JPS6140004B2 - - Google Patents

Info

Publication number
JPS6140004B2
JPS6140004B2 JP11670781A JP11670781A JPS6140004B2 JP S6140004 B2 JPS6140004 B2 JP S6140004B2 JP 11670781 A JP11670781 A JP 11670781A JP 11670781 A JP11670781 A JP 11670781A JP S6140004 B2 JPS6140004 B2 JP S6140004B2
Authority
JP
Japan
Prior art keywords
dust
dust collection
electrostatic precipitator
abnormal
tapping
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
JP11670781A
Other languages
Japanese (ja)
Other versions
JPS5819418A (en
Inventor
Shuichi Aoki
Osamu Shimizu
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 JP56116707A priority Critical patent/JPS5819418A/en
Publication of JPS5819418A publication Critical patent/JPS5819418A/en
Publication of JPS6140004B2 publication Critical patent/JPS6140004B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/22Dust arresters

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrostatic Separation (AREA)
  • Blast Furnaces (AREA)

Description

【発明の詳細な説明】 本発明は、高炉鋳床集塵設備に係り、詳しくは
高炉操業時の出銑作業において発生する全ての発
塵ガスを鋳床建家上部に導き、電気集塵機により
集塵することを可能にした集塵設備に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a blast furnace casthouse dust collection system, and more specifically, all dust gases generated during the tapping operation during blast furnace operation are guided to the upper part of the casthouse building and collected by an electrostatic precipitator. Regarding dust collection equipment that makes it possible to remove dust.

高炉鋳床集塵は、一般的に1次集塵と2次集塵
の組合せからなつている。1次集塵設備は、通常
出銑時に出銑口、大樋、スキンマー、溶銑樋、傾
注樋等から発生する発塵を、発生源近傍で局所的
に集塵し、2次集塵設備は、出銑時の初期又は末
期に出銑口から発生する膨大な量の発煙(通称異
状発塵)を建家内に貯留し集塵する。現在最も広
く採用されているのは、この方式において各発塵
部から発生する発塵ガスをそれぞれ大型排風機で
強制吸引し、バグフイルター(集塵機)で煙を清
浄にしている。
Blast furnace casthouse dust collection generally consists of a combination of primary dust collection and secondary dust collection. The primary dust collection equipment normally collects dust generated from the taphole, big culvert, skinmer, hot metal trough, tilting trough, etc. during tapping locally near the source, and the secondary dust collection equipment A huge amount of smoke (commonly known as abnormal dust generation) generated from the taphole at the beginning or end of the tapping period is stored in the building and collected. Currently, the most widely used method is this method, in which the dust gas generated from each part of the dust generating section is forcibly sucked in using large exhaust fans, and the smoke is purified using bag filters (dust collectors).

第1図は上記の集塵システムを示したものであ
る。1は高炉であり通常出銑時において出銑口、
大樋、スキンマー、溶銑滓樋、溶銑滓傾注樋等か
ら発生する発塵ガスをフード2によつて集煙し、
フード2に連結した集塵ダクト3を通して地上に
設置した大型排風機4により吸引し、バグフイル
ター5で集塵するものである。
FIG. 1 shows the above-mentioned dust collection system. 1 is a blast furnace, and during normal tapping, the taphole,
The dust gas generated from the big gutter, skimmer, hot metal slag gutter, hot metal slag pouring gutter, etc. is collected by the hood 2,
The dust is sucked in by a large exhaust fan 4 installed on the ground through a dust collection duct 3 connected to a hood 2, and the dust is collected by a bag filter 5.

一方出銑口からの異状発塵ガス等は、建家天井
部のフード6から集塵ダクト7を通して地上に設
置した大型排風機8により吸引し、バグフイルタ
ー9により集塵するものである。ところがこの方
式では、次の3つの重大な欠点がある。
On the other hand, abnormal dust gases etc. from the taphole are sucked from a hood 6 on the ceiling of the building through a dust collection duct 7 by a large exhaust fan 8 installed on the ground, and collected by a bag filter 9. However, this method has the following three serious drawbacks.

