JPS6270508A - Method for controlling recovering of waste gas from converter - Google Patents

Method for controlling recovering of waste gas from converter

Info

Publication number
JPS6270508A
JPS6270508A JP21024285A JP21024285A JPS6270508A JP S6270508 A JPS6270508 A JP S6270508A JP 21024285 A JP21024285 A JP 21024285A JP 21024285 A JP21024285 A JP 21024285A JP S6270508 A JPS6270508 A JP S6270508A
Authority
JP
Japan
Prior art keywords
oxygen
decarburization
rate
abnormal
damper
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
JP21024285A
Other languages
Japanese (ja)
Other versions
JPS6332844B2 (en
Inventor
Zenichi Meguro
目黒 善一
Hiroshi Yamashita
宏 山下
Yasuhiko Chiba
千葉 康彦
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 JP21024285A priority Critical patent/JPS6270508A/en
Publication of JPS6270508A publication Critical patent/JPS6270508A/en
Publication of JPS6332844B2 publication Critical patent/JPS6332844B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/38Removal of waste gases or dust
    • C21C5/40Offtakes or separating apparatus for converter waste gases or dust
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/38Removal of waste gases or dust

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Abstract

PURPOSE:To efficiently control the recovery of a waste gas from a converter by detecting the generation of abnormal decarburization from the full opening of a damper for adjusting the recovery of the waste gas, stepwise reducing the rate of the oxygen to be passed and restoring the rate of oxygen when the abnormal decarburization settles down. CONSTITUTION:The waster gas generated from the converter 9 is induced by an induced draft fan 12 into a recovery system and the damper 4 is operated in the open direction by a device 18 for controlling the recovery of the waste gas via an operating device 5 to prevent the overflow of the waste gas from the converter throat part 16. The rate of deceleration to command the throttling of the rate of the oxygen to be passed is added to the output value of an oxygen flow rate program setter 20 by a block 21 for suppressing the abnormal decarburization when the damper 4 attains a full open region upon abnormal progression of the decarburization reaction. A controller 19 for the rate of the oxygen to be passed decelerates the rate of the oxygen to be passed to an oxygen lance 7 by such command and makes this operation stepwise to move the damper 4 in the close direction until the damper is moved to the outside of the full open region. The throttled rate of the oxygen is stepwise restored to the previous rate when the abnormal decarburization settles down. The deceleration restoration deceleration are thus repeated.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、製鉄(製鋼工程)の転炉精錬分野における排
ガス回収制御方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an exhaust gas recovery control method in the field of converter refining in iron manufacturing (steel manufacturing process).

[従来の技術] 転炉精錬においては、純酸素を吹き込むことで、2C+
O,→2GOの脱炭反応により高濃度の可燃ガスを含む
排ガスが発生する。、この排ガスを未燃焼状態で高効率
で回収するために、従来から種々の改善、工夫がなされ
ており、1つの例とじて特開昭58−1011では排ガ
ス回収装置により吹き込み酸素や副原料投入によって生
じる排ガスの増減に応じ、排ガス調整用ダンパーを操作
し排ガス回収を高効率で実現する方法が開示されている
[Conventional technology] In converter refining, 2C+
The decarburization reaction of O,→2GO generates exhaust gas containing a high concentration of combustible gas. In order to recover this exhaust gas in an unburned state with high efficiency, various improvements and devices have been made in the past.One example is JP-A-58-1011, which uses an exhaust gas recovery device to blow oxygen and input auxiliary materials. A method is disclosed in which exhaust gas is recovered with high efficiency by operating an exhaust gas adjustment damper in accordance with the increase or decrease in exhaust gas generated by the exhaust gas.

[発明が解決しようとする問題点] しかし、精錬開始後3〜5分経過すると脱炭反応が急速
に進行し、時には排ガス回収能力以上に排ガスが発生す
る異常脱炭現象が生じる場合がある。このため、回収し
きれないガス量は、回収系外へ溢れ出し排ガス回収率が
低下するという問題点が生じた。特に近年は、生産性向
上のため過酸速度を大幅に上昇させる場合があり、排ガ
スの吹き出しが頻発し、操業トラブルの原因となること
がある。
[Problems to be Solved by the Invention] However, after 3 to 5 minutes have passed after the start of refining, the decarburization reaction rapidly progresses, and sometimes an abnormal decarburization phenomenon occurs in which exhaust gas is generated in excess of the exhaust gas recovery capacity. For this reason, a problem arose in that the amount of gas that could not be recovered overflowed to the outside of the recovery system, reducing the exhaust gas recovery rate. Particularly in recent years, the peracid rate has sometimes been significantly increased to improve productivity, which has resulted in frequent blow-off of exhaust gas, which can cause operational troubles.

