JPH01127645A - Method for treating closed type alloy electric furnace equipment at stopping power - Google Patents

Method for treating closed type alloy electric furnace equipment at stopping power

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Publication number
JPH01127645A
JPH01127645A JP28463587A JP28463587A JPH01127645A JP H01127645 A JPH01127645 A JP H01127645A JP 28463587 A JP28463587 A JP 28463587A JP 28463587 A JP28463587 A JP 28463587A JP H01127645 A JPH01127645 A JP H01127645A
Authority
JP
Japan
Prior art keywords
gas
electric furnace
cooling
exhaust gas
equipment
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
JP28463587A
Other languages
Japanese (ja)
Inventor
Yukiyoshi Kurita
栗田 幸善
Shinjiro Takeuchi
竹内 伸二郎
Yoshio Ono
小野 善男
Masao Morimoto
森本 政夫
Shinichi Kubota
伸一 窪田
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP28463587A priority Critical patent/JPH01127645A/en
Publication of JPH01127645A publication Critical patent/JPH01127645A/en
Pending legal-status Critical Current

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  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

PURPOSE:To prevent explosion accident after stopping supply of power to the electric furnace by introducing non-combustible gas from connecting part of an electric furnace with a cooling and dust collecting equipment, to diluting stagnant combustible gas in equipment, and discharging it to outside. CONSTITUTION:Just after stopping supply of the power to the electric furnace 1, the non-combustible gas of N2 gas, etc., is blown from non-combustible gas introducing pipe 16 arranged in the connecting part of the electric furnace 1 with the waste gas cooling and dust collecting equipment. By this gas blowing, CO gas component in the waste from a second chimney 13 is reduced and atmosphere in the waste gas cooling and dust collecting equipment is come to out of the explosion dangerous range. Successively, an inspection hole 14 for ignition being apart from gas off-take part 3 in the electric furnace 1 is opened, and after igniting, a damper 11 for adjusting gas flow rate is fully opened to introduce the air, and the remained gas in the electric furnace 1 is burnt. After introducing the combustion waste gas cooling and dust collecting equipment, the waste gas is diffused from the second chimney 13.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は密閉式合金鉄電気炉を正電するときの電気炉内
残留ガスを安全に処理する方法に関し、詳細には残留ガ
スを着火燃焼して処理するときの爆発危険をなくす方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for safely processing residual gas in an electric furnace when a closed type ferroalloy electric furnace is positively energized, and in particular, a method for igniting and burning the residual gas. This article relates to a method to eliminate the danger of explosion when processing.

[従来の技術] 合金鉄製造用の電気炉からは大量の高熱可燃性ガスが発
生しており1.これをそのまま大気中に放散することは
有価物質の損失、熱エネルギーの放出、大気汚染の発生
等といった問題を招く。この様なところから、電気炉を
密閉式とすることが検討され、今や本邦の電気炉は大部
分が密閉式となっている。
[Prior Art] A large amount of high-temperature flammable gas is generated from an electric furnace for manufacturing ferroalloy.1. Dispersing this into the atmosphere as it is causes problems such as loss of valuable substances, release of thermal energy, and generation of air pollution. For this reason, consideration has been given to making the electric furnace a closed type, and now the majority of electric furnaces in Japan are of the closed type.

密閉方式を採用して回収される可燃性ガスの成分は製造
目的となる合金鉄によっても異なるが、一般にCOを主
成分とし、少量のN2やco2或は更に少量の0.やN
2等から構成され、燃料又は合成化学工業用原料として
有用である。しかし電気炉内から噴出してくるものであ
るから大量のダストを含むと共に高温であって、有用ガ
スとしてガスホルダーに保持したい場合はダスト除去と
冷却処理を施す必要がある。従って例えば散水等で冷却
し回収熱を各種熱源として利用すると共に、ダスト除去
の為のガス処理設備が設置されている。
The components of the combustible gas recovered using the closed system vary depending on the ferroalloy for which it is manufactured, but generally the main component is CO, with a small amount of N2, CO2, or even a small amount of O. YaN
It is useful as a fuel or raw material for synthetic chemical industry. However, since it is ejected from inside the electric furnace, it contains a large amount of dust and is at a high temperature, so if it is desired to retain it in a gas holder as a useful gas, it is necessary to perform dust removal and cooling treatment. Therefore, for example, they are cooled by water spraying and the recovered heat is used as various heat sources, and gas processing equipment is installed to remove dust.