○ア 集塵フード、ダクトの圧力損失が300m/m
Aq程度あり、さらにバグフイルターの圧力損
失が250m/mAq程度あるので排風機が非常に
大型となり、莫大な運転費が必要である。
○A Pressure loss of dust collection hood and duct is 300m/m
Aq, and the pressure loss of the bag filter is about 250m/mAq, making the exhaust fan very large and requiring huge operating costs.

○イ 出銑口からの異状発塵は熱上昇気流によつて
建家天井部まで上昇してゆき、この発塵を天井
部のフードから地上に設置した排風機で吸引
し、バグフイルターで集塵しているが、この場
合強制吸引をするため、鋳床内の余分な空気ま
で吸い込む。したがつて排風機が大型となり無
駄な運転費を使うことになる。
○B Abnormal dust from the taphole rises to the ceiling of the building due to the rising heat, and this dust is sucked through the hood in the ceiling by an exhaust fan installed on the ground, and collected by a bag filter. Although it is dusty, in this case forced suction is used, which sucks in even the excess air inside the cast bed. As a result, the exhaust fan becomes large, resulting in unnecessary operating costs.

○ウ 通常出銑時、出銑口の開閉はマツドガン開口
機で作業を行うため、出銑口前の大樋カバーの
一部を取外す必要があり、この間は完全な防塵
対策が取れない。この場合の発塵ガスは1次集
塵設備では対処できないので上記○イと同じ系統
で集塵する必要がある。
○C During normal tapping, the taphole is opened and closed using a Matsudogun opening machine, so it is necessary to remove part of the large gutter cover in front of the taphole, and during this time complete dustproof measures cannot be taken. In this case, the dust gas cannot be handled by the primary dust collection equipment, so it is necessary to collect the dust using the same system as in A above.

上記の欠点から、このシステムでは運転費が莫
大となるため、省エネルギー上問題であつた。こ
の運転費用を少くする方法として排風機の回転数
制御等の省電力システムを採用しているが、それ
でも運転費は相当なものになつている。更に運転
費の軽減対策として、2次集塵用のバグフイルタ
ーを電気集塵機に変更する方法がある。これは電
気集塵機を鋳床建家上部に搭載するもので、いわ
ゆる建家直接搭載型電気集塵装置と言われ既に特
公昭56−4123号によつて提案されている。
Due to the above-mentioned drawbacks, this system has an enormous operating cost, which poses a problem in terms of energy conservation. As a way to reduce operating costs, power-saving systems such as controlling the rotation speed of exhaust fans have been adopted, but operating costs are still considerable. Furthermore, as a measure to reduce operating costs, there is a method of replacing the bag filter for secondary dust collection with an electrostatic precipitator. This is a device in which an electrostatic precipitator is mounted on the upper part of the casting house, and is called a so-called electrostatic precipitator mounted directly on the building, and has already been proposed in Japanese Patent Publication No. 4123/1983.

第2図は、1次集塵設備は従来どおりである
が、2次集塵設備を上記のものに改善したものを
示す。このシステムは出銑口1からの異状発塵ガ
スを建家天井部に搭載した電気集塵機10で集塵
するものである。この場合、発塵ガスは熱上昇気
流による、いわゆる自然換気方式を採用するため
大型排風機を必要とせず、2次集塵システムの大
幅な運転費の削減をもたらす。しかし電気集塵機
の利用は、異常発塵及び出銑口開閉時のみで、そ
の他はいわゆる遊んでいる状態であり、利用率は
非常に低いにもかかわらず、電気集塵機は常時荷
電された状態にある。一方1次集塵設備2〜5は
従来通りで改善されてなく、運転費は莫大となつ
ている。
FIG. 2 shows a system in which the primary dust collection equipment is the same as the conventional one, but the secondary dust collection equipment has been improved to the one described above. This system collects abnormal dust gas from the tap hole 1 using an electric precipitator 10 mounted on the ceiling of the building. In this case, a so-called natural ventilation method is adopted in which the dust gas is generated by thermal upward currents, so a large exhaust fan is not required, resulting in a significant reduction in operating costs for the secondary dust collection system. However, the electrostatic precipitator is only used when there is abnormal dust generation or when the taphole is opened and closed, and otherwise it is in a so-called idle state.Although the utilization rate is very low, the electrostatic precipitator is always charged. . On the other hand, the primary dust collection facilities 2 to 5 are the same as before and have not been improved, resulting in enormous operating costs.

