JPS6119720A - Operation of hermetically closed-type converter exhaust gas treatment apparatus - Google Patents

Operation of hermetically closed-type converter exhaust gas treatment apparatus

Info

Publication number
JPS6119720A
JPS6119720A JP14028384A JP14028384A JPS6119720A JP S6119720 A JPS6119720 A JP S6119720A JP 14028384 A JP14028384 A JP 14028384A JP 14028384 A JP14028384 A JP 14028384A JP S6119720 A JPS6119720 A JP S6119720A
Authority
JP
Japan
Prior art keywords
gas
exhaust gas
air
amount
blowing
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
JP14028384A
Other languages
Japanese (ja)
Other versions
JPS6220251B2 (en
Inventor
Seiji Ogata
緒方 征二
Shoichi Osada
長田 昭一
Motoaki Hirao
平尾 元亮
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.)
Kawasaki Heavy Industries Ltd
Nippon Steel Corp
Kawasaki Motors Ltd
Original Assignee
Kawasaki Heavy Industries Ltd
Nippon Steel Corp
Kawasaki Jukogyo KK
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 Kawasaki Heavy Industries Ltd, Nippon Steel Corp, Kawasaki Jukogyo KK filed Critical Kawasaki Heavy Industries Ltd
Priority to JP14028384A priority Critical patent/JPS6119720A/en
Publication of JPS6119720A publication Critical patent/JPS6119720A/en
Publication of JPS6220251B2 publication Critical patent/JPS6220251B2/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

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 enhance safety against explosion by sufficiently forming an inert gas layer, by adjusting the components of exhaust gas by blowing air in a converter after blowing-in was started and stopping the blowing-in of air when said gas reaches a definite amount. CONSTITUTION:When CO gas is generated from a converter after the beginning of blowing-in, the amount of air to be blown in is adjusted by the damper 13' of an air blow-in apparatus 12 on the basis of the signal of an exhaust gas analysis terminal 14 so as to obtain a predetermined exhaust gas composition such that O2-concn. is 5.5% or less and CO-concn. is 12.5% or less. The blowing- in amount of air is increased with the increase in the amount of the gas generated from the converter 1 and the O2 or CO- concn. in exhaust gas is controlled to a predetermined composition. The exhaust gas amount of an inert gas state, wherein O2 in the exhaust gas is 5.5% or less and CO therein is 12.5% or less, is measured and integrated by an exhaust gas flow meter 17 and, when the integrated amount reaches a predetermined one, a damper 13 is completely closed to stop the blowing-in of air and the treatment of the exhaust gas is brought to a hermetically closed state. By this method, the recovery of high purity CO gas can be performed.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、安全性を向上すると共に純度の高いCOガス
の回収を可能くした密閉又は密閉に近い状態で運転され
る密閉型転炉排ガス処理装置の操業方法に関する。
Detailed Description of the Invention (Industrial Application Field) The present invention is directed to a closed converter exhaust gas system that is operated in a hermetically sealed or nearly hermetic state, which improves safety and makes it possible to recover CO gas with high purity. It relates to a method of operating a processing device.

(従来技術とその問題点) 溶銑を収容した転炉内に、純酸素を吹込んで(以下吹錬
という)精錬する際に、大量のCOガスが発生する。こ
のCOガスは、外気と接触すると爆発の危険がある。又
外部に漏れると一酸化炭素中毒を起すので危険である。
(Prior art and its problems) A large amount of CO gas is generated during refining by blowing pure oxygen into a converter containing hot metal (hereinafter referred to as blowing). This CO gas poses a risk of explosion if it comes into contact with outside air. Also, if it leaks outside, it is dangerous as it can cause carbon monoxide poisoning.

このように転炉から発生する危険なガス唸、排ガス処理
装置によシ安全に処理するよ5Kしている。
5K is working to safely dispose of the dangerous gases generated from the converter using exhaust gas treatment equipment.

