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JP3755318B2 - Method and equipment for preventing dust accumulation in exhaust gas duct - Google Patents
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JP3755318B2 - Method and equipment for preventing dust accumulation in exhaust gas duct - Google Patents

Method and equipment for preventing dust accumulation in exhaust gas duct Download PDF

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Publication number
JP3755318B2
JP3755318B2 JP00154599A JP154599A JP3755318B2 JP 3755318 B2 JP3755318 B2 JP 3755318B2 JP 00154599 A JP00154599 A JP 00154599A JP 154599 A JP154599 A JP 154599A JP 3755318 B2 JP3755318 B2 JP 3755318B2
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Japan
Prior art keywords
dust
powder
exhaust gas
gas duct
molten metal
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JP00154599A
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Japanese (ja)
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JP2000199008A (en
Inventor
光紀 牧野
治志 奥田
照義 田本
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JFE Steel Corp
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JFE Steel Corp
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  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、粉体吹込みを行う精錬装置の集塵設備における排ガスダクト内のダスト堆積防止方法および設備に関するものである。
【0002】
【従来の技術】
従来、溶銑の脱珪、脱燐等を行う溶銑予備処理では、精錬用粉体を貯蔵するディスペンサから鉄鉱石、ミルスケール等に石灰、蛍石、ソーダ灰等を混合した精錬用粉体をキャリアガスと共に粉体輸送配管により輸送し、粉体用ランスを介して精錬用容器内の金属溶湯中に添加している。例えば、高炉鋳床に設置された溶銑樋を流れる溶銑を傾注樋に導き、この傾注樋中の溶銑上に粉体用ランスを用いて添加して脱珪処理した後、トピードカーで受銑する。また、ディスペンサ内に貯蔵した精錬用粉体を溶銑予備処理場においてトピードカー内或いは取鍋内の溶銑中に精錬用粉体を粉体用ランスを用いて吹き込み、脱燐や脱硫等の溶銑予備処理を行っている。
【0003】
溶銑の脱珪、脱燐等を行う溶銑の予備処理工場では、例えば、図4に示すように、4基のディスペンサ6には種類の異なった精錬用粉体が貯蔵されており、4基のディスペンサ6のうちNo.1には酸化鉄A、No.2には生石灰、No.3には酸化鉄BまたNo.4にはソーダ灰が貯蔵してある。各ディスペンサ6には圧縮エアを供給して所定の圧力に保たれている。粉体用ランス1が、台車2上に設けた傾動可能なランス昇降装置3によってトピードカー4の真上で停止される。
【0004】
次に、エア導管7中に精錬用粉体が堆積しないように、粉体の搬送に合った圧力と流量に調節されたキャリアガスとなるドライエアを自動弁8を開いて粉体用ランス1より吹き出させた後、粉体切出弁9を開き、精錬用粉体を流し、エア導管7に供給する。同時に、酸素導管10に配設した自動弁11を開いて必要な圧力と流量に調節された気体酸素を粉体用ランス1より吹き出させる。ここで粉体用ランス1より溶銑12中に吹き込むのに必要な圧力と流量に調節するため、余剰のエアは排気管24に配設した排気弁13によって排気される。なお、粉体用ランス1に酸素導管10を介して気体酸素を供給せずキャリアガスのみを精錬用粉体と共に吹き込む場合も多い。