そこで本発明は、建家搭載型電気集塵機で、通
常出銑時の局所発塵ガスと異状発塵ガスの両方を
集塵することにより大幅な電力費の削減をはかる
システムを提供するものである。
Therefore, the present invention provides a system that uses a building-mounted electrostatic precipitator to collect both local dust gas and abnormal dust gas during normal tapping, thereby significantly reducing power costs. .

本発明は建家天井部に複数個の電気集塵機を搭
載し、従来どおり出銑口からの異状発塵ガス等を
集塵するのは、もちろんのこと、この異状発塵は
めつたにない(数回/月)ことから、電気集塵機
は大半が遊んでおり設備の効率が甚だ悪いことに
着目し、この遊んでいる時間を利用して通常出銑
時の出銑口、大樋、スキンマー、溶銑滓樋、溶銑
滓落口等の局所発塵ガスをこの建家電気集塵機で
集塵しようとするものである。この方法が可能と
なる理由は、異状発塵は出銑初期又は末期に発生
するが、ラツプ出銑は同時に異状発塵が発生しな
いように実施されている。すなわち、どちらかの
集塵機は遊んでいるので異状発塵が発生しても同
時に発生する局所発塵ガスを他の電気集塵機にま
わすことで集塵は可能である。又通常出銑時の局
所発塵風量と異状発塵風量は同程度であるため、
従来の建家電気集塵機の容量を大幅にアツプさせ
ずに両方の発塵ガスを処理することが可能とな
る。
The present invention has a plurality of electrostatic precipitators mounted on the ceiling of the building, and while it is possible to collect abnormal dust gas etc. from the taphole as in the past, this abnormal dust generation is rare (a few cases). Therefore, we focused on the fact that most of the electrostatic precipitators are idle and the efficiency of the equipment is extremely poor. This electric dust collector is intended to collect locally generated dust gas from gutters, hot metal slag pits, etc. The reason why this method is possible is that while abnormal dust generation occurs at the beginning or end of the tapping process, lap tapping is carried out in such a way that abnormal dust generation does not occur at the same time. That is, since one of the dust collectors is idle, even if abnormal dust generation occurs, dust collection is possible by diverting the locally generated dust gas generated at the same time to the other electrostatic precipitator. In addition, since the local dust generation air volume during normal tapping and the abnormal dust generation air volume are about the same,
It is possible to process both dust gases without significantly increasing the capacity of conventional building electric precipitators.

しかしてこの局所発塵ガスは、本発明によれば
小型の排風機で吸引後建家天井部に設置した電気
集塵機下部まで集塵ダクトで導きダクト末端に設
けたノズルで均等に放散し、その後は煙の自然通
風力で電気集塵機で集塵するものである。この場
合例えば異状発塵が末期で発生した場合、当該出
銑口の直上の電気集塵機でその異状発塵ガスを処
理するとともにこの時の同系統の局所発塵ガスは
他方の遊んでいる電気集塵機へ導き処理する。
However, according to the present invention, the locally generated dust gas from the lever is sucked in by a small exhaust fan, then guided through a dust collection duct to the bottom of the electric dust collector installed on the ceiling of the building, and then evenly dispersed by a nozzle installed at the end of the duct. The dust is collected using an electric precipitator using the natural draft of smoke. In this case, for example, if abnormal dust generation occurs at the final stage, the abnormal dust generation gas will be treated with the electrostatic precipitator directly above the tap hole, and the local dust generation gas in the same system will be collected by the other idle electrostatic precipitator. to be processed.

