JPS6320405A - Skirt control method for converter waste gas treatment device - Google Patents

Skirt control method for converter waste gas treatment device

Info

Publication number
JPS6320405A
JPS6320405A JP16389686A JP16389686A JPS6320405A JP S6320405 A JPS6320405 A JP S6320405A JP 16389686 A JP16389686 A JP 16389686A JP 16389686 A JP16389686 A JP 16389686A JP S6320405 A JPS6320405 A JP S6320405A
Authority
JP
Japan
Prior art keywords
waste gas
skirt
flow rate
converter
surging
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
JP16389686A
Other languages
Japanese (ja)
Inventor
Nobuyasu Sakanashi
坂梨 暢泰
Hiroshi Yamane
山根 博史
Kiyokazu Sakane
坂根 清和
Takeya Fukumoto
福本 武也
Katsuya Sakagami
阪上 勝弥
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.)
Fuji Electric Co Ltd
Nippon Steel Corp
Original Assignee
Fuji Electric Co Ltd
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 Fuji Electric Co Ltd, Nippon Steel Corp filed Critical Fuji Electric Co Ltd
Priority to JP16389686A priority Critical patent/JPS6320405A/en
Publication of JPS6320405A publication Critical patent/JPS6320405A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To prevent surging of a fan by raising a skirt up to a prescribed height when the state of the decrease of the flow rate of a waste gas down to a prescribed value or below continues at the time of treating and recovering the waste gas while the throat and skirt of a converter are held hermetically closed. CONSTITUTION:The throat and skirt (inside seal) 4a of the converter 1 are held hermetically closed or are put in the state approximately similar thereto and blowing is executed in this state with the converter 1. The waste gas generated at this time is sucked and discharged through dust collectors 11a, 11b by the induced draft fan 14. The gaseous pressure at the throat part is detected by an in-furnace detector 6 and the opening degree of a damper 12 in the secondary dust collector 11b is controlled. A control device 15 controls a skirt operating device 16 in accordance with the signal from a waste gas flow rate transmitter 5 to rise the skirt 4a and to admit the atm. air from the spacing between the skirt 4a and the throat when the state of the decrease of the flow rate of the waste gas down to the prescribed value or below continues for the prescribed time or longer. The generation of the surging in the fan 14 is thereby prevented and the safe operation is executed.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、誘引送風機(IDファン)のサージング防
止機能を備えた転炉廃ガス処理装置(OG)におけるス
カート制御方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a skirt control method in a converter waste gas treatment device (OG) equipped with a surging prevention function of an induced fan (ID fan).

(従来の技術) 従来の転炉廃ガス処理装置においては通常、炉口部の上
部に位置するスカート部を炉口部に密着させることなく
操業しており、このため炉圧または炉内圧は約プラス、
マイナス数鰭H20(水柱)の範囲に入っていた。すな
わち、炉内圧が大気圧よりも低ければ炉口とスカートの
隙間から空気が吸引されるので、廃ガス発生量が少ない
ときにも所定の炉圧側j1をしていれば結果として成る
程度の廃ガス流量が得られ、これによって送風機のサー
ジングを防止することができた。
(Prior art) Conventional converter waste gas treatment equipment is normally operated without bringing the skirt part located above the furnace mouth into close contact with the furnace mouth, and therefore the furnace pressure or furnace internal pressure is approximately plus,
It was within the range of minus several fins H20 (water column). In other words, if the furnace internal pressure is lower than atmospheric pressure, air will be sucked in from the gap between the furnace mouth and the skirt, so even when the amount of waste gas generated is small, if the specified furnace pressure side Gas flow rates were obtained, which prevented blower surging.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、スカートを炉口部に密着ないしこれに近
い状態で操業するときに炉内からの廃ガス発生量が少な
くなると、炉圧制御をしていても炉口部から空気が吸引
できないか、またはできても極く少量のため廃ガス流量
があまり増えず、結果としてサージングが防止できない
と云う問題がある。つまり、転炉廃ガス処理装置は設備
を安全に保ちながら廃ガスの冷却、集塵1回収を行いつ
\吹錬を継続するためのもので、安全性を確保すること
が最も基本的なことであるから、送風機がサージングを
起こせば操業を停止せざるを得ない。
However, if the amount of waste gas generated from the furnace decreases when the skirt is in close contact with or close to the furnace mouth, air cannot be sucked from the furnace mouth even if the furnace pressure is controlled, or Even if it were possible, the amount would be very small, so the flow rate of the waste gas would not increase much, and as a result, there would be a problem that surging could not be prevented. In other words, the converter waste gas treatment equipment is designed to keep the equipment safe while cooling the waste gas, collecting dust, and continuing blowing.Ensuring safety is the most fundamental thing. Therefore, if the blower causes surging, the operation must be stopped.