【0005】
エア導管7内のドライエアと混合した精錬用粉体(酸化鉄A、生石灰、酸化鉄B、ソーダ灰)は、フレキシブルホース14を通り、また酸素導管10内の気体酸素はフレキシブルホース15を通り粉体用ランス1より吹き出しつつ、直ちに、ランス昇降装置3によってトピードカー4に収容された溶銑12の任意深さに浸漬され、粉体用ランス1から吹き込まれる精錬用粉体により溶銑12の脱珪、脱燐処理が行われる。
【0006】
一般に、粉体を吹き込む場合、その一部は、本来の目的に沿わず一部が系外に漏洩する。そのため、相当能力の集塵設備を設置して漏洩する粉体を集塵している。溶銑12の脱珪、脱燐処理中に炉内で発生する含塵ガスは、トピードカー4に設けた炉口5の上方をカバーする集塵フード16により捕集され、排ガスダクト17を経由して排出される。含塵ガスは、排ガスダクト17の途中に配設したガスクーラ18により冷却された後、集塵機19(電気集塵機やバグフィルタ集塵機等を使用)に導いて集塵される。
【0007】
ところで、排ガスダクト17を介して集塵機19に導き含塵ダストを集塵する際に、図5に示すように、排ガスダクト17が垂直から屈曲して水平になる部分にダスト21が堆積しやすく、これが含塵ガスの通気性を妨げるので集塵能力の低下原因となり、また排ガスダクト17内に堆積したダスト18を、マンホール22を取り外して度々掃除するのを余儀なくされるという問題点があった。堆積ダストが生じた場合、例えば、特開昭9-323050号公報には電気集塵機が備えた電極の下方に配置した下部ホッパのダスト堆積位置に気体発生装置から気体を供給し、噴射により除去する方法が開示されている。
【0008】
【発明が解決しようとする課題】
しかしながら、排ガスダクトや下部ホッパに堆積したダストに気体を噴射するには、気体発生装置が必要で、設備費が嵩むことになる。一般に、粉塵の漏洩による環境汚染を防止のためには、相当能力の集塵機が必要となり、コスト的な問題を伴う。経済面を重視して能力の過少な集塵機を設置すると、集塵ダクト内にダストが堆積し、集塵能力の低下や集塵ダクト内の堆積ダストに掃除を頻繁に行わなければならない等の問題点があるのは前述の通りである。
【0009】
本発明は、前記問題点を解決し、気体発生装置を設置することなく排ガスダクト内のダスト堆積を防止する方法および設備を提供することを目的とするものである。
【0010】
【課題を解決するための手段】
前記目的を達成するための請求項1記載の本発明は、ディスペンサ内の精錬用粉体をキャリアガスと共に粉体輸送配管を介して気送し、粉体用ランスから溶湯容器の金属溶湯中へ添加する一方、該溶湯容器内で発生する含塵ガスを前記溶湯容器の炉口上方に配置したフードで捕集し、排ガスダクトを経由して集塵機に導き集塵する際の排ガスダクト内のダスト堆積防止方法において、前記ディスペンサの排気を排気管を介して該排気管の先端部に形成した吹出ノズルから前記排ガスダクト内のダストが堆積し易い箇所に導き、噴出することを特徴とする排ガスダクト内のダスト堆積防止方法である。
【0011】
請求項2記載の本発明は、精錬用粉体を貯蔵するディスペンサと、該ディスペンサから精錬用粉体をキャリアガスと共に輸送する粉体輸送配管と、該粉体輸送配管により輸送される精錬用粉体を溶湯容器の金属溶湯中に添加する粉体用ランスと、前記溶湯容器内で発生する含塵ガスを捕集する前記溶湯容器の炉口上方に配置したフードと、該フードで捕集した含塵ガスを排ガスダクトを経由して集塵する集塵機とを具備した精錬用粉体供給設備において、前記ディスペンサから排気を取り出すための排気管を、前記排ガスダクト内でダストが堆積し易い箇所まで延設し、前記排ガスダクト内に臨ませ、該排気管の先端部に吹出ノズルを配設したことを特徴とする排ガスダクト内のダスト堆積防止装置付精錬用粉体供給設備である。
【0012】
【発明の実施の形態】
以下、本発明の実施形態を図面に基づいて説明する。
図1に示すように、4基のディスペンサ6には種類の異なった精錬用粉体が貯蔵されており、4基のディスペンサ6のうちNo.1には酸化鉄A、No.2には生石灰、No.3には酸化鉄BまたNo.4にはソーダ灰が貯蔵されている。各ディスペンサ6には圧縮エアを供給して所定の圧力に保たれている。1番線軌道および2番線軌道にはそれぞれ2台、計4台の溶銑を収容したトピードカー4が停止している。なお、図4に示したものと同じものは同一符号を付し説明が重複するのを省略する。
【0013】