先ず転炉排ガス処理装置とその操業方法の概要を第1図
を用いて説明する。図において、図示省略の高炉で生産
された溶銑は、転炉1内に注入され、スカート2によシ
シールされる。この状態で、酸素ランス11よシ純酸素
を転炉1内に吹込み、吹錬が開始される。かくして溶銑
中の炭素と吹込まれた酸素とか反応して脱炭され、良質
の鋼ができる。この脱炭反応によって大量のCOガスが
発生する。
First, an overview of the converter exhaust gas treatment device and its operating method will be explained using FIG. In the figure, hot metal produced in a blast furnace (not shown) is injected into a converter 1 and sealed by a skirt 2. In this state, pure oxygen is blown into the converter 1 through the oxygen lance 11, and blowing is started. In this way, the carbon in the hot metal reacts with the injected oxygen and decarburizes, producing high-quality steel. This decarburization reaction generates a large amount of CO gas.

このCOガス社、誘引送風機7によって7−ド3内に誘
引され、7−ド3及び冷却器4内で冷却され、次いで除
塵量5,6にて除塵され、有価ガスとして、ガスホルダ
IOK回収すれる。
This CO gas is drawn into the 7-door 3 by the induced blower 7, cooled in the 7-door 3 and the cooler 4, and then removed with dust removal amounts 5 and 6, and recovered as valuable gas in the gas holder IOK. Ru.

この転炉排ガス処理装置において、転炉操業は次のよう
にして行われている。吹錬開始*a、7−ド3から切換
ダンパ9に至る間には空気が滞溜している。この空気と
吹錬によシ発生したCOガスとが接触すると爆発する危
険がある。
In this converter exhaust gas treatment device, the converter operation is performed as follows. Start of blowing*a, 7-Air is accumulated between the door 3 and the switching damper 9. If this air comes into contact with the CO gas generated during blowing, there is a danger of an explosion.

そこで、この爆発を避けるために、吹錬初期のCa2度
の低いガス祉、炉口とスカート2との間の隙間から外気
を吸引してCOガスを燃焼することにより02濃度5.
5−以下CO濃度12.5−以下てN2ガスとCO2ガ
スを主成分とするガス層を生成し、装置内に滞溜してい
る空気と吹錬最盛期に発生するCOガスとの間に上記の
ガス層を介在して、空気とCOガスとの接触を防止し、
爆発を防止するようにしている。又吹錬末期においても
同様に、スカート2と炉口との間から外気を吸引して前
述のガス層を生成し、吹錬終了時に侵入してくる外気と
の接触を防止している。
Therefore, in order to avoid this explosion, the CO gas is combusted by sucking the outside air through the gap between the furnace mouth and the skirt 2 and burning the CO gas at a low Ca2 concentration in the early stage of blowing.
5- or less CO concentration is 12.5- or less, a gas layer mainly composed of N2 gas and CO2 gas is generated between the air stagnant in the equipment and the CO gas generated at the peak of blowing. Preventing contact between air and CO gas through the above gas layer,
Trying to prevent explosions. Also, at the end of blowing, outside air is similarly sucked in between the skirt 2 and the furnace mouth to generate the above-mentioned gas layer, thereby preventing contact with outside air that enters at the end of blowing.

即ち、吹錬最盛期のCO濃度の高いCOガスは、吹錬の
初期と末期に燃焼して生成された02濃度5.5 %以
下CO濃度12.5−以下テN、ガスとCO2ガスを主
成分とするガスに狭まれた状態で外気と遮断され、(こ
の0□11度5.5%以下、CO員変度125%以下で
N2ガスとCO2ガスを主成分とするガスを以下イナー
トガス層という)安全に回収される。なお、このイナー
トガス層は、切換ダンパ9によシ、放散塔8より大気中
に放散される。
In other words, CO gas with a high CO concentration at the peak of blowing has a CO concentration of 5.5% or less and a CO concentration of 12.5% or less produced by combustion at the beginning and end of blowing. Inert gas is a gas whose main components are N2 gas and CO2 gas, which are separated from the outside air in a state where the main components are 0□11 degrees and 5.5% or less, and CO2 gas is 125% or less. layer) is safely recovered. Note that this inert gas layer is dissipated into the atmosphere by the switching damper 9 and from the dispersion tower 8.