第1図中、16で示す導入管を除く部分は従来の処理設
備を示す説明図であり、電気炉1の定常運転操業によっ
て発生した電気炉ガスは電気炉々M2に形成されたガス
オフテイク部3を通じて図面右方向のガス処理設備へ送
られる。その際電気炉々蓋2に形成されている点検孔4
(図では14箇所)及び炉上の第1煙突5に通じる水封
ダンパ6は外気の流入を防止する為に閉鎖状態とする。
In Fig. 1, the portion excluding the inlet pipe indicated by 16 is an explanatory diagram showing conventional processing equipment, and the electric furnace gas generated by the steady operation of the electric furnace 1 is transferred to the gas offtake formed in the electric furnace M2. The gas is sent through section 3 to the gas processing equipment on the right side of the drawing. At that time, an inspection hole 4 formed in the electric furnace cover 2
(14 locations in the figure) and a water seal damper 6 leading to the first chimney 5 above the furnace are closed to prevent outside air from entering.

ガス処理設備に入ってきた高温・含塵ガスはまず予冷塔
7で冷却されると共に予備的除塵を受け、更にタイゼン
ワッシャ8で除塵される。次いで水分々離器9で水滴の
除去を済ませ、ブースタープロア10で昇圧される。尚
電気炉1におけるガス発生量は操業条件によって変動す
るのを常とするから、当該発生量に相当するガス送り量
を調節する為の電動ダンパ11が設けられており、ガス
ラインの任意の位置で実施するガス分析の結果、ガスホ
ルダーへの貯留に適したガスであればU字状水封管15
を介して貯留部に供給され、貯留に不適当なガスである
ことが分かると三方切換弁12が作動し、適当なガス処
理を介しまたは介さずに第2煙突13から大気中へ放出
される。尚水封ダンパ6が閉鎖されているときに電気炉
2からの排ガス量が一時的に増加するとガス処理設備内
の負荷が上昇するので、これを緩和するためにアスカニ
アダンパ17を開いてリサイクル管18内のリサイクル
ガス量を増加させる。
The high-temperature, dust-containing gas entering the gas processing equipment is first cooled in a pre-cooling tower 7 and subjected to preliminary dust removal, and then further dust removed in a Tizen washer 8. Next, water droplets are removed by a water separator 9, and the pressure is increased by a booster roller 10. Since the amount of gas generated in the electric furnace 1 usually varies depending on the operating conditions, an electric damper 11 is provided to adjust the gas feed amount corresponding to the amount of gas generated. As a result of the gas analysis performed, if the gas is suitable for storage in the gas holder, the U-shaped water seal tube 15
When the gas is found to be unsuitable for storage, the three-way switching valve 12 is activated and the gas is released into the atmosphere from the second chimney 13 with or without appropriate gas treatment. . If the amount of exhaust gas from the electric furnace 2 increases temporarily while the water seal damper 6 is closed, the load in the gas processing equipment will increase, so in order to alleviate this, the Ascania damper 17 is opened and the recycling pipe is opened. Increase the amount of recycled gas in 18.