[問題点を解決するための手段] 本発明では、異常脱炭により排ガス量が回収能力以上に
発生する場合、排ガス調整用ダンパーは全開領域の状態
にあることに着眼し、排ガス調整用ダンパーが急速に全
開領域に到達した場合、通′酸量を段階的に絞り込み、
2C+02→2COの脱炭反応を抑制していく方法に想
到した。脱炭反応が抑えられ、異常脱炭が鎮静した段階
で絞り込んだ酸素量を再び復量させる事で転炉精錬の主
目的である脱炭および鋼浴昇温への影響を回避している
。又トータル通酸量がほぼ同量なので、精錬時間が従来
より延長して生産能率が低下する不利もない。即ち、本
発明の特徴とするところは、酸素転炉の排ガス回収制御
方法において、排ガス回収調整用ダンパーの全開を感知
することによって異常脱炭の発生を検出し、過酸量を段
階的に絞り込み、異常脱炭が鎮静した段階で絞り込んだ
酸素量を復量させることにある。ここで酸素転炉とは、
主に純酸素を上吹き、あるいは上底吹き、もしくは底吹
きして製鋼精錬する転炉を云う。
[Means for Solving the Problems] The present invention focuses on the fact that when the amount of exhaust gas is generated due to abnormal decarburization than the recovery capacity, the exhaust gas adjustment damper is in a fully open region, and the exhaust gas adjustment damper is If the full-open range is rapidly reached, reduce the amount of acid in stages,
We came up with a method to suppress the decarburization reaction of 2C+02→2CO. By restoring the reduced amount of oxygen once the decarburization reaction has been suppressed and the abnormal decarburization has subsided, the main purpose of converter refining is decarburization and the effect on steel bath temperature rise is avoided. In addition, since the total amount of acid passing is almost the same, there is no disadvantage that the refining time is longer than before and the production efficiency is lowered. That is, the feature of the present invention is that, in the exhaust gas recovery control method for an oxygen converter, the occurrence of abnormal decarburization is detected by sensing the full opening of the exhaust gas recovery adjustment damper, and the amount of superacid is gradually reduced. The aim is to restore the amount of oxygen that has been squeezed out once the abnormal decarburization has subsided. What is an oxygen converter here?
A converter that mainly uses pure oxygen to make and refine steel by top-blowing, top-bottom blowing, or bottom-blowing.

以下本発明の要旨を例示的に解説することにする。排ガ
ス回収調整用ダンパーは、通常の操業においては、0〜
40%に開度調整しているが、排気誘引ファンは通常一
定速度で定格運転していることから全開即ち開度85%
以上の領域に到達したことは吸引能カ一杯の状態を意味
し、転炉からのガス発生量が更に増加傾向を維持すると
当然炉口からの余剰ガス吹き出し現象が生じる。即ち、
ダンパーの全開状態は排ガス回収制御におけるクリイテ
ィカルポイントであり、アクションの起点である。過酸
量の絞り込みは、段階的に実行することを要件とする。
The gist of the present invention will be explained below by way of example. During normal operation, the exhaust gas recovery adjustment damper
The opening is adjusted to 40%, but since the exhaust induction fan normally operates at a constant speed, it is fully open, or 85%.
Reaching the above range means that the suction capacity is full, and if the amount of gas generated from the converter continues to increase further, a phenomenon of excess gas blowing out from the furnace mouth will naturally occur. That is,
The fully open state of the damper is a critical point in exhaust gas recovery control and the starting point of action. It is necessary to narrow down the amount of peracid in stages.

即ち、過酸速度の減速は、吹錬時間や脱炭、昇温に悪影
響を及ぼさない様に。
In other words, the deceleration of the overacid rate should not have a negative effect on the blowing time, decarburization, and temperature rise.

