the maximum and minimum pressure values measured by a sensor to the average pressure value at that height level exceeds a set ratio.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6669392A JPH05271728A (en) | 1992-03-25 | 1992-03-25 | Method for preventing blowby in blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6669392A JPH05271728A (en) | 1992-03-25 | 1992-03-25 | Method for preventing blowby in blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05271728A true JPH05271728A (en) | 1993-10-19 |
Family
ID=13323277
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6669392A Pending JPH05271728A (en) | 1992-03-25 | 1992-03-25 | Method for preventing blowby in blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05271728A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56119708A (en) * | 1980-02-22 | 1981-09-19 | Nippon Steel Corp | Blast furnace operating method |
JPH01319611A (en) * | 1988-06-17 | 1989-12-25 | Kawasaki Steel Corp | Method of predicting slip in blast furnace operation |
JPH03215616A (en) * | 1990-01-19 | 1991-09-20 | Nkk Corp | Operation of blast furnace |
-
1992
- 1992-03-25 JP JP6669392A patent/JPH05271728A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS56119708A (en) * | 1980-02-22 | 1981-09-19 | Nippon Steel Corp | Blast furnace operating method |
JPH01319611A (en) * | 1988-06-17 | 1989-12-25 | Kawasaki Steel Corp | Method of predicting slip in blast furnace operation |
JPH03215616A (en) * | 1990-01-19 | 1991-09-20 | Nkk Corp | Operation of blast furnace |
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