したがって、この発明は送風機のサージングを防止して
安全操業を図ることを目的とする。
Therefore, it is an object of the present invention to prevent the blower from surging and to ensure safe operation.

(問題点を解決するための手段〕 送風機の入ロダンパ間度を段階的に制御してサージング
防止を行う転炉廃ガス処理装置において、廃ガス流量を
監視し、その2it量が所定値以下となる状態がある時
間以上続いたときはスカートを所定の高さまで上昇させ
る。
(Means for solving the problem) In a converter waste gas treatment system that prevents surging by controlling the blower inlet damper in stages, the waste gas flow rate is monitored and the amount of 2 it is below a predetermined value. If this condition continues for a certain period of time, the skirt is raised to a predetermined height.

(作用〕 つまり、スカート部を炉口部に密着させることなく操業
する従来のタイプでは、炉圧制御している限りはか\る
サージングを回避することができるのは前述の通りであ
るが、炉口とスカートとを密閉またはこれと略同等の状
態にして操業するタイプのものではこのサージング問題
を避けることが出来ず、しかも現在ある転炉廃ガス処理
装置にはこの種のものが多いので、上記の如(すること
によって炉口からの空気吸引量を増大させ、サージング
が発生しないようにする。
(Operation) In other words, as mentioned above, in the conventional type, which operates without bringing the skirt part into close contact with the furnace mouth, severe surging can be avoided as long as the furnace pressure is controlled. This surging problem cannot be avoided with the type of equipment that operates with the furnace mouth and skirt sealed or in a similar state, and many of the existing converter waste gas treatment equipment are of this type. By doing the above, the amount of air sucked from the furnace mouth is increased to prevent surging from occurring.

〔実施例〕〔Example〕

第1図はこの発明の詳細な説明するための説明図、第2
図はこの発明が実施される転炉廃ガス処理装置の具体例
を示す概要図、第3図はサージング防止制御方法の改良
された従来例を説明するためのグラフである。
FIG. 1 is an explanatory diagram for explaining the invention in detail, and FIG.
The figure is a schematic diagram showing a specific example of a converter waste gas treatment apparatus in which the present invention is implemented, and FIG. 3 is a graph for explaining a conventional example of an improved surging prevention control method.

まず、第2図について説明する。なお、同図において、
1は転炉、2は溶銑およびスクラップ、3は上吹ランス
、4aはスカート(内側シール)、4bはスカート(外
側シール)、5は廃ガス流量発信器、6は炉内圧発信器
、7はフード部、8は送風機人口ダンパ(サクションダ
ンパ)、9はダンパ操縦器、10は上部安全弁、lla
は1次集塵器、llbは2次集塵器、12はダンパ、1
3は電油操縦器、14は誘引送風機、15は制御装置、
16はスカート操作装置(油圧装置)である。
First, FIG. 2 will be explained. In addition, in the same figure,
1 is a converter, 2 is hot metal and scrap, 3 is a top blowing lance, 4a is a skirt (inner seal), 4b is a skirt (outer seal), 5 is a waste gas flow rate transmitter, 6 is a furnace pressure transmitter, 7 is a Hood section, 8 is a blower artificial damper (suction damper), 9 is a damper controller, 10 is an upper safety valve, lla
is the primary dust collector, llb is the secondary dust collector, 12 is the damper, 1
3 is an electrohydraulic controller, 14 is an induced blower, 15 is a control device,
16 is a skirt operating device (hydraulic device).