1回あたりの減速指令は例えば200〜300を装入吹
錬では5000 N rn’ / Hrとする。指令を
出して10秒間はダンパーの開度判定を行わない。
The deceleration command per time is, for example, 200 to 300, and 5000 Nrn'/Hr for charging blowing. The damper opening degree is not determined for 10 seconds after issuing the command.

これは、減速操作による効果を待つためである。This is to wait for the effect of the deceleration operation.

10秒後に、再びダンパー開度判定を行う。異常脱炭が
鎮静せず、ダンパー開度が未だ85%以上の領域にあれ
ば、再び前記の減速操作を行う。実績では3回以内の減
速操作で異常脱炭現象は、鎮静化することができる 排ガス回収調整用ダンパー開度が通常の操業域0〜40
%内に到達した時、過酸速度の絞り込みにより吹き込ま
れなかった減速酸素量を再び供給する必要がある。この
増量操作は、絞り込み操作によって若干遅れた脱炭反応
、昇温を回復するためである0通酸速度の増量操作は、
前記の減速分を現状の過酸速度に上載せする形で、減速
操作とは逆の形で、段階的に、1回の操作において20
0〜300を吹錬の場合であれば5000 N rri
’/Hrづつ増量し、減速前のレベルに到達したならば
、減速過酸量に見合う量を更に加算した上で復電操作を
行う。
After 10 seconds, the damper opening degree is determined again. If the abnormal decarburization has not subsided and the damper opening is still in the region of 85% or more, the above-described deceleration operation is performed again. In actual practice, the abnormal decarburization phenomenon can be suppressed by performing deceleration operations within 3 times.
%, it is necessary to supply again the amount of decelerating oxygen that was not blown in due to the restriction of the peracid rate. This volume increase operation is to recover the decarburization reaction and temperature rise that were slightly delayed by the squeezing operation.
By adding the above deceleration amount to the current peracid rate, in a stepwise manner in the opposite manner to the deceleration operation, 20% in one operation.
If blowing from 0 to 300, 5000 Nri
When the amount is increased by '/Hr and reaches the level before deceleration, an amount commensurate with the amount of deceleration superacid is further added, and then the power restoration operation is performed.

復電操作により、異常脱炭を鎮静化するために制御した
減速操作による脱炭、昇温べの影響を回避 −する事が
できる。
By performing power restoration operations, it is possible to avoid the effects of decarburization and temperature rise caused by controlled deceleration operations to suppress abnormal decarburization.

[作用] 以下、本発明について実例に基づき説明する。[Effect] Hereinafter, the present invention will be explained based on actual examples.

第1図は1本発明の転炉排ガス回収制御方法を示す全体
図であり、従来の排ガス回収制御方法に対して、異常脱
炭抑制ブロック21を付加しているところが特徴的なポ
イントである。
FIG. 1 is an overall diagram showing a converter exhaust gas recovery control method according to the present invention, and a characteristic point is that an abnormal decarburization suppression block 21 is added to the conventional exhaust gas recovery control method.

異常脱炭抑制ブロック21の指令は、酸素流量プログラ
ム設定器20の指令に加算されて、過酸量調節計19の
設定信号となっている。
The command from the abnormal decarburization suppression block 21 is added to the command from the oxygen flow rate program setting device 20 to become a setting signal for the superacid amount controller 19.

第2図は、第1図における異常脱炭抑制ブロック21の
詳細図である。
FIG. 2 is a detailed diagram of the abnormal decarburization suppression block 21 in FIG. 1.