エア導管7内でキャリアガスとなるドライエアと混合した精錬用粉体(酸化鉄A、生石灰、酸化鉄B、ソーダ灰)は、フレキシブルホース14を通り、また酸素導管10内の気体酸素はフレキシブルホース15を通り粉体用ランス1より吹き出し、トピードカー4に収容された溶銑12中に吹き込まれ、溶銑の脱珪、脱燐処理が行われる。粉体用ランス1より溶銑12中に吹き込むのに必要な圧力と流量に調節しつつ、余剰のエアをディスペンサ6のガス排気弁13によって排気する。図1では、傾動可能なランス昇降装置3を備えた台車2を省略して示す。
【0014】
溶銑12の脱珪、脱燐処理中にトピードカー4内で発生する含塵ガスは、炉口5の上方をカバーする集塵フード16により捕集され、排ガスダクト17を経由して排出される。ここで、排ガスダクト17は途中に設けたダンパ23により仕切って2系統に分けてあり、図面上で右側2台のトピードカー4内で発生する含塵ガスは、排ガスダクト17の途中に配設したガスクーラ18により冷却された後、排風機20を介してNo.1集塵機19に導き集塵され、左側2台のトピードカー4内で発生する含塵ガスはNo.1集塵機19に導き集塵される。
【0015】
ところで、排ガスダクト17を介して集塵機19に導いて含塵ダストを集塵するに際し、排ガスダクト17が垂直から水平に屈曲する部分やダンパ23で仕切られた近傍部分では、排ガスダクト17内にダスト21が堆積しやすい。そこで、本発明では、ダンパ23の近傍にNo.1の吹出ノズル25を、また排ガスダクト17の屈曲部の近傍にNo.2の吹出ノズル25およびNo.3の吹出ノズル25を配設し、それぞれ排ガスダクト17内に臨ませる。4基のディスペンサ6から取り出した排気管24を延設してダストが堆積し易い箇所まで導き、排気管24の先端部をそれぞれの吹出ノズル25に接続してある。図2は、ダンパ23の近傍における排ガスダクト17内ににNo.1の吹出ノズル25を排ガス流26の方向に向けて配設した場合を示し、また、図3は排ガスダクト17の屈曲部にNo.2の吹出ノズル25を排ガス流26の方向に向けて配設した場合を示している。
【0016】
次に、本発明の作用について説明する。
溶銑12の脱珪、脱燐処理中にトピードカー4内で発生する含塵ガスは、炉口5の上方をカバーする集塵フード16により捕集され、排ガスダクト17を経由して排出される。排ガスダクト17内を流れる排ガス中のダストが、堆積しやすい箇所に配置された吹出ノズル25(No.1、No.2、No.3)に、ディスペンサ6内の加圧された余剰エアを排気弁13を開として排気管24を通して導き、排ガスダクト17内に堆積するダストを吹出ノズル25から噴出する気体により吹き飛ばす。
【0017】
ディスペンサ6の余剰エアは、堆積しやすい箇所の堆積ダストを吹き飛ばす圧力を有し、そのエア量も十分である。吹き飛ばされたダストは排ガス流26に乗せて流れ、2系統の排ガスダクト17を経由して一方はNo1.集塵機19に、また、他方はNo.2の集塵機にそれぞれ導かれて集塵される。その結果、排ガスダクト17内にダストが堆積するのが防止され、また、ダスト21は、マンホール22の箇所に少量堆積する程度に止まり堆積ダストの掃除回数を大幅に削減できる。
【0018】
【発明の効果】
以上説明したように本発明では、ディスペンサから排出した余剰の圧力排気を利用し、これを排ガスダクトのダストが堆積する可能性の高い箇所に導き、吹出ノズルから噴出させて排ガスダクト内の堆積ダストを早めに吹き飛ばし、排ガスと共に集塵機によって集塵除去できる。このため吹出ノズルに供給する気体発生装置の増設が不要であり、集塵ダクト内の堆積ダストに起因する集塵能力の低下が防止され、また堆積ダストの除去作業を大幅に低減できる等、その効果は多大である。
【図面の簡単な説明】
【図1】本発明例に係わるディスペンサのみを側面で示し、他を平面で示す精錬用粉体供給装置の全体配置図である。
【図2】図1のA−A矢視方向を示す断面図である。
【図3】図1のB−B矢視方向を示す断面図である。
【図4】従来例の精錬用粉体供給装置の全体配置図である。
【図5】従来例に係わる排ガスダクト内にダストが堆積した状態を示す説明図である。
【符号の説明】
1 粉体用ランス
2 台車
3 ランス昇降装置
4 トピードカー
5 炉口
6 ディスペンサ
7 エア導管
8 自動弁
9 切出弁
10 酸素導管
11 自動弁
12 溶銑
13 排気弁
14、15 フレキシブルホース
16 集塵フード
17 排ガスダクト
18 ガスクーラ
19 集塵機
20 排風機
21 ダスト
22 マンホール
23 ダンパ
24 排気管
25 吹出ノズル
26 排ガス流
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method and an apparatus for preventing dust accumulation in an exhaust gas duct in a dust collection facility of a refining apparatus that performs powder blowing.