上記の様な定常運転操業においては、例えば電気炉1或
は関連諸設備の定期修理時期が到来したとぎ、或は電気
炉1の炉内観察を実施したいとき等色々な事情によって
操業を中断しなければならない場合がある。この様な中
断に当たっては電気炉への給電を中止するが、これによ
って炉内でのガス発生がなくなるから、炉蓋内の空間部
に残留した可燃性ガスの処置が問題となる。不処置のま
まで次の作業に入ると、大気圧との圧力バランスの関係
によって炉蓋内各空間部位に大気が流入してくる可能性
がある。また何らかの事情によって炉蓋を開放した場合
には当然大気が流入し、炉蓋内の可燃性ガスと混合され
る。一方炉内は高温であり且つ着火源が存在するから大
気と混合した可燃性ガスはこれによって燃焼し、混合割
合によっては爆発事故を起こす。この様なところから止
電時の炉蓋的残留ガスを安全に処理することが必要とな
り、また該処理に伴って排出されてくるダストは大気汚
染防止の観点から、何らかの手段によって処置されなけ
ればならない。尚この炉蓋内はドーム状を呈し、且つ幾
つかに分かれた複雑な構造を有しているから、炉蓋内残
留ガス組成を全て炉中央部のガス組成と同一視すること
はできないという複雑な問題がある。
In the above-mentioned steady-state operation, the operation may be interrupted for various reasons, such as when it is time for periodic repairs to the electric furnace 1 or related equipment, or when it is desired to observe the inside of the electric furnace 1. There are times when you have to. In such an interruption, the power supply to the electric furnace is stopped, but as this stops gas generation within the furnace, the problem becomes how to deal with the flammable gas remaining in the space within the furnace lid. If the next work is started without treatment, there is a possibility that air will flow into each space inside the furnace lid depending on the pressure balance with the atmospheric pressure. Furthermore, if the furnace lid is opened for some reason, air naturally flows in and mixes with the flammable gas inside the furnace lid. On the other hand, since the temperature inside the furnace is high and there is an ignition source, the flammable gas mixed with the atmosphere burns, causing an explosion depending on the mixing ratio. For this reason, it is necessary to safely dispose of the residual gas on the furnace lid when the power is cut off, and the dust emitted from this processing must be disposed of by some means from the perspective of preventing air pollution. It won't happen. The inside of this furnace lid is dome-shaped and has a complicated structure divided into several parts, so it is difficult to equate the residual gas composition inside the furnace lid with the gas composition in the center of the furnace. There is a problem.

そこで従来は防災の観点から次の様な2つの方法が採ら
れていた。
Conventionally, the following two methods have been adopted from the perspective of disaster prevention.

■ガス処理設備への排ガス導入部を水対等の手段によっ
て電気炉内から遮断し大気や高熱の炉内ガスがガス処理
設備内へ入らない様な処置を講じた後止型する。次いで
電気炉々蓋内が外気圧力に対して負圧とならない様に配
慮を払いつつ該炉蓋内に不活性ガスや蒸気を導入し、炉
蓋内ガスの組成を可燃範囲外とする方法。
■The exhaust gas introduction part to the gas processing equipment is shut off from the electric furnace by means such as a water counter, and measures are taken to prevent atmospheric air and high-temperature furnace gas from entering the gas processing equipment. Next, inert gas or steam is introduced into the electric furnace lid while taking care to prevent the inside of the electric furnace lid from becoming negative pressure with respect to outside air pressure, thereby bringing the composition of the gas inside the furnace lid out of the flammable range.

■炉蓋内の残留可燃性ガスを積極的に燃焼させる方法。■A method of actively burning residual flammable gas within the furnace lid.

[発明が解決しようとする問題点] 上記方法のうち■の方法では炉蓋内ガスが可燃範囲から
外れる迄の時間経過が必要である他、炉蓋内におけるガ
ス成分及び濃度を測定する必要がある。しかし炉蓋内の
構造は前述の如く複雑であり且つ多くの空間に分かれて
いるから、それらの全部位において可燃範囲外となった
か否かを確認することは実買上不可能であり、実操業に
おいては必要十分以上のパージを実施して安全確保を図
っているのが実情である。
[Problems to be solved by the invention] Among the above methods, method (①) requires time to elapse until the gas inside the furnace lid is out of the flammable range, and it is also necessary to measure the gas components and concentration within the furnace lid. be. However, as mentioned above, the structure inside the furnace lid is complex and divided into many spaces, so it is impossible to check whether all parts are outside the flammable range, and it is impossible to do so during actual operation. The reality is that in order to ensure safety, purging is carried out more than necessary and sufficient.

