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JPS6157368B2 - - Google Patents
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JPS6157368B2 - - Google Patents

Info

Publication number
JPS6157368B2
JPS6157368B2 JP249079A JP249079A JPS6157368B2 JP S6157368 B2 JPS6157368 B2 JP S6157368B2 JP 249079 A JP249079 A JP 249079A JP 249079 A JP249079 A JP 249079A JP S6157368 B2 JPS6157368 B2 JP S6157368B2
Authority
JP
Japan
Prior art keywords
gas
exhaust gas
converter
cooler
composition
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.)
Expired
Application number
JP249079A
Other languages
Japanese (ja)
Other versions
JPS5594429A (en
Inventor
Takahiro Yasuda
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
Original Assignee
Kawasaki Heavy 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP249079A priority Critical patent/JPS5594429A/en
Publication of JPS5594429A publication Critical patent/JPS5594429A/en
Publication of JPS6157368B2 publication Critical patent/JPS6157368B2/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)

Description

【発明の詳細な説明】 本発明は、転炉等から発生するガスを非燃焼の
まゝ処理する排ガス処理装置の爆発防止装置に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an explosion prevention device for an exhaust gas treatment device that processes gas generated from a converter or the like in a non-combustible manner.

従来、係る排ガス処理装置は、冷却器で熱を回
収して排ガスを冷却した後、湿式の集塵器で除塵
し、煙突から放散或は有価ガスとして回収してい
た。又、排ガス処理装置の爆発対策として、吹錬
の開始時間を基準として吹錬の初期及び末期に対
して、排ガス処理装置内に滞留している空気に換
え不活性ガス層を生成し、防爆積層構造を形成し
ていた。
Conventionally, such an exhaust gas treatment device recovers heat with a cooler to cool the exhaust gas, removes dust with a wet dust collector, and releases the exhaust gas from a chimney or recovers it as a valuable gas. In addition, as a countermeasure against explosions in exhaust gas treatment equipment, at the beginning and end of blowing based on the start time of blowing, the air stagnant in the exhaust gas treatment equipment is replaced with an inert gas layer to create an explosion-proof laminated layer. formed a structure.

このように従来では着火源をもたない湿式集塵
器を採用していたので、単なる一律的なシーケン
ス制御による不活性ガスへの置換だけで充分であ
つた。
In this way, conventionally, a wet type precipitator without an ignition source was used, so simply replacing the dust with an inert gas through uniform sequence control was sufficient.

然るに省エネルギーに対処するため、現在では
通気抵抗の大きい湿式集塵器に代え、通気抵抗の
少い電気集塵器が採用されるようになり、誘引送
風機の消費電力を極力節減するようにしている。
However, in order to save energy, electric precipitators with low ventilation resistance are now being used instead of wet type precipitators with high ventilation resistance, and the power consumption of induced blowers is reduced as much as possible. .

この電気集塵器は、湿式集塵器とは違つて排ガ
スへの着火源となり、従来のようなタイマーによ
る一律的な不活性ガスへの置換だけでは爆発の危
険を回避することができず、排ガスの組成によつ
て爆発の危険が伴うので、そのような対策が必要
となつてくる。
Unlike wet precipitators, this electrostatic precipitator is a source of ignition for the exhaust gas, and the risk of explosion cannot be avoided simply by uniformly replacing the gas with inert gas using a conventional timer. Since there is a risk of explosion depending on the composition of the exhaust gas, such measures are necessary.

本発明は、こうした現状に鑑みなされたもので
ある。即ち本発明は、すでに本発明者によつて提
案されている高速ガスサンプリング装置(特願昭
53〜118891号)を採用することによつて、ガスの
組成を3〜4秒で検知して発信し、ガスの組成が
爆発の危険域に達する前に、前記信号によつて冷
却器以降の装置内に水を噴出させて着火源を完全
になくすと共に、不活性ガスを噴出し、ガスを希
釈しながら滞留ガスを排出するようにしたことを
特徴とする。
The present invention has been made in view of these current circumstances. That is, the present invention is based on a high-speed gas sampling device (patent application
53-118891), the composition of the gas is detected and transmitted in 3 to 4 seconds, and the signal is used to alert the cooler and subsequent components before the gas composition reaches the explosive danger zone. The device is characterized in that water is ejected into the device to completely eliminate ignition sources, and inert gas is ejected to dilute the gas while discharging the accumulated gas.