[0002]
[Prior art]
Conventionally, in hot metal pretreatment for hot metal desiliconization, dephosphorization, etc., a refining powder in which lime, fluorite, soda ash, etc. are mixed with iron ore, mill scale, etc. from a dispenser that stores the refining powder is used as a carrier. It is transported together with the gas by a powder transport pipe and added to the molten metal in the refining vessel through the powder lance. For example, the hot metal flowing through the hot metal installed on the blast furnace casting floor is guided to the tilting iron, added to the hot metal in the tilting iron using a lance for powder, and desiliconized, and then received by a topped car. In addition, the powder for refining stored in the dispenser is blown into the hot metal in the topped car or ladle at the hot metal pretreatment plant using the powder lance, and the hot metal pretreatment such as dephosphorization or desulfurization is performed. It is carried out.
[0003]
In a hot metal pretreatment plant that performs hot metal desiliconization, dephosphorization, etc., for example, as shown in FIG. 4, four types of refining powders are stored in four dispensers 6. Of the dispensers 6, No. 1 stores iron oxide A, No. 2 stores quick lime, No. 3 stores iron oxide B, and No. 4 stores soda ash. Each dispenser 6 is supplied with compressed air and maintained at a predetermined pressure. The powder lance 1 is stopped immediately above the topped car 4 by a tiltable lance lifting device 3 provided on the carriage 2.
[0004]
Next, dry air, which is a carrier gas adjusted to a pressure and flow rate suitable for the conveyance of the powder, is opened from the lance 1 for powder by opening the automatic valve 8 so that the powder for refining does not accumulate in the air conduit 7. After blowing out, the powder cutting valve 9 is opened, the powder for refining is poured, and supplied to the air conduit 7. At the same time, the automatic valve 11 disposed in the oxygen conduit 10 is opened to blow out gaseous oxygen adjusted to the required pressure and flow rate from the powder lance 1. Here, excess air is exhausted by an exhaust valve 13 disposed in an exhaust pipe 24 in order to adjust the pressure and flow rate required to blow into the hot metal 12 from the powder lance 1. In many cases, only the carrier gas is blown into the powder lance 1 together with the refining powder without supplying gaseous oxygen via the oxygen conduit 10.
[0005]
Powder for refining (iron oxide A, quicklime, iron oxide B, soda ash) mixed with dry air in the air conduit 7 passes through the flexible hose 14, and gaseous oxygen in the oxygen conduit 10 passes through the flexible hose 15 to powder. While blowing out from the body lance 1, the hot metal 12 is desiliconized by the smelting powder immersed in the hot metal 12 accommodated in the topped car 4 by the lance lifting device 3 and blown from the powder lance 1. A dephosphorization process is performed.