これにより通常出銑時の局所発塵ガスと異状発
塵ガスを建家電気集塵機で処理可能となる。この
場合局所発塵ガスは排風機を必要とするが、バグ
フイルターを必要としないことと、集塵ダクト長
さが従来の約半分ですむことから圧力損失は100
〜50m/mAqとなり小型の排風機でよいことにな
る。又電気集塵機の電力費が小さいことから従来
のシステムに比べ大幅な電力費の削減が可能とな
り省エネルギーに寄与すること大なるものがあ
る。又設備費も従来タイプ、および改良型に比べ
半分ですむ。さらには地上に排風機及びバグフイ
ルターを設置しなくてすむため高炉周辺の敷地の
有効利用がはかれる。
This makes it possible to treat local dust gas and abnormal dust gas during normal tapping with the building electric precipitator. In this case, locally generated dust gas requires an exhaust fan, but since there is no need for a bag filter and the length of the dust collection duct is about half that of the conventional one, the pressure loss is 100%.
~50m/mAq, which means that a small exhaust fan is sufficient. Furthermore, since the electricity cost of the electrostatic precipitator is small, it is possible to significantly reduce the electricity cost compared to conventional systems, which greatly contributes to energy conservation. The equipment cost is also half that of the conventional type and improved type. Furthermore, since there is no need to install an exhaust fan or bag filter above ground, the site around the blast furnace can be used more effectively.

以下本発明の実施例を図面により詳しく説明す
る。
Embodiments of the present invention will be described in detail below with reference to the drawings.

第3図及び第4図において11は高炉である。
この高炉は2つの出銑口12a,12bを有す
る。13は局所集塵用のフード(又はカバー)
で、出銑口、大樋、スキンマー、溶銑溶滓樋、溶
銑溶傾注樋等から通常の出銑時に発生する発塵を
集塵する。14a,14bは、この各フード13
に連結した集塵ダクトで、このダクト14a,1
4bの後端は鋳床上に設置した小型の排風機15
に接続する。この排風機15には更に集塵ダクト
16a,16bが接続され、他端は建家17上に
搭載した電気集塵機18a,18bの下に位置し
ている。この電気集塵機18a,18bは出銑口
12a,12bの数に対応して2基設けられ、
夫々出銑口の直上に設けることが望ましい。上記
電気集塵機18a,18bの下に位置する集塵ダ
クト16a,16bの水平部には集塵ガスの分配
ノズル19を多数個電気集塵機18a,18bに
向けて設ける。第5図に於いて20はノズル19
上に設けた遮へい板、21はノズル19の両側に
配置したシユート、22は排水樋である。電気集
塵機18a,18b内の上部より間歇的に噴射さ
れるダスト洗浄水はノズル19に侵入せずに排水
樋22から流出する。第3図に於いて23は集塵
ダクト16aと16bとを連結する連結ダクト
で、この連結ダクト23内には24、集塵ダクト
16a,16b内には連結ダクト23の夫々両側
に25,26及び27,28の切替ダンバーを設
ける。而して異状発塵時の発塵ガスは熱上昇気流
によつて建家天井部まで舞上つて、第5図に於い
て29で示す如く上昇し電気集塵機18a,18
bにより集塵されるようになつている。一方通常
出銑時に発生する発塵ガスは各フード13により
捕集され、集塵ダクト14a,14b、排風機1
5及び集塵ダクト16a,16bを通つて電気集
塵機18a,18bの下へ導かれ、第5図に於い
て30で示す如く自然通風力によつて上昇し異状
発塵ガスと同時に電気集塵機18a,18bによ
り集塵されるようになつている。第4図において
31は建家内の換気を補強するための換気ギヤラ
リーを示している。尚、本発明をより効果的にす
るために、高炉本体と建家との接続部にジヤバ
ラ、ウオーター又はサンドシールを設けて密閉化
を計るとか、或いは外部からの鋳床内への横風防
止のために鋳床建家垂直部と鋳床面との間に、衝
立を設けることは有効な手段である。
In FIGS. 3 and 4, 11 is a blast furnace.
This blast furnace has two tap ports 12a and 12b. 13 is a hood (or cover) for local dust collection
The dust that is generated during normal tapping is collected from the taphole, large culvert, skimmer, hot metal slag trough, hot metal pouring trough, etc. 14a and 14b are each of these hoods 13
This duct 14a, 1
The rear end of 4b is a small exhaust fan 15 installed on the cast bed.
Connect to. Dust collection ducts 16a and 16b are further connected to this exhaust fan 15, and the other end is located below electric dust collectors 18a and 18b mounted on the building 17. Two electric precipitators 18a and 18b are provided corresponding to the number of tap holes 12a and 12b.
It is desirable to install each directly above the tap hole. A plurality of dust collecting gas distribution nozzles 19 are provided in the horizontal parts of the dust collecting ducts 16a, 16b located below the electric dust collectors 18a, 18b, facing the electric dust collectors 18a, 18b. In Fig. 5, 20 is the nozzle 19
A shielding plate provided above, 21 a chute disposed on both sides of the nozzle 19, and 22 a drainage gutter. The dust cleaning water that is intermittently injected from the upper part of the electrostatic precipitators 18a and 18b flows out from the drain gutter 22 without entering the nozzle 19. In FIG. 3, 23 is a connecting duct that connects the dust collecting ducts 16a and 16b, 24 is inside the connecting duct 23, and 25, 26 are inside the dust collecting ducts 16a and 16b on both sides of the connecting duct 23, respectively. and switching dampers 27 and 28 are provided. When the dust is abnormally generated, the dust gas rises up to the ceiling of the building due to the rising heat and rises as shown at 29 in FIG.
Dust is collected by b. On the other hand, dust gas generated during normal tapping is collected by each hood 13, dust collection ducts 14a, 14b, and exhaust fan 1.
5 and the dust collecting ducts 16a, 16b to the bottom of the electrostatic precipitators 18a, 18b, and as shown at 30 in FIG. Dust is collected by 18b. In FIG. 4, numeral 31 indicates a ventilation gear rally for reinforcing ventilation within the building. In order to make the present invention more effective, it is possible to provide a bellows, water or sand seal at the connection between the blast furnace main body and the building to ensure airtightness, or to prevent cross winds from entering the casthouse from outside. Therefore, it is an effective means to provide a screen between the vertical part of the casthouse building and the casthouse surface.