以下の説明は、第1図の転炉徘ガス回収制御方法の全体
図に基づき記述されている。転炉精錬の進行により、排
ガス回収制御装置18は1発生排ガスを排ガス誘引ファ
ン12にて回収系内に誘引し、転炉炉口部16でのガス
溢れ出しが生じない様に徐々にダンパー操作器5に対し
て、排ガス調整用ダンパー4を開方向に動作させる指令
を出す。精錬開始後3〜5分経つと、精錬反応形態が脱
炭反応(2G+02→2GO)主体となり、脱炭反応が
頂点に到達する。この際、脱炭反応が異常に進行し約数
分間排ガス回収能力を越える排ガスが発生することがあ
る。本発明は、以下の制御により、この現象を回避する
技術である。この場合、排ガス回収制御装置18は、ダ
ンパー操作器5に対して排ガス調整用ダンパー4の全開
指令を出しており、排ガス調整用ダンパー4が全開領域
に到達した時、異常脱炭抑制ブロック21により酸素流
量プログラム設定器20の出力値に対して1通酸量の絞
り込みを指示するための減速量を加算する。
The following description is based on the general diagram of the converter wandering gas recovery control method shown in FIG. As the converter refining progresses, the exhaust gas recovery control device 18 draws the generated exhaust gas into the recovery system using the exhaust gas induction fan 12, and gradually operates the damper to prevent gas from overflowing at the converter mouth 16. A command is issued to the device 5 to operate the exhaust gas regulating damper 4 in the opening direction. After 3 to 5 minutes have passed after the start of refining, the refining reaction mode becomes mainly a decarburization reaction (2G+02→2GO), and the decarburization reaction reaches its peak. At this time, the decarburization reaction may progress abnormally and generate exhaust gas that exceeds the exhaust gas recovery capacity for several minutes. The present invention is a technique for avoiding this phenomenon through the following control. In this case, the exhaust gas recovery control device 18 issues a command to the damper operating device 5 to fully open the exhaust gas adjustment damper 4, and when the exhaust gas adjustment damper 4 reaches the fully open region, the abnormal decarburization suppression block 21 A deceleration amount is added to the output value of the oxygen flow rate program setting device 20 to instruct narrowing down to one oxygen flow amount.

過酸量調節計19は、この指令により吹き込み酸素ラン
ス7への過酸量を減速する。本制御は、2C+O,→2
COの脱炭反応を抑制するものである。異常脱炭が続き
、前述の操作量だけでは反応を抑制しきれない時は、再
び異常脱炭抑制ブロック21は、同様の指令を発生する
。減速操作を平均2.5回(25秒)実施する事で、先
の異常脱炭を抑え1回収能力以内の排ガス発生量とする
ことが出来る。
The peracid amount controller 19 slows down the amount of peracid supplied to the blown oxygen lance 7 based on this command. This control is 2C+O, →2
This suppresses the decarburization reaction of CO. When the abnormal decarburization continues and the reaction cannot be suppressed by the above-mentioned operation amount alone, the abnormal decarburization suppression block 21 issues a similar command again. By performing the deceleration operation an average of 2.5 times (25 seconds), the previous abnormal decarburization can be suppressed and the amount of exhaust gas generated can be kept within one recovery capacity.

過酸量の低下により、2C十02→2GOの脱炭反応が
急速に抑制されるために、排ガス回収制御装@18は、
ダンパー操作器5に対して排ガス調整用ダンパー4を閉
方向に移動する指令を生じる。
Because the decarburization reaction of 2C102→2GO is rapidly suppressed due to the decrease in the amount of peracid, the exhaust gas recovery control system @18
A command is issued to the damper operating device 5 to move the exhaust gas adjusting damper 4 in the closing direction.

この指令により、排ガス調整用ダンパー4の状態は閉方
向に移動するため、全開領域を外れる。よって、異常脱
炭抑制ブロック21は同ブロック内の過酸量復帰ブロッ
ク第2図−3にて絞り込んだ過酸量の復帰処理を行なう
指令を酸素流量プログラム設定器20の出力側に増速址
を加算し、減速量を相殺する方向に動作する。過酸量調
節計19は、異常脱炭抑制ブロック21からの指令量だ
け吹き込み酸素ランス7からの過酸を復電し、脱炭反応
を再び強める作用を及ぼす。異常脱炭抑制ブロック21
が、排ガス調整用ダンパー4の全開領域を閾値として、
吹き込み酸素ランスの過酸量を減速→復量→減速→復電
させる事で、常に回収能力以内の排ガス回収制御を実施
する事が出来る様に作用する。
Due to this command, the state of the exhaust gas regulating damper 4 moves in the closed direction, so that it is out of the fully open region. Therefore, the abnormal decarburization suppression block 21 sends a command to the output side of the oxygen flow rate program setting device 20 to perform the process of restoring the amount of overacid narrowed down in the overacid amount recovery block in FIG. 2-3. , and operates in the direction of canceling out the amount of deceleration. The peracid amount regulator 19 restores the peracid from the oxygen lance 7 by blowing in the amount commanded from the abnormal decarburization suppression block 21, and has the effect of reinforcing the decarburization reaction. Abnormal decarburization suppression block 21
However, with the fully open area of the exhaust gas adjustment damper 4 as the threshold,
By decelerating the amount of superacid in the blown oxygen lance → reducing the amount → reducing the amount → returning the power, it works so that exhaust gas recovery control can always be performed within the recovery capacity.