上記の転炉操業において、最近では、回収ガスの品位向
上、回収ガスの原単位の向上の為、転炉とスカート間の
間を密閉又は密閉に近い状態にして外気の侵入を防止し
高純度のCOガスの回収が望まれるようになってきた。
In the converter operation mentioned above, recently, in order to improve the quality of recovered gas and the basic unit of recovered gas, the space between the converter and the skirt is sealed or close to sealed to prevent outside air from entering, resulting in high purity. Recovery of CO gas has become desirable.

このように、転炉炉口とスカートとの間の隙間を密閉又
は密閉に近い状態にするいわゆる密閉型の転炉排ガス処
理装置では、外気の侵入がないかあっても僅かなために
充分なイナートガス層が生成されないという問題がある
In this way, in the so-called closed type converter exhaust gas treatment equipment in which the gap between the converter mouth and the skirt is sealed or close to sealed, there is no or very little intrusion of outside air, so it is not enough. There is a problem that an inert gas layer is not generated.

現在性なわれている密閉型の転炉排ガス処理装置の操業
方法としては、吹錬の初期と末期においてスカートを上
昇させ、転炉炉口とスカートとの間に隙間をもたせてこ
こから外気を吸引し、イナート層を生成するようにして
いる。
The current method of operating closed-type converter exhaust gas treatment equipment is to raise the skirt at the beginning and end of blowing, and create a gap between the converter mouth and the skirt to draw outside air from here. It is designed to generate an inert layer by suction.

然し乍ら、吹錬の初期と末期にスカートを上昇させて、
外気を吸引するのは、結局従前の排ガス処理装置と変ら
ず、密閉型の転炉排ガス処理装置にした効果が期待でき
ず、高純度のcOガスの回収ができないという問題があ
る。
However, the skirt is raised at the beginning and end of the blowing process,
In the end, the suction of outside air is no different from the conventional exhaust gas treatment equipment, and there is a problem in that the effects of using a closed converter exhaust gas treatment equipment cannot be expected, and high purity cO gas cannot be recovered.

(発明の目的) 本発明は、この問題を解決するためになされCOガスの
回収を可能にした密閉型転炉排ガス処理装置の操業方法
を提供するととを目的とする本のである◇ (発明の構成) 本発明は、従来のようにスカートを上昇して炉口とスカ
ートとの間から外気を吸引すみのではなく、空気吹込装
置を設けて行うようにしたものであシ、炉口部を密閉又
社書閉に近い状態にした状態で炉内圧力を調整しながら
上記空気吹込装置から吹込まれる空気量を調整して排ガ
ス中のCOが12.51以下0□が5.5−以下の予め
定められた排ガス組成になるようにガス成分を調整し、
同時に上記成分のガス流量を測定し、このガス量が一定
量に達したときに空気吹込装置からの空気の吹込を停、
止することを特徴とする。
(Purpose of the Invention) The present invention is a book that aims to solve this problem and provide a method for operating a closed converter exhaust gas treatment device that makes it possible to recover CO gas. Structure) The present invention does not raise the skirt and draw in outside air from between the furnace mouth and the skirt as in the past, but instead installs an air blowing device. With the furnace closed or close to closed, adjust the pressure inside the furnace and adjust the amount of air blown in from the air blowing device to ensure that the CO in the exhaust gas is 12.51 or less and 0□ is 5.5 or less. Adjust the gas components to a predetermined exhaust gas composition,
At the same time, the gas flow rate of the above components is measured, and when this gas amount reaches a certain amount, the air blowing device stops blowing air.
It is characterized by stopping.