本発明の一実施例の構成は上記の通りであり、
先づ2つの出銑口12a,12bによる単独出銑
作業時の集塵作業を説明すると、出銑口12aか
らの出銑開始時の異状発塵及びその後の通常出銑
時の局所発塵は出銑口12aの直上にある電気集
塵機18aで集塵する。出銑口12aから出銑が
末期になり異状発塵と局所発塵が同時に起つた場
合には、異状発塵は出銑口12aの直上にある電
気集塵機18aで集塵するが局所発塵は18bの
電気集塵機で集塵する。即ち第3図における切替
ダンパー25,28を閉め中間ダンパー24を開
にすることにより集塵ガスは連結ダクト23を右
から左へ流れ18bの電気集塵機で集塵される。
出銑口12aから出銑が終了すれば、今度は出銑
口12bから出銑するが、その操作は上記の場合
と全く同一である。
The configuration of one embodiment of the present invention is as described above,
First, to explain the dust collection operation during individual tapping using the two tapholes 12a and 12b, the abnormal dust generation at the start of tapping from the taphole 12a and the local dust generation during the subsequent normal tapping are as follows. Dust is collected by an electric precipitator 18a located directly above the tap hole 12a. When tapping from the tap hole 12a reaches the final stage and abnormal dust generation and local dust generation occur at the same time, the abnormal dust generation is collected by the electrostatic precipitator 18a located directly above the tap hole 12a, but the local dust generation is Collect dust using an electric precipitator No. 18b. That is, by closing the switching dampers 25 and 28 in FIG. 3 and opening the intermediate damper 24, the dust collecting gas flows through the connecting duct 23 from right to left and is collected by the electrostatic precipitator 18b.
Once the tapping from the taphole 12a is completed, the taphole is then tapped from the taphole 12b, but the operation is exactly the same as in the above case.