転炉1の中に主原料としてスクラップ、溶銑2を装入し
、転炉上部からランス3を用いて高圧酸素を吹き込み、
溶銑を精鉄して溶鋼にする。このことを吹錬という。こ
の吹錬中に、酸素は溶銑中の炭素と化合し、COガスを
主成分とする廃ガスを発生する。この廃ガスは約120
0℃の高温であり、約150g/Nm’という多量の酸
化鉄系ダストを含んでいる。この廃ガスは高温であるか
ら、装置本体を保護するためフード部7は水冷管にて水
冷される。一方、この廃ガス中のダストを除去するため
に1次集塵器(IDC)lla、2次集塵器(2DC)
llbが設けられている。これらの集塵器は集塵水を用
いた方式であるため、廃ガスは急冷されて温度は70℃
まで下がる。廃ガスから除塵をするためには、先の2つ
の集塵器のところでガスを高速で通過させる必要があり
、各集塵器113.11bにはダンパを備え、絞り機構
となっている。また、ガス吸引は誘引送風機14によっ
て行われる。炉口部のガス圧力は炉内圧力(炉内圧)と
呼ばれ、これは炉内圧検出器6で検出されると\もに、
制御装置15を用いて2次集塵器11b内のダンパ12
を動かすことにより制御される。なお、このダンパの駆
動には通常電池操縦器13が使用されている。炉内圧は
通常大気圧近くに制御され、炉口部とスカート(内側シ
ール)4aとの隙間からガスが吹出したり、大気を吸引
したりする量をできるだけ少なくなるようにしている0
通常、スカート4aと炉口の隙間が200 u位であれ
ば、炉内圧はプラス、マイナス数ta Hz Oの間で
制御される。しかし、スカー)4aを下げ、さらに外側
シール4bと呼ばれるスカートを炉体に密着させる装置
を動作させると、炉口部の隙間は殆んど無くなる。この
ような密閉状態で操作すると、炉圧の振れ幅は大きくな
り、異常時にはプラス、マイナス数百am H! Oに
なり得る。このため、制御装置15により種々の炉圧制
御を行い、安全操業を図るようにしている。
Scrap and hot metal 2 are charged as main raw materials into a converter 1, and high pressure oxygen is blown into the converter using a lance 3 from the top of the converter.
Refining hot metal into molten steel. This is called blowing. During this blowing, oxygen combines with carbon in the hot metal to generate waste gas mainly composed of CO gas. This waste gas is approximately 120
It has a high temperature of 0°C and contains a large amount of iron oxide dust of about 150 g/Nm'. Since this waste gas has a high temperature, the hood part 7 is water-cooled with a water-cooled pipe to protect the main body of the apparatus. On the other hand, in order to remove the dust in this waste gas, a primary dust collector (IDC) lla and a secondary dust collector (2DC) are installed.
llb is provided. Since these dust collectors use dust collecting water, the waste gas is rapidly cooled to a temperature of 70°C.
down to In order to remove dust from the waste gas, it is necessary to pass the gas through the first two dust collectors at high speed, and each dust collector 113.11b is equipped with a damper and serves as a throttling mechanism. Further, gas suction is performed by an induced fan 14. The gas pressure at the furnace mouth is called the furnace pressure (furnace pressure), and when it is detected by the furnace pressure detector 6,
The damper 12 in the secondary dust collector 11b is controlled using the control device 15.
It is controlled by moving the . Note that a battery controller 13 is normally used to drive this damper. The pressure inside the furnace is usually controlled close to atmospheric pressure to minimize the amount of gas blown out or the amount of atmospheric air sucked through the gap between the furnace mouth and the skirt (inner seal) 4a.
Normally, if the gap between the skirt 4a and the furnace mouth is about 200 μ, the furnace pressure is controlled between plus and minus several ta Hz O. However, if the skirt 4a is lowered and a device called an outer seal 4b that brings the skirt into close contact with the furnace body is operated, the gap at the furnace mouth will almost disappear. When operated in such a closed state, the fluctuation of the furnace pressure becomes large, and in the event of an abnormality, it can exceed + or - several hundred amH! It can be O. For this reason, the control device 15 performs various furnace pressure controls to ensure safe operation.

こ\で、送風機14のサージング防止制御について説明
する。
Here, surging prevention control of the blower 14 will be explained.