以下、その詳細を実施例により説明する。図に
おいて、1は転炉でその上方に冷却器2が設けら
れている。この冷却器2には第1集塵器5が接続
され、更にガス導路14によつて第2集塵器6が
接続されている。7は誘引送風機でガス導路15
によつて第2集塵器6に接続され、その吐出側は
ダンパー8によつて煙突9と回収系10に排ガス
を切換えて導くようになつている。16はガス導
路で、11は高速ガスサンプリング装置で冷却器
2に取付けられている。12の水噴出用弁、13
は不活性ガス噴出用弁で、この12及び13の弁
は高速ガスサンプリング装置11からの信号で作
動する。17は水タンクで、水噴出用弁12に配
管で接続されている。18は不活性ガス配管、1
9は水配管であり、これら18,19の配管は冷
却器2以降の排ガス処理装置の任意箇所に接続さ
れている。尚3はランス、4は副原料投入装置で
ある。
The details will be explained below using examples. In the figure, 1 is a converter furnace, and a cooler 2 is provided above it. A first dust collector 5 is connected to the cooler 2, and a second dust collector 6 is further connected to the cooler 2 through a gas conduit 14. 7 is an induced blower and gas guide line 15
It is connected to a second precipitator 6 by a damper 8 on its discharge side, and the exhaust gas is switched and guided to a chimney 9 and a recovery system 10 by a damper 8. 16 is a gas conduit, and 11 is a high speed gas sampling device attached to the cooler 2. 12 water spout valves, 13
is a valve for blowing out inert gas, and these valves 12 and 13 are operated by a signal from the high speed gas sampling device 11. 17 is a water tank, which is connected to the water jetting valve 12 through piping. 18 is an inert gas pipe, 1
9 is a water pipe, and these pipes 18 and 19 are connected to any part of the exhaust gas treatment device after the cooler 2. Note that 3 is a lance, and 4 is an auxiliary raw material input device.

上述した構成からなる本実施例において、転炉
1で発生したガスは、誘引送風機7によつて誘引
され、まず冷却器2で熱回収されて冷却され、第
1集塵器5及び第2集塵器6で除塵された後、煙
突9から放散又は弁8の切換えによつて回収系1
0を経て回収される。
In this embodiment having the above-described configuration, the gas generated in the converter 1 is attracted by the induced blower 7, and first the heat is recovered and cooled by the cooler 2. After the dust is removed by the dust collector 6, it is released from the chimney 9 or by switching the valve 8 to the recovery system 1.
It is collected after passing through 0.

このようにして転炉1で発生した排ガスは冷却
除塵されて処理されるのであるが、吹錬の初期、
最盛期及び末期、或はランス3から吹込まれる酸
素、副原料投入装置4から投入される副原料など
転炉1内での反応の状態によりガス組成が変化す
る。このガス組成の変化を高速ガスサンプリング
装置11で連続して分析する。かくしてその分析
値が例えばO2濃度が(5%)になつて爆発の危
険な状態に至つた際、直ちに水噴出用弁12と不
活性ガス噴出用弁13に開の信号を入力し、水噴
出によつて着火源を消滅せしめると同時に、不活
性ガスによつてCO濃度を下げ(希釈)しなが
ら、排ガス装置内を局部的に不活性ガスで置換す
る。そこでガス組成が正常に戻つて爆発の危険が
なくなつた時、高速ガスサンプリング装置からの
信号は解除され、水噴出用弁12及び不活性ガス
噴出用弁13は閉となる。
In this way, the exhaust gas generated in the converter 1 is cooled, dedusted, and treated.
The gas composition changes depending on the reaction state in the converter 1, such as the peak period and the final stage, or the oxygen blown in from the lance 3 and the auxiliary raw material charged from the auxiliary raw material input device 4. This change in gas composition is continuously analyzed by a high-speed gas sampling device 11. In this way, when the analysis value reaches, for example, the O 2 concentration (5%) and reaches a dangerous situation of explosion, an open signal is immediately input to the water spouting valve 12 and the inert gas spouting valve 13, and the water is turned off. The ignition source is extinguished by the ejection, and at the same time, the CO concentration is lowered (diluted) by the inert gas, and the inside of the exhaust gas device is locally replaced with inert gas. When the gas composition returns to normal and there is no danger of explosion, the signal from the high speed gas sampling device is released and the water jetting valve 12 and the inert gas jetting valve 13 are closed.