[実施例コ 第3図に本発明に基づく排ガス回収制御結果を示す。従
来の排ガス制御では、ダンパー全開領域4に到達し、炉
口からの吹き出し5を生じていたが、本発明によりダン
パー全開領域4への到達と共に過酸量1の段階的絞り込
みを実施するため吹き出し5を生じる事なく排ガス回収
制御を実現できる。
[Example 3] Fig. 3 shows the results of exhaust gas recovery control based on the present invention. In conventional exhaust gas control, when the damper fully open region 4 is reached, a blowout 5 is generated from the furnace mouth, but according to the present invention, when the damper fully open region 4 is reached, the amount of superacid 1 is gradually narrowed down, so that the blowout is Exhaust gas recovery control can be realized without causing 5.

[発明の効果] 本発明による効果を1例に就いて述べると本発明によっ
て転炉排ガスの炉口からの吹出しは回避されることによ
り、転炉排ガス回収原単位は実施前に比して、約2 N
 rn’ / t−611(熱量2000Kcal換算
値)向上しており、相当な効果を達成することができた
。又製鋼時間の延長もなく生産性の低下もなかった。
[Effects of the Invention] To describe the effects of the present invention as an example, since the present invention prevents converter exhaust gas from blowing out from the furnace mouth, the recovery unit of converter exhaust gas is reduced compared to before implementation. Approximately 2 N
rn'/t-611 (heat value converted to 2000 Kcal) was improved, and a considerable effect could be achieved. Furthermore, there was no extension of steelmaking time and no decrease in productivity.

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

第1図は本発明の転炉排ガス回収制御方法をしめす全体
図 第2図は第1図における異常脱炭制御ブロック21の詳
細図 第3図は本発明の排ガス制御法を従来法と対比して示す
図である
Fig. 1 is an overall diagram showing the converter exhaust gas recovery control method of the present invention. Fig. 2 is a detailed diagram of the abnormal decarburization control block 21 in Fig. 1. Fig. 3 is a comparison of the exhaust gas control method of the present invention with the conventional method. This is a diagram showing

Claims (1)

【特許請求の範囲】[Claims] 酸素転炉の排ガス回収制御方法において、排ガス回収調
整用ダンパーの全開を感知することによって異常脱炭の
発生を検出し、通酸量を段階的に絞り込み、異常脱炭が
鎮静した段階で絞り込んだ酸素量を復量させることを特
徴とする転炉排ガス回収制御方法。
In the exhaust gas recovery control method for oxygen converters, the occurrence of abnormal decarburization is detected by sensing when the damper for exhaust gas recovery adjustment is fully opened, and the amount of oxidation is reduced in stages, until the abnormal decarburization has subsided. A converter exhaust gas recovery control method characterized by restoring the amount of oxygen.
JP21024285A 1985-09-25 1985-09-25 Method for controlling recovering of waste gas from converter Granted JPS6270508A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21024285A JPS6270508A (en) 1985-09-25 1985-09-25 Method for controlling recovering of waste gas from converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21024285A JPS6270508A (en) 1985-09-25 1985-09-25 Method for controlling recovering of waste gas from converter

Publications (2)

Publication Number Publication Date
JPS6270508A true JPS6270508A (en) 1987-04-01
JPS6332844B2 JPS6332844B2 (en) 1988-07-01

Family

ID=16586136

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21024285A Granted JPS6270508A (en) 1985-09-25 1985-09-25 Method for controlling recovering of waste gas from converter

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JP (1) JPS6270508A (en)

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Publication number Publication date
JPS6332844B2 (en) 1988-07-01

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