一般に転炉廃ガス処理用送風機においては、送風量がそ
の流量−圧力特性線の頂点以下の流量に低下すると、風
圧および風量が振動して騒音を発生する、いわゆるサー
ジング現象が起る。送風機の送風量がサージングの発生
する点の流量以下に低下したとき、ダンパまたは吸込弁
の開度を絞り送風機の吐出圧力を下げるようにすれば、
送風機の流量−圧力特性が変わるので、これによりサー
ジングの発生を防止することができる。このような方法
により、送風機のダンパ開度を送風量に応じて連続的に
制御する制御方法があるが、この方法では送風量が絶え
ず変動する場合はダンパの操作頻度が高くなり、このた
めダンパの回転部分の摩耗が大きくなってその寿命が短
(なると云う問題がある。
Generally, in a converter waste gas processing blower, when the air flow rate decreases to a flow rate below the peak of the flow rate-pressure characteristic line, a so-called surging phenomenon occurs in which the wind pressure and air volume vibrate and generate noise. When the airflow rate of the blower drops below the flow rate at which surging occurs, the opening of the damper or suction valve can be throttled to lower the blower's discharge pressure.
Since the flow rate-pressure characteristics of the blower change, it is possible to prevent surging from occurring. There is a control method that continuously controls the damper opening degree of the blower according to the air flow rate, but with this method, if the air flow rate constantly fluctuates, the damper has to be operated more frequently, so the damper There is a problem that the wear of the rotating parts of the motor increases and its lifespan becomes short.

このような問題を回避するため、ダンパ開度を送風機の
送風量に応じて段階的に制御する方法もある。この方法
によれば、ダンパ開度を連続的に制御するものに比べて
操作頻度は低下するが、ダンパの段階的な各開度は、送
風量が各開度対応の流量設定値よりも大きいかまたは小
さいかによって決定されるので、成る流量設定値近傍で
送風量が変動すると、ダンパが開閉を繰返し、動作が不
安定となる欠点がある。
In order to avoid such problems, there is also a method of controlling the damper opening degree in stages according to the amount of air blown by the blower. According to this method, the frequency of operation is lower than when the damper opening is controlled continuously, but each stepwise opening of the damper means that the air volume is larger than the flow rate set value corresponding to each opening. Therefore, if the air flow rate fluctuates near the set flow rate, the damper will repeatedly open and close, resulting in unstable operation.

このような欠点を除去すべく、次の如きサージング防止
方法が提案されている(特公昭58−10598号公報
)。第3図はか\る方法を説明するためのグラフである
In order to eliminate such drawbacks, the following surging prevention method has been proposed (Japanese Patent Publication No. 58-10598). FIG. 3 is a graph for explaining the method.

これは、送風量に応じてダンパ開度をA(20%)、B
(40%)、C(60%)、D(80%)。
This means that the damper opening degree can be set to A (20%) or B depending on the air flow rate.
(40%), C (60%), D (80%).

E(100%)の如く段階的に制御すると\もに、ダン
パ開度の切換点に対応する送風量設定値に対し、送風量
が減少するとき(F+ 、F3.FS+F?)と増加す
るとき(F2 、F4.F4 、Fs )とで成る幅の
ヒステリシス(例えばΔF参照)を持たせることにより
、ダンパの操作頻度を低下させ、動作の安定化を図るも
のである。なお、同図のS+ 、St 、Sz 、S4
.Ssが流量−圧力特性の頂点であり、その右側が安全
領域、左側がサージング領域と云うことになる。
When controlling in stages like E (100%), when the airflow rate decreases (F+, F3.FS+F?) and when it increases with respect to the airflow setting value corresponding to the switching point of the damper opening degree. By providing a hysteresis (for example, see ΔF) with a width of (F2, F4.F4, Fs), the frequency of operation of the damper is reduced and the operation is stabilized. In addition, S+, St, Sz, S4 in the same figure
.. Ss is the peak of the flow rate-pressure characteristic, and the right side is the safe area and the left side is the surging area.

次に、この発明の実施例につき第1図を参照して説明す
る。なお、同図(イ)は送風機のmff1−圧力特性に
応じたサージング防止制御特性を示すグラフ、同図(ロ
)は廃ガス流量の時間的変化を示すグラフ、同図(ハ)
はスカート高さの変化を示すグラフである。
Next, an embodiment of the present invention will be described with reference to FIG. In addition, the same figure (a) is a graph showing the surging prevention control characteristics according to the mff1-pressure characteristics of the blower, the same figure (b) is a graph showing the temporal change in the exhaust gas flow rate, the same figure (c)
is a graph showing changes in skirt height.