一方■の方法を実施する場合も、まずはじめに■と同様
の手段で電気炉内を遮断した後、電気炉を正電する。次
いで水封ダンパ6の開度をコントロールしながら、炉内
圧力が負圧にならない様に、即ち外気圧よりも高い状態
を形成し、ガスオフテイク部3から最も遠い着火点検孔
14を開け、炉外に放散されてきたガスを種火によって
着火する。その後、水封ダンパ6の開度を大きくして炉
蓋内を外気圧より負圧に調整することにより、着火燃焼
中のガスを大気と共に炉内に引込み、炉蓋内のガスを燃
焼させる。この方法は■の方法に比べて熟練を要すが、
処理時間が短くて済み、炉蓋内ガスは安全レベルまで燃
焼してしまうから、安全性においても優れており、−股
肉には■の方法が汎用されつつある。尚この場合の燃焼
排ガスを第1図のガスラインに従ってガス処理設備に導
入することは、該処理設備内の可燃性ガスと燃焼排ガス
中の酸素の混合による爆発事故の原因ともなるので、第
1図に示した第1煙突5から大気中に放散する。但しこ
のときの排ガスは専用の集塵装置を経由させないことが
多いから多量のダストを含んだままであり、数十分に亘
って褐色あるいは白色の排煙が大気中に放散される。
On the other hand, when carrying out method (2), first, the inside of the electric furnace is shut off using the same method as in (2), and then the electric furnace is positively energized. Next, while controlling the opening degree of the water seal damper 6, the ignition inspection hole 14 furthest from the gas off-take part 3 is opened so that the pressure inside the furnace does not become a negative pressure, that is, it is higher than the outside pressure. The gas that has been released outside the furnace is ignited using a pilot flame. Thereafter, by increasing the opening degree of the water seal damper 6 to adjust the pressure inside the furnace lid to be more negative than the outside pressure, the gas being ignited and burned is drawn into the furnace together with the atmosphere, and the gas inside the furnace lid is combusted. This method requires more skill than method ■, but
Since the processing time is short and the gas in the furnace lid burns to a safe level, it is also excellent in terms of safety, and method (2) is becoming more and more commonly used for crotch meat. In this case, introducing the flue gas into the gas treatment equipment according to the gas line shown in Figure 1 may cause an explosion accident due to the mixing of flammable gas in the treatment equipment and oxygen in the flue gas. It is released into the atmosphere from the first chimney 5 shown in the figure. However, since the exhaust gas at this time is often not passed through a dedicated dust collector, it still contains a large amount of dust, and brown or white exhaust gas is released into the atmosphere for several tens of minutes.

以上述べた様に従来の方法では安全性および環境係合の
面から見て十分な方法とは言い得なかった。
As described above, the conventional methods cannot be said to be sufficient from the viewpoints of safety and environmental friendliness.

[問題点を解決する為の手段] 本発明者等はこの様な事情に着目し、電気炉正電作業を
安全性と環境衛生の両面が満足される様に実施し得る方
法を提供する目的で研究を行なった。即ち本発明は、密
閉式合金鉄電気炉に排ガス冷却・除塵設備が連設されて
いる場合において、電気炉への給電を停止した後、前記
電気炉と前記排ガス冷却・除塵設備の連結部から非燃焼
性ガスを導入して前記排ガス冷却・除塵設備内雰囲気を
爆発危険範囲から外し、次いで電気炉内ガスを着火燃焼
させ、燃焼排ガスを前記排ガス冷却・除塵設備経由で系
外へ放出する様に実施することを要旨とするものである
[Means for Solving the Problems] The inventors of the present invention have focused on the above-mentioned circumstances, and the purpose of the present inventors is to provide a method that can perform electric furnace positive electric work in a manner that satisfies both safety and environmental hygiene. conducted research. That is, the present invention provides, in a case where an exhaust gas cooling/dust removal equipment is connected to a closed type ferroalloy electric furnace, after stopping the power supply to the electric furnace, from the connecting part of the electric furnace and the exhaust gas cooling/dust removal equipment A non-combustible gas is introduced to remove the atmosphere inside the exhaust gas cooling/dust removal equipment from an explosion danger range, and then the gas in the electric furnace is ignited and combusted, and the combustion exhaust gas is released outside the system via the exhaust gas cooling/dust removal equipment. The aim is to implement the project in the future.