[0006]
In general, when powder is blown, a part of the powder does not meet the original purpose and a part leaks out of the system. For this reason, a dust collection facility with a considerable capacity is installed to collect the leaked powder. Dust-containing gas generated in the furnace during desiliconization and dephosphorization of the hot metal 12 is collected by a dust collection hood 16 that covers the top of the furnace port 5 provided in the topped car 4 and passes through an exhaust gas duct 17. Discharged. The dust-containing gas is cooled by a gas cooler 18 disposed in the middle of the exhaust gas duct 17, and then guided to a dust collector 19 (using an electric dust collector, a bag filter dust collector, etc.) and collected.
[0007]
By the way, when the dust-containing dust is guided to the dust collector 19 via the exhaust gas duct 17 and dust is collected, as shown in FIG. This hinders the air permeability of the dust-containing gas, which causes a decrease in dust collection capability, and there is a problem that the dust 18 accumulated in the exhaust gas duct 17 must be frequently cleaned by removing the manhole 22. When accumulated dust is generated, for example, Japanese Patent Laid-Open No. 9-323050 discloses that gas is supplied from a gas generator to a dust accumulation position of a lower hopper disposed below an electrode provided in an electrostatic precipitator and removed by jetting. A method is disclosed.
[0008]
[Problems to be solved by the invention]
However, in order to inject gas into the dust accumulated in the exhaust gas duct or the lower hopper, a gas generator is required, which increases the equipment cost. In general, in order to prevent environmental pollution due to dust leakage, a dust collector with a considerable capacity is required, which is associated with cost problems. If a dust collector with insufficient capacity is installed with emphasis on the economy, dust accumulates in the dust collection duct, causing problems such as a decrease in dust collection capacity and frequent cleaning of the accumulated dust in the dust collection duct. The point is as described above.
[0009]
An object of the present invention is to solve the above problems and to provide a method and equipment for preventing dust accumulation in an exhaust gas duct without installing a gas generator.
[0010]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, the present invention according to claim 1 is characterized in that the powder for refining in the dispenser is fed together with the carrier gas through the powder transport pipe, and from the powder lance to the molten metal in the molten metal container. While being added, the dust-containing gas generated in the molten metal container is collected by a hood disposed above the furnace port of the molten metal container, and dust is collected in the exhaust gas duct when it is collected through the exhaust gas duct to the dust collector. In the accumulation prevention method, exhaust gas from the dispenser is guided through a discharge nozzle to a place where dust in the exhaust gas duct is likely to accumulate through an exhaust pipe, and exhausted. It is a dust accumulation prevention method in the inside.
[0011]
The present invention described in claim 2 is a dispenser for storing a refining powder, a powder transport pipe for transporting the refining powder together with a carrier gas from the dispenser, and a refining powder transported by the powder transport pipe. A powder lance for adding the body to the molten metal in the molten metal container, a hood disposed above the furnace port of the molten metal container for collecting dust-containing gas generated in the molten metal container, and the hood In a refining powder supply facility equipped with a dust collector that collects dust-containing gas via an exhaust gas duct, an exhaust pipe for taking out exhaust gas from the dispenser to a place where dust easily accumulates in the exhaust gas duct A powder supply facility for refining with a dust accumulation preventing device in an exhaust gas duct, characterized in that it extends, faces the exhaust gas duct, and a blow-off nozzle is disposed at the tip of the exhaust pipe.
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
As shown in FIG. 1, four kinds of refining powders are stored in four dispensers 6, and among the four dispensers 6, No. 1 is iron oxide A and No. 2 is quicklime. No. 3 stores iron oxide B and No. 4 stores soda ash. Each dispenser 6 is supplied with compressed air and maintained at a predetermined pressure. The toped car 4 containing a total of four hot metal baths is stopped on the first track and the second track. 4 that are the same as those shown in FIG. 4 are given the same reference numerals, and redundant descriptions are omitted.