すなわち、この実施例はサージング防止制御を第3図と
同様に行うもので、送風量(廃ガス流量)が時間と\も
に減少するとき、ダンパ開度を廃ガス流量に応じて段階
的に変更する。例えば、流量F、では開度を100%か
ら80%に、流量FSでは開度を80%から60%に、
流it F 3では開度を60%から40%に、さらに
流IFlでは開度を40%から20%にそれぞれ変更す
る。こ\で、ダンパの開度の最小値を20%と定めてい
るものとすれば、廃ガス流量がF、よりさらに減少し続
けるとサージングが発生する。つまり、同図(イ)のグ
ラフの開度20%の特性カーブ(E)上の点S、で示さ
れた流量以下になれば、サージング領域に入る。したが
って、これより若干太き目の流量F0を予め定めておき
、廃ガス流量がこの設定値F0以下となり且つこれが一
定時間(同図(ロ)のt参照)以上継続すれば、同図(
ハ)の如くスカート高さを例えばhlmmだけ上昇させ
る。これにより、スカートと炉口間からの吸引空気量が
増大するので、廃ガス流量も増大することになる。しか
し、このような操作にもか\わらず、さらに炉内発生ガ
スが減少して廃ガス流量が再度F0以下となり、これが
t秒以上継続すれば同図(ハ)の如(再びスカート高さ
をhamsになる迄上昇させるようにする。なお、廃ガ
ス流量の監視は発信器5からの信号にもとづき制御装置
15にて行われ、こ\で廃ガス流量が所定値F0以下と
なる状態が所定時間以上続いたことが検出されると、油
圧装置からなるスカートff1作装置16を介して以上
の如き制御が行われる。
In other words, this embodiment performs surging prevention control in the same way as shown in Fig. 3, and when the air flow rate (waste gas flow rate) decreases over time, the damper opening degree is adjusted in stages according to the exhaust gas flow rate. change. For example, for flow rate F, the opening degree is changed from 100% to 80%, and for flow rate FS, the opening degree is changed from 80% to 60%.
In flow it F3, the opening degree is changed from 60% to 40%, and in flow IFl, the opening degree is changed from 40% to 20%. Here, assuming that the minimum value of the damper opening is set at 20%, surging will occur if the exhaust gas flow rate continues to decrease further than F. In other words, when the flow rate falls below the point S on the characteristic curve (E) at 20% opening in the graph of FIG. Therefore, a flow rate F0 that is slightly thicker than this is predetermined, and if the waste gas flow rate becomes less than this set value F0 and continues for a certain period of time (see t in the same figure (b)),
As shown in c), the skirt height is raised by, for example, hlmm. As a result, the amount of air sucked between the skirt and the furnace mouth increases, so the flow rate of the exhaust gas also increases. However, despite these operations, the gas generated in the furnace further decreases and the waste gas flow rate falls below F0 again, and if this continues for more than t seconds, the skirt height will rise again as shown in Figure (C). hams.The exhaust gas flow rate is monitored by the control device 15 based on the signal from the transmitter 5, and the state where the exhaust gas flow rate is below the predetermined value F0 is detected. When it is detected that the elongation continues for a predetermined period of time or more, the above-described control is performed via the skirt ff1 making device 16, which is a hydraulic device.

〔発明の効果〕〔Effect of the invention〕

この発明によれば、転炉の炉口とスカートとを密閉また
はこれと略同等の状態にして操業する転炉廃ガス処理装
置にてサージング防止制御を行うに当たり、廃ガス流量
が所定値以下となる状態が所定時間以上続いたときはス
カートを所定の高さ迄上昇させるだけの筒車な操作によ
り吹錬を4!!続できるので、安定操業に大きく貢献し
得る利点がもたらされる。
According to this invention, when performing surging prevention control in a converter waste gas treatment device that operates with the converter mouth and skirt sealed or in a substantially equivalent state, the waste gas flow rate is determined to be below a predetermined value. If this condition continues for more than a predetermined time, blowing is performed by simply raising the skirt to a predetermined height. ! This provides advantages that can greatly contribute to stable operation.