[作用〕 本発明においては、従来例で述べた■の方法が、炉蓋内
ガス燃焼後の処置(第1煙突5からの白煙放出)の面で
問題があることに鑑み、排ガス冷却・除塵設備における
ガス配管内の可燃性ガスを予め非燃焼性ガスでパージす
ることを基本構成としている。
[Function] In the present invention, in view of the fact that the method (2) described in the conventional example has a problem in the treatment after the combustion of the gas in the furnace lid (white smoke discharge from the first chimney 5), the present invention provides exhaust gas cooling and The basic configuration is to purge combustible gas in gas piping in dust removal equipment with non-combustible gas in advance.

即ち上記ガス配管内にはCOリッチで更にH2をも含有
する可燃性ガスが残留しており、前記■の方法で発生し
た高熱ガスと大気の混合ガスをそのまま上記ガス配管内
に供給する場合はこれらが混合されて爆発危険領域ガス
組成となり、高温排ガスを熱源として爆発することが恐
れられた。しかし本発明の方法を採用すれば、上記ガス
配管内の可燃性ガスの大部分が非燃焼性ガスでパージさ
れ、上記の様な事態が回避される。従って炉蓋的燃焼ガ
スが大気と共に排ガス冷却・除塵設備内に導入されてき
ても爆発を起こさず、当該設備内で冷却及び除塵が遂行
され、例えば第1図の第2煙突13から放出しても褐色
乃至白色の煙が出ていくという環境保全上の問題は無く
なった。尚本発明で使用される上述の非燃焼性ガスとし
ては、窒素ガスが代表的であるが、他の燃焼装置で発生
した燃焼排ガスを利用することも可能である。本発明の
要点は上述の如く電気炉と排ガス冷却・除塵設備の連結
部から非燃焼性ガスを導入して排ガス冷却・除塵設備内
の可燃性ガスを安全に若しくは部分的にパージして爆発
雰囲気の形成を予防した点に存在するものであるから、
電気炉や排ガス冷却・除塵設備の個々の構成は不問であ
り、また上記パージ後のガス組成を絶対的に規制するも
のではない。
In other words, there is a combustible gas rich in CO and also containing H2 remaining in the gas pipe, and if the mixed gas of the high-temperature gas and the atmosphere generated in the method ① is supplied as it is into the gas pipe. It was feared that these would mix to form a gas composition in the explosion danger zone, and that it would explode using the high-temperature exhaust gas as a heat source. However, if the method of the present invention is adopted, most of the combustible gas in the gas pipe is purged with non-combustible gas, and the above situation can be avoided. Therefore, even if the combustion gas from the furnace lid is introduced into the exhaust gas cooling/dust removal equipment together with the atmosphere, it will not cause an explosion, and the cooling and dust removal will be carried out within the equipment. However, the environmental conservation problem of brown to white smoke being emitted has disappeared. The above-mentioned non-combustible gas used in the present invention is typically nitrogen gas, but it is also possible to use combustion exhaust gas generated from other combustion devices. As mentioned above, the main point of the present invention is to introduce non-combustible gas from the joint between the electric furnace and the exhaust gas cooling/dust removal equipment to safely or partially purge the combustible gas in the exhaust gas cooling/dust removal equipment to create an explosive atmosphere. Because it exists in preventing the formation of
The individual configurations of the electric furnace and exhaust gas cooling/dust removal equipment do not matter, and the composition of the gas after the purging is not absolutely regulated.

尚本発明は上記の如き非燃焼性ガスによるパージ法を採
用するものであるが、従来技術の項で説明した■の方法
に比べると、■の方法が炉蓋内という非常にパージしに
くい場所を無理やり且つ不完全・不経済にパージしてい
たのに対してパイプ内パージという非常に確実且つ経済
的な方法であり、しかも■の方法が炉蓋内の圧力制御と
いう熟練を要しながらも、必要十分以上の過剰パージを
しなければならなかったという汎用性の低い方法である
のに対し、本発明は格別の熟練を必要とせずに必要最低
限のパージを行なえば良いものであり、等しくパージ法
と言い得ても、その技術的内容及び作用効果は本発明が
格段に優れたものと言うことができる。
The present invention employs the above-mentioned purging method using non-combustible gas, but compared to the method (2) explained in the prior art section, the method (2) uses the inside of the furnace lid, which is a place that is extremely difficult to purge. In contrast to forced, incomplete, and uneconomical purging, this method uses pipe purging, which is a very reliable and economical method. , which is a less versatile method that requires excessive purging beyond the necessary and sufficient amount, whereas the present invention allows only the minimum amount of purging to be performed without requiring special skill. Although it can equally be called a purge method, it can be said that the present invention is far superior in terms of its technical content and effects.