次にラツプ出銑作業時の集塵作業を説明すると
出銑口12aからの出銑開始時の異状発塵及びそ
の後の局所発塵、並び末期の異状発塵は出銑口1
2aの直上の電気集塵機18aで集塵し、末期の
局所発塵は切替ダンパー25,28を閉め中間ダ
ンパー24を開にして18bの電気集塵機で集塵
する。出銑口12aからの出銑にラツプして出銑
口12bからの出銑が開始されると、出銑開始時
の異状発塵及びその後の局所発塵並びに末期の異
状発塵は出銑口12bの直上の電気集塵機18b
で集塵し、末期の異状発塵と同時に発生する末期
の局所発塵は切替ダンパー27,26を閉め中間
ダンパー24を開にして18aの電気集塵機で集
塵する。この場合、出銑口12aからの末期の局
所発塵と、出銑口12bからの出銑開始後の局所
発塵の双方は18bの電気集塵機で同時にラツプ
集塵することになるが、電気集塵機の容量として
は、このラツプ集塵と異状発塵の集塵とを比較し
て風量の大きい方を基準にして設計する。
Next, to explain the dust collection work during lap tapping work, abnormal dust generation at the start of tapping from the tap hole 12a, local dust generation after that, and abnormal dust generation at the end of the tap hole 1
Dust is collected by an electric precipitator 18a directly above 2a, and in the final stage of local dust generation, the switching dampers 25 and 28 are closed, the intermediate damper 24 is opened, and the dust is collected by an electric precipitator 18b. When tapping from the taphole 12b starts after tapping from the taphole 12a, abnormal dust generation at the start of tapping, local dust generation after that, and abnormal dust generation at the end are caused by the taphole. Electrostatic precipitator 18b directly above 12b
The terminal stage localized dust generation that occurs simultaneously with the terminal stage abnormal dust generation is collected by the electrostatic precipitator 18a by closing the switching dampers 27 and 26 and opening the intermediate damper 24. In this case, both the localized dust generation from the taphole 12a at the final stage and the localized dust generation after the start of tapping from the taphole 12b are lap-collected at the same time by the electrostatic precipitator 18b, but the electrostatic precipitator The capacity is designed based on the larger air volume by comparing this lap dust collection and abnormal dust collection.

上記の実施例は、出銑口2個の場合に電気集塵
機2基の例を示したが、例えば第6図、第7図に
示した如く出銑口及び電気集塵機が増加した場合
にも本発明が実施できる。この例では電気集塵機
の基数は出銑口の数に対応しているが、出銑口、
大樋、傾注樋等のレイアウトを変更し、又建家上
部でのたれ幕、仕切壁の設置等により電気集塵機
の基数の減少を計ることは可能である。
The above embodiment shows an example in which two electrostatic precipitators are used in the case of two tapholes, but this can also be applied when the number of tapholes and electrostatic precipitators is increased, as shown in Figs. 6 and 7, for example. The invention can be put into practice. In this example, the radix of the electrostatic precipitator corresponds to the number of tapholes;
It is possible to reduce the number of electrostatic precipitators by changing the layout of large gutters, tilting gutters, etc., and by installing hanging curtains and partition walls above the building.

以上詳述した如く、本発明は1次集塵系である
通常出銑時の発塵ガスと、2次集塵系である出銑
口からの異状発塵ガスを全て建家直接搭載型電気
集塵機で集塵するようにしたので、従来型及びそ
の改良型集塵システムに比べて、大幅な運転費の
削減が可能となり、省エネルギーに大きく寄与す
るものである。
As described in detail above, the present invention is designed to collect all the dust gas generated during normal tapping, which is the primary dust collection system, and the abnormal dust gas from the taphole, which is the secondary dust collection system, by using an electric appliance directly mounted on the building. Since dust is collected