(実施例) 本発明の一実施例について詳細に説明する。(Example) An embodiment of the present invention will be described in detail.

第2図において、転炉1から発生したCOガスは、置引
送風機7によって7−ド3内に誘引され、7−ド3及び
冷却器4にて冷却された後除塵器5,6で除塵され、ガ
スホルダ10に回収される。
In Fig. 2, CO gas generated from the converter 1 is drawn into the 7-door 3 by the air blower 7, cooled by the 7-door 3 and cooler 4, and then removed by dust removers 5 and 6. and collected in the gas holder 10.

なお2はスカート、8は放散塔、9紘切換弁である。1
2は、転炉1の炉口になるべく近い位置に設けられた空
気吹込装置であり、2個のダンパ13,13′が設けら
れている。17はガス流量計である。
Note that 2 is a skirt, 8 is a diffusion tower, and 9 is a flow switching valve. 1
Reference numeral 2 denotes an air blowing device provided as close as possible to the furnace mouth of the converter 1, and is provided with two dampers 13, 13'. 17 is a gas flow meter.

この密閉型の転炉紳ガス処理装置において、吹錬の初期
と末期には、空気吹込装置12のダンパ13,13′が
開かれる。このダンパ13 、13’の開度調整は、次
のようにして行なわれる。
In this closed type converter gas treatment apparatus, the dampers 13 and 13' of the air blowing apparatus 12 are opened at the beginning and end of blowing. The opening degree adjustment of the dampers 13 and 13' is performed as follows.

先ず、ダンパ13は、ガス流量計17の信号15により
調整される。即ち、吹錬の初期と末期において、イナー
トガスが生成されるまでは、ダンパ13は全開になる。
First, the damper 13 is adjusted by the signal 15 of the gas flow meter 17. That is, at the beginning and end of blowing, the damper 13 is fully opened until inert gas is generated.

従って空気吹込装置12から吹込まれる空気量は、ダン
パ13により調整される。このダンパ13′の開度調整
は、ガス成分(COh 02 )検出端14からの信号
によシ行われる。
Therefore, the amount of air blown from the air blowing device 12 is adjusted by the damper 13. The opening degree adjustment of the damper 13' is performed by a signal from the gas component (COh 02 ) detection end 14.

即ち、吹錬の初期と末期に発生するCO濃度ガスの生成
される量は、供給される空気量と転炉発生ガス量により
変る。ガス成分検出端14によりガス成分を検出し、爆
発を起さないCO成分12.5 %以下と02成分5.
5−以下の予め定められた排ガス組成になるように、ダ
ンパ13′の開度が調節され、COと02の濃度が所定
の値以下になるいわゆるイナートガスの生成を行う。
That is, the amount of CO concentration gas generated at the beginning and end of blowing varies depending on the amount of air supplied and the amount of gas generated in the converter. The gas component is detected by the gas component detection end 14, and the CO component that does not cause an explosion is 12.5% or less and the 02 component 5.
The opening degree of the damper 13' is adjusted so that the exhaust gas composition becomes a predetermined value of 5- or less, and so-called inert gas is generated in which the concentration of CO and 02 becomes less than a predetermined value.

このようにイナートガスが生成され、そのイナートガス
の流量をガス流量計17により計測し充分な量に達した
ときダンパ13を全閉にし、排ガス処理装置は、完全に
密閉された状態になる。
Inert gas is generated in this way, and the flow rate of the inert gas is measured by the gas flow meter 17, and when a sufficient amount is reached, the damper 13 is fully closed, and the exhaust gas treatment device becomes completely sealed.

この操業方法を第3図を用いて更に詳しく説明する。第
3図は、吹錬初期について示したものである。
This operating method will be explained in more detail using FIG. FIG. 3 shows the initial stage of blowing.