[0013]
Powder for refining (iron oxide A, quicklime, iron oxide B, soda ash) mixed with dry air, which is a carrier gas, in the air conduit 7 passes through the flexible hose 14, and the gaseous oxygen in the oxygen conduit 10 is the flexible hose. 15 is blown out from the lance 1 for powder and blown into the hot metal 12 accommodated in the topped car 4 to perform desiliconization and dephosphorization of the hot metal. Excess air is exhausted by the gas exhaust valve 13 of the dispenser 6 while adjusting the pressure and flow rate required to blow into the hot metal 12 from the powder lance 1. In FIG. 1, the cart 2 provided with the tiltable lance lifting device 3 is omitted.
[0014]
Dust-containing gas generated in the topped car 4 during the desiliconization and dephosphorization processes of the hot metal 12 is collected by a dust collection hood 16 that covers the top of the furnace port 5 and is discharged through an exhaust gas duct 17. Here, the exhaust gas duct 17 is divided into two systems by a damper 23 provided in the middle, and the dust-containing gas generated in the two topped cars 4 on the right side in the drawing is disposed in the middle of the exhaust gas duct 17. After being cooled by the gas cooler 18, the dust is introduced into the No. 1 dust collector 19 through the exhaust fan 20, and the dust-containing gas generated in the left two topped cars 4 is led to the No. 1 dust collector 19 and collected. .
[0015]
By the way, when dust-containing dust is collected by being guided to the dust collector 19 via the exhaust gas duct 17, dust is contained in the exhaust gas duct 17 at a portion where the exhaust gas duct 17 is bent from the vertical to the horizontal or a portion partitioned by the damper 23. 21 is easy to deposit. Therefore, in the present invention, the No. 1 blowing nozzle 25 is disposed in the vicinity of the damper 23, and the No. 2 blowing nozzle 25 and the No. 3 blowing nozzle 25 are disposed in the vicinity of the bent portion of the exhaust gas duct 17, Each is exposed to the exhaust gas duct 17. The exhaust pipes 24 taken out from the four dispensers 6 are extended and led to a place where dust is likely to accumulate, and the tip end portions of the exhaust pipes 24 are connected to the respective blowing nozzles 25. FIG. 2 shows a case in which the No. 1 blowing nozzle 25 is arranged in the direction of the exhaust gas flow 26 in the exhaust gas duct 17 in the vicinity of the damper 23, and FIG. The case where the No. 2 blowing nozzle 25 is arranged in the direction of the exhaust gas flow 26 is shown.
[0016]
Next, the operation of the present invention will be described.
Dust-containing gas generated in the topped car 4 during the desiliconization and dephosphorization processes of the hot metal 12 is collected by a dust collection hood 16 that covers the top of the furnace port 5 and is discharged through an exhaust gas duct 17. Excess pressurized air in the dispenser 6 is exhausted to the blowout nozzles 25 (No.1, No.2, No.3) located where the dust in the exhaust gas flowing in the exhaust gas duct 17 is likely to accumulate. The valve 13 is opened and guided through the exhaust pipe 24, and the dust accumulated in the exhaust gas duct 17 is blown away by the gas ejected from the blowing nozzle 25.
[0017]
The surplus air of the dispenser 6 has a pressure to blow away the accumulated dust at the place where it is easy to accumulate, and the amount of air is sufficient. The dust blown off flows on the exhaust gas stream 26, and is guided to the No. 1 dust collector 19 and the other to the No. 2 dust collector through the two exhaust gas ducts 17, and is collected. As a result, dust is prevented from accumulating in the exhaust gas duct 17, and the dust 21 stops only to a small extent in the manhole 22, and the number of cleanings of the accumulated dust can be greatly reduced.
[0018]
【The invention's effect】
As described above, in the present invention, excess pressure exhaust discharged from the dispenser is used, and this is led to a place where the dust in the exhaust gas duct is highly likely to accumulate, and is ejected from the blow nozzle to be accumulated dust in the exhaust gas duct. The dust can be blown away early and collected with a dust collector together with the exhaust gas. For this reason, it is not necessary to add a gas generator to be supplied to the blowout nozzle, preventing a decrease in dust collection capacity caused by accumulated dust in the dust collecting duct, and greatly reducing the work of removing accumulated dust. The effect is enormous.