[実施例コ 第1図中の電気炉1の出口側ガス配管(ガスオフテイク
部3)に鎖線で示す非燃焼性ガス導入管16を取付けて
本発明実施装置を形成した。
[Example 1] A non-combustible gas introduction pipe 16 shown by a chain line was attached to the outlet side gas pipe (gas off-take section 3) of the electric furnace 1 in FIG. 1 to form an apparatus for implementing the present invention.

電気炉1への給電を中止した直後に非燃焼性ガス導入管
16から約1500 Nm3/Hrの窒素ガスを吹込ん
だ。窒素ガス吹込み直前に第2煙突13近傍で測定した
排ガス組成(電気炉1内のガス組成に等しい)はCOニ
ア3%、H2:1.5%、CO2:25%、その他二0
.5%であったが、同地点におけるガス組成を測定し続
けていた所、窒素ガス吹込みの5分後からCO酸成分低
下しはじめ、10分経過後にはco酸成分12%まで低
下した。Coガスの可燃範囲は一般に12.5%以上と
されているので、上記測定値は爆発危険を脱しているこ
とを示す。そこで電気炉1におけるガスオフテイク部3
から一番離れた着火用点検孔14を開け、種火を用いて
着火後ガス流量調整ダンパ11を全開して大気を導入し
1、電気炉1内の残留ガスを燃焼させた。電気炉1内の
燃焼排ガスを排ガス冷却・除塵設備内に導入し、冷却お
よび除塵の各処理を施した後、第2煙突13から放散し
た。この様な本発明措置を講じなかった従来例の排ガス
(前記■法における第1煙突5からの排ガス)ではダス
ト濃度25.3g/Nm’であったものが本発明方法の
実施により0.056 g/Nm3まで改善された。
Immediately after stopping power supply to the electric furnace 1, about 1500 Nm3/Hr of nitrogen gas was blown from the non-combustible gas introduction pipe 16. The exhaust gas composition measured near the second chimney 13 immediately before nitrogen gas injection (equivalent to the gas composition in the electric furnace 1) was CO2: 3%, H2: 1.5%, CO2: 25%, and other 20%.
.. 5%, but as we continued to measure the gas composition at the same point, the CO acid component began to decrease 5 minutes after nitrogen gas was blown in, and the CO acid component decreased to 12% after 10 minutes. Since the flammability range of Co gas is generally considered to be 12.5% or more, the above measured value indicates that the danger of explosion has been avoided. Therefore, the gas offtake section 3 in the electric furnace 1
The ignition inspection hole 14 furthest from the furnace was opened, and after ignition using a pilot flame, the gas flow rate adjustment damper 11 was fully opened to introduce atmospheric air 1, and the residual gas in the electric furnace 1 was combusted. The combustion exhaust gas in the electric furnace 1 was introduced into the exhaust gas cooling/dust removal equipment, and after being subjected to cooling and dust removal treatment, it was released from the second chimney 13. The dust concentration of conventional exhaust gas (exhaust gas from the first chimney 5 in method ①) in which such measures of the present invention were not taken was 25.3 g/Nm', but by implementing the method of the present invention, the dust concentration was reduced to 0.056 g/Nm'. g/Nm3.