即ち吹錬直前の状態から操業に移る状態を示す。図にお
いて、吹錬の直前で社、スカート2によシ転炉1の炉口
が密閉又は密閉に近い状態で、空気吹込装置12よシ空
気が吹込まれている。従って排ガス量としては、吹込ま
れた空気量になる。
In other words, it shows the state of transition from the state immediately before blowing to operation. In the figure, just before blowing, air is blown into the converter 1 through the skirt 2 through the air blowing device 12 while the furnace opening of the converter 1 is closed or close to closed. Therefore, the amount of exhaust gas is the amount of air blown into it.

次に吹錬が開始され、転炉からCOO20発生しだすと
排ガス分析端14の信号によシ、排ガス中の02濃度は
5.5チ以下、CO濃度は12.5チ以下の予め定めら
れた排ガス組成になる様にダンパ13’により吹込空気
量が調整される。吹錬開始直後においては転炉からの発
生COガス量が少ないため吹込空気量は一旦減少するが
、転炉からの発生ガス量の増加に伴ない吹込空気量は増
加し、排ガス中の02又はCO濃度は予め定められた組
成にコントロールされる。この排カスノ組成カ025.
5ts以下、CO12,5%以下の範囲内にあるいわゆ
るイナートガスの状態の排ガス量は排ガス流量計17に
よシ計測・積算され、その積算量が予め定められた量に
達した時ダンパ13を全閉にして空気吹込が停止され排
ガス処理装置は完全に密閉された状態又は密閉に近い状
態となる。
Next, blowing is started, and when COO20 begins to be generated from the converter, a signal from the exhaust gas analysis terminal 14 indicates that the 02 concentration in the exhaust gas is 5.5 inches or less, and the CO concentration is 12.5 inches or less. The amount of air blown is adjusted by the damper 13' so that the composition of the exhaust gas is achieved. Immediately after the start of blowing, the amount of CO gas generated from the converter is small, so the amount of blown air temporarily decreases, but as the amount of gas generated from the converter increases, the amount of blown air increases, and the amount of CO gas in the exhaust gas increases. The CO concentration is controlled to a predetermined composition. The composition of this waste gas is 025.
The amount of exhaust gas in the so-called inert gas state, which is within the range of 5ts or less and CO12.5% or less, is measured and integrated by the exhaust gas flow meter 17, and when the integrated amount reaches a predetermined amount, the damper 13 is When it is closed, air blowing is stopped and the exhaust gas treatment device becomes completely sealed or nearly sealed.

従ってこの時の排ガス組成は純度の高いCOとなり、排
ガス量は転炉発生ガス量に等しいガス量となる。
Therefore, the composition of the exhaust gas at this time is CO with high purity, and the amount of exhaust gas is equal to the amount of gas generated in the converter.

(発明の効果) 以上詳述した通り本発明による密閉型転炉排ガス処理装
置の操業方法は、転炉排ガス処理装置に空気吹込装置を
設け、吹錬の初期と末期において、COと02の濃度に
よって空気吹込装置からの空気吹込量を調整しイナート
ガス(C02ガス)を確実に生成すると共に、このイナ
ートガスの量が充分に生成されたことを確認した上で、
空気の吹込みを停止するようにしたので、排ガス処理装
置を完全に管間した状態でイナートガス層を確実に生成
して安全性を保障することができると共に、高純度のC
OO20回収が可能になシ、COO20有価ガスとして
の価値を大巾に向上することができるという産業上優れ
た効果を有する。
(Effects of the Invention) As detailed above, the operating method of the closed type converter exhaust gas treatment device according to the present invention is such that the converter exhaust gas treatment device is provided with an air blowing device, and the concentration of CO and 02 is controlled at the initial and final stages of blowing. After adjusting the amount of air blown from the air blowing device to reliably generate inert gas (C02 gas) and confirming that a sufficient amount of this inert gas has been generated,
Since the air blowing is stopped, it is possible to reliably generate an inert gas layer with the exhaust gas treatment device completely connected between the pipes, ensuring safety, and also to ensure safety.
It has an industrially excellent effect in that it is possible to recover OO20 and greatly improve the value of COO20 as a valuable gas.