[Brief description of the drawings]
FIG. 1 is an overall layout view of a refining powder supply apparatus showing only a dispenser according to an embodiment of the present invention on a side surface and the other on a plane.
FIG. 2 is a cross-sectional view showing the direction of arrows AA in FIG.
FIG. 3 is a cross-sectional view showing the direction of arrows BB in FIG. 1;
FIG. 4 is an overall layout view of a refining powder supply apparatus of a conventional example.
FIG. 5 is an explanatory view showing a state where dust is accumulated in an exhaust gas duct according to a conventional example.
[Explanation of symbols]
1 Lance for powder 2 Dolly 3 Lance lifting device 4 Topped car 5 Furnace port 6 Dispenser 7 Air conduit 8 Automatic valve 9 Cutting valve
10 Oxygen conduit
11 Automatic valve
12 Hot metal
13 Exhaust valve
14, 15 Flexible hose
16 Dust collection hood
17 Exhaust duct
18 Gas cooler
19 Dust collector
20 Ventilator
21 dust
22 Manhole
23 Damper
24 Exhaust pipe
25 Outlet nozzle
26 Exhaust gas flow

Claims (2)

ディスペンサ内の精錬用粉体をキャリアガスと共に粉体輸送配管を介して気送し、粉体用ランスから溶湯容器の金属溶湯中へ添加する一方、該溶湯容器内で発生する含塵ガスを前記溶湯容器の炉口上方に配置したフードで捕集し、排ガスダクトを経由して集塵機に導き集塵する際に、前記ディスペンサの排気を、排気管を介して該排気管の先端部に形成した吹出ノズルから前記排ガスダクト内のダストが堆積し易い箇所に噴出することを特徴とする排ガスダクト内のダスト堆積防止方法。The fine powder for refining in the dispenser is pneumatically fed together with a carrier gas through a powder transport pipe, and added from the powder lance to the molten metal in the molten metal container, while the dust-containing gas generated in the molten metal container is When collecting with a hood arranged above the furnace port of the molten metal container and collecting the dust through the exhaust gas duct to the dust collector, the exhaust of the dispenser was formed at the tip of the exhaust pipe via the exhaust pipe. A dust accumulation preventing method in an exhaust gas duct, characterized in that the dust in the exhaust gas duct is ejected from a blowing nozzle to a place where dust in the exhaust gas duct is likely to accumulate. 精錬用粉体を貯蔵するディスペンサと、該ディスペンサから精錬用粉体をキャリアガスと共に輸送する粉体輸送配管と、該粉体輸送配管により輸送される精錬用粉体を溶湯容器の金属溶湯中に添加する粉体用ランスと、前記溶湯容器内で発生する含塵ガスを捕集する前記溶湯容器の炉口上方に配置したフードと、該フードで捕集した含塵ガスを排ガスダクトを経由して集塵する集塵機とを具備した精錬用粉体供給設備において、前記ディスペンサから排気を取り出すための排気管を、前記排ガスダクト内でダストが堆積し易い箇所まで延設し、前記排ガスダクト内に臨ませ、前記排気管の先端部に吹出ノズルを配設したことを特徴とする排ガスダクト内のダスト堆積防止装置付精錬用粉体供給設備。Dispenser for storing refining powder, powder transport pipe for transporting refining powder together with carrier gas from the dispenser, and refining powder transported by the powder transport pipe in the molten metal in the molten metal container A lance for powder to be added, a hood arranged above the furnace port of the molten metal container for collecting the dust-containing gas generated in the molten metal container, and the dust-containing gas collected by the hood through an exhaust gas duct In a refining powder supply facility comprising a dust collector for collecting dust, an exhaust pipe for taking out exhaust gas from the dispenser is extended to a location where dust is likely to accumulate in the exhaust gas duct, A powder supply facility for refining with a dust accumulation preventing device in an exhaust gas duct, characterized in that a blow-off nozzle is arranged at the tip of the exhaust pipe.
JP00154599A 1999-01-07 1999-01-07 Method and equipment for preventing dust accumulation in exhaust gas duct Expired - Fee Related JP3755318B2 (en)

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