以上詳述した通り本発明によれば、高速ガスサ
ンプリング装置により連続的にガスの組成を分析
し、ガス組成が爆発の危険性を呈する状態に達し
た際、排ガス処理装置内に水を噴出せしめて着火
源を消滅させると同時に、不活性ガスによつてガ
ス組成を変え、爆発に対して安定したガスにする
ようにしたので、電気集塵器のような着火源とな
る集塵器を採用したとしても、いかなるガス組成
変化に対しても爆発の危険を急速的確に防止する
ことができる等卓越した効果を奏するものであ
る。
As detailed above, according to the present invention, the composition of the gas is continuously analyzed using a high-speed gas sampling device, and when the gas composition reaches a state where there is a danger of explosion, water is spouted into the exhaust gas treatment device. At the same time, we used inert gas to extinguish the ignition source, and at the same time changed the gas composition with an inert gas to make the gas stable against explosions. Even if this method is adopted, it has excellent effects such as being able to quickly and accurately prevent the risk of explosion regardless of any change in gas composition.

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

第1図は本発明の実施例で、簡略化して示した
説明用図である。 11……高速サンプリング装置、12……水噴
出用弁、13……不活性ガス噴出用弁、17……
水タンク。
FIG. 1 is a simplified explanatory diagram showing an embodiment of the present invention. 11...High-speed sampling device, 12...Water jetting valve, 13...Inert gas jetting valve, 17...
water tank.

Claims (1)

【特許請求の範囲】[Claims] 1 転炉等から発生するガスを非燃焼のまま冷却
した後除塵して排出又は回収する排ガス処理装置
において、転炉等から発生するガスの集塵器入口
の排ガスの組成を検知する高速ガスサンプリング
装置と、冷却器以降の任意個所に設けられ前記高
速サンプリング装置からの信号により作動する水
噴出用弁及び不活性ガス噴出用弁とから成る転炉
非燃焼式排ガス処理装置の爆発防止装置。
1. High-speed gas sampling that detects the composition of the exhaust gas at the inlet of the dust collector of the gas generated from the converter, etc., in an exhaust gas treatment device that cools the gas generated from the converter, etc. in an unburned state, removes dust, and then discharges or collects the gas. 1. An explosion prevention device for a converter non-combustion type exhaust gas treatment device, comprising a water jetting valve and an inert gas jetting valve, which are provided at any location after the cooler and are operated by a signal from the high-speed sampling device.
JP249079A 1979-01-10 1979-01-10 Explosion preventing device of converter non-combustion type exhaust gas treating apparatus Granted JPS5594429A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP249079A JPS5594429A (en) 1979-01-10 1979-01-10 Explosion preventing device of converter non-combustion type exhaust gas treating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP249079A JPS5594429A (en) 1979-01-10 1979-01-10 Explosion preventing device of converter non-combustion type exhaust gas treating apparatus

Publications (2)

Publication Number Publication Date
JPS5594429A JPS5594429A (en) 1980-07-17
JPS6157368B2 true JPS6157368B2 (en) 1986-12-06

Family

ID=11530794

Family Applications (1)

Application Number Title Priority Date Filing Date
JP249079A Granted JPS5594429A (en) 1979-01-10 1979-01-10 Explosion preventing device of converter non-combustion type exhaust gas treating apparatus

Country Status (1)

Country Link
JP (1) JPS5594429A (en)

Also Published As

Publication number Publication date
JPS5594429A (en) 1980-07-17

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