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

第1図はこの発明の詳細な説明するための説明図、第2
図はこの発明が実施される転炉廃ガス処理装置を示す概
要図、第3図はサージング防止制御方法の改良された従
来例を説明するためのグラフである。 符号説明 1・・・転炉、2・・・溶銑およびスクラップ、3・・
・上吹ランス、4a・・・スカート(内側シール)、4
b・・・スカート(外側シール)5・・・廃ガス流量発
信器、6・・・炉内圧発信器、7・・・フード部、8・
・・送風機人ロダンバ、9・・・ダンパ操縦器、10・
・・上部安全弁、11a・・・1次集塵器、llb・・
・2次集塵器、13・・・電油操縦器、14・・・誘引
送風機、15・・・制御装置、16・・・スカート操作
装置、A−4・・・流量−圧力特性図、S、−SS・・
・頂点、F、・・・廃ガス流量設定値。 代理人 弁理士 並 木 昭 夫 代理人 弁理士 松 崎   清 第1図 的闇υ)〕 1113  図
FIG. 1 is an explanatory diagram for explaining the invention in detail, and FIG.
The figure is a schematic diagram showing a converter waste gas treatment apparatus in which the present invention is implemented, and FIG. 3 is a graph for explaining a conventional example of an improved surging prevention control method. Code explanation 1... Converter, 2... Hot metal and scrap, 3...
・Top blow lance, 4a...Skirt (inner seal), 4
b... Skirt (outer seal) 5... Waste gas flow rate transmitter, 6... Furnace pressure transmitter, 7... Hood part, 8...
... Blower Rodanba, 9... Damper controller, 10.
...Top safety valve, 11a...Primary dust collector, llb...
- Secondary dust collector, 13... Electrohydraulic controller, 14... Induced blower, 15... Control device, 16... Skirt operating device, A-4... Flow rate-pressure characteristic diagram, S, -SS...
・Vertex, F, ... Waste gas flow rate setting value. Agent Patent Attorney Akio Namiki Agent Patent Attorney Kiyoshi Matsuzaki Figure 1 Darkness υ)] 1113 Figure

Claims (1)

【特許請求の範囲】 転炉の炉口とスカートとを密閉またはこれと略同等の状
態にして転炉からの廃ガスを処理、回収するとゝもに、
送風機のサージング防止制御を行う転炉廃ガス処理装置
において、 廃ガス流量を監視し、該廃ガス流量が所定値以下となる
状態が所定時間以上続いたときは前記スカートを所定の
高さまで上昇させることにより、送風機のサージングを
防止することを特徴とする転炉廃ガス処理装置における
スカート制御方法。
[Scope of Claims] Waste gas from the converter is treated and recovered by sealing the opening and skirt of the converter or in a state substantially equivalent to this, and
In a converter waste gas treatment device that performs surging prevention control of a blower, the waste gas flow rate is monitored, and when the waste gas flow rate remains below a predetermined value for a predetermined time or more, the skirt is raised to a predetermined height. A skirt control method in a converter waste gas treatment equipment, which is characterized by preventing surging of a blower.
JP16389686A 1986-07-14 1986-07-14 Skirt control method for converter waste gas treatment device Pending JPS6320405A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16389686A JPS6320405A (en) 1986-07-14 1986-07-14 Skirt control method for converter waste gas treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16389686A JPS6320405A (en) 1986-07-14 1986-07-14 Skirt control method for converter waste gas treatment device

Publications (1)

Publication Number Publication Date
JPS6320405A true JPS6320405A (en) 1988-01-28

Family

ID=15782868

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16389686A Pending JPS6320405A (en) 1986-07-14 1986-07-14 Skirt control method for converter waste gas treatment device

Country Status (1)

Country Link
JP (1) JPS6320405A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103883551A (en) * 2014-03-31 2014-06-25 国家电网公司 Control method for eliminating surge of axial flow fans

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103883551A (en) * 2014-03-31 2014-06-25 国家电网公司 Control method for eliminating surge of axial flow fans
CN103883551B (en) * 2014-03-31 2016-01-20 国家电网公司 A kind of controlling method eliminating axial-flow blower surge

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