[発明の効果] 本発明はこの様に構成されており、排ガス冷却・除塵設
備内の滞留燃焼性ガスは非燃焼性ガスによって爆発危険
領域以下まで希釈されるので、電気炉の炉蓋的残留ガス
を燃焼させたときに生成する高熱燃焼排ガスと大気との
混合ガスが排ガス冷却・除塵設備内に導入されても当該
設備内で爆発事故を起こすことがない。また従来例に比
べて操業手順が簡略化され、且つ熟練を要さずとも手軽
に実施することができる上に、炉蓋的残留ガスの燃焼排
ガスを冷却および除塵処理できるので、大気放散による
環境悪化の懸念も解消された。
[Effects of the Invention] The present invention is configured as described above, and since the combustible gas accumulated in the exhaust gas cooling/dust removal equipment is diluted by the non-combustible gas to below the explosion danger area, the remaining combustible gas on the lid of the electric furnace is reduced. Even if a mixed gas of high-temperature combustion exhaust gas generated when gas is combusted and the atmosphere is introduced into the exhaust gas cooling/dust removal equipment, an explosion will not occur in the equipment. In addition, the operating procedure is simplified compared to the conventional example, and it can be easily carried out without requiring any skill.In addition, the combustion exhaust gas remaining on the furnace cover can be cooled and dust removed, so it is possible to reduce the environmental impact due to atmospheric dissipation. Concerns about deterioration have also been resolved.

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

第1図は電気炉と排ガス冷却・除塵設備の配設例を示す
説明図である。 1・・・電気炉      2・・・炉蓋3・・・ガス
オフテイク部 4・・・点検孔5・・・第1煙突   
  6・・・水封ダンパ7・・・予冷塔      8
・・・タイゼンワッシャ9・・・水分々部器    l
O・・・ブースターブロワ11・・・ガス流量調整ダン
パ 12・・・三方切換弁    13・・・第2煙突14
・・・着火点検孔    15・・・U字状水封管16
・・・非燃焼性ガス導入管
FIG. 1 is an explanatory diagram showing an example of the arrangement of an electric furnace and exhaust gas cooling/dust removal equipment. 1... Electric furnace 2... Furnace lid 3... Gas off-take part 4... Inspection hole 5... First chimney
6... Water seal damper 7... Precooling tower 8
... Tizen washer 9 ... Moisture unit l
O... Booster blower 11... Gas flow rate adjustment damper 12... Three-way switching valve 13... Second chimney 14
...Ignition inspection hole 15...U-shaped water seal tube 16
...Non-combustible gas introduction pipe

Claims (1)

【特許請求の範囲】[Claims] 合金鉄溶製用電気炉に排ガス冷却・除塵設備を連設して
なる密閉式合金鉄電気設備の止電時処理方法において、
電気炉への給電を停止した後、前記電気炉と前記排ガス
冷却・除塵設備の連結部から非燃焼性ガスを導入して前
記排ガス冷却・除塵設備内雰囲気を爆発危険範囲から外
し、次いで電気炉内ガスを着火燃焼させ、燃焼排ガスを
前記排ガス冷却・除塵設備経由で系外へ放出することを
特徴とする密閉式合金鉄電気炉設備の止電時処理方法。
In a power outage treatment method for closed-type ferroalloy electric equipment, which consists of an electric furnace for ferroalloy melting and exhaust gas cooling and dust removal equipment,
After stopping the power supply to the electric furnace, non-combustible gas is introduced from the connection between the electric furnace and the exhaust gas cooling/dust removal equipment to remove the atmosphere inside the exhaust gas cooling/dust removal equipment from the explosion danger range, and then the electric furnace is turned off. A method for processing a closed type ferroalloy electric furnace equipment during a power outage, characterized in that internal gas is ignited and burned, and the combustion exhaust gas is discharged outside the system via the exhaust gas cooling and dust removal equipment.
JP28463587A 1987-11-11 1987-11-11 Method for treating closed type alloy electric furnace equipment at stopping power Pending JPH01127645A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28463587A JPH01127645A (en) 1987-11-11 1987-11-11 Method for treating closed type alloy electric furnace equipment at stopping power

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28463587A JPH01127645A (en) 1987-11-11 1987-11-11 Method for treating closed type alloy electric furnace equipment at stopping power

Publications (1)

Publication Number Publication Date
JPH01127645A true JPH01127645A (en) 1989-05-19

Family

ID=17681027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28463587A Pending JPH01127645A (en) 1987-11-11 1987-11-11 Method for treating closed type alloy electric furnace equipment at stopping power

Country Status (1)

Country Link
JP (1) JPH01127645A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0313098U (en) * 1989-06-21 1991-02-08

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0313098U (en) * 1989-06-21 1991-02-08

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