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

第1図は転炉排ガス処理装置の概略図、第2図及び第3
図は本発明の一実施例であシ、第2図は本発明の操業方
法を実施するための転炉排ガス処理装置を示す概略構成
図、第3図は操業に際しての排ガスの組成、排ガス量、
空気吹込量、転炉発生ガス量の関係を示す線図である。 1・・・転炉  2・・・スカート  7・・・誘引送
風機  12・・・空気吹込装置  14・・・ガス分
析検出端  15・・・流量検出端17・・・ガス流量
Figure 1 is a schematic diagram of the converter exhaust gas treatment equipment, Figures 2 and 3
The figure shows one embodiment of the present invention. Figure 2 is a schematic configuration diagram showing a converter exhaust gas treatment equipment for carrying out the operating method of the present invention. Figure 3 shows the composition and amount of exhaust gas during operation. ,
FIG. 2 is a diagram showing the relationship between the amount of air blown and the amount of gas generated in the converter. 1... Converter 2... Skirt 7... Induced blower 12... Air blowing device 14... Gas analysis detection end 15... Flow rate detection end 17... Gas flow meter

Claims (1)

【特許請求の範囲】[Claims] 転炉排ガス処理装置の炉口近くに空気吹込装置を備えた
転炉排ガス処理装置において、炉口部を密閉又は密閉に
近い状態にした状態で炉内圧力を調整しながら、上記空
気吹込装置から吹込まれる空気量を調整して排ガス中の
COが12.5%以下O_2が5.5%以下の予め定め
られた排ガス組成となるようにガス成分を調整し、同時
に上記成分のガス流量を測定し、このガスが一定量に達
したときに空気吹込装置からの空気の吹込を停止するこ
とを特徴とする密閉型転炉排ガス処理装置の操業方法。
In a converter exhaust gas treatment device equipped with an air blowing device near the furnace mouth of the converter flue gas treatment device, while adjusting the pressure inside the furnace with the furnace mouth in a sealed or nearly sealed state, from the air blowing device. By adjusting the amount of air blown in, the gas components are adjusted so that CO in the exhaust gas becomes a predetermined composition of 12.5% or less and O_2 is 5.5% or less, and at the same time the gas flow rate of the above components is adjusted. 1. A method for operating a closed converter exhaust gas treatment device, which comprises measuring the amount of gas and stopping blowing air from an air blowing device when this gas reaches a certain amount.
JP14028384A 1984-07-06 1984-07-06 Operation of hermetically closed-type converter exhaust gas treatment apparatus Granted JPS6119720A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14028384A JPS6119720A (en) 1984-07-06 1984-07-06 Operation of hermetically closed-type converter exhaust gas treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14028384A JPS6119720A (en) 1984-07-06 1984-07-06 Operation of hermetically closed-type converter exhaust gas treatment apparatus

Publications (2)

Publication Number Publication Date
JPS6119720A true JPS6119720A (en) 1986-01-28
JPS6220251B2 JPS6220251B2 (en) 1987-05-06

Family

ID=15265172

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14028384A Granted JPS6119720A (en) 1984-07-06 1984-07-06 Operation of hermetically closed-type converter exhaust gas treatment apparatus

Country Status (1)

Country Link
JP (1) JPS6119720A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014169483A (en) * 2013-03-04 2014-09-18 Nippon Steel & Sumitomo Metal Method for recovering converter exhaust gas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014169483A (en) * 2013-03-04 2014-09-18 Nippon Steel & Sumitomo Metal Method for recovering converter exhaust gas

Also Published As

Publication number Publication date
JPS6220251B2 (en) 1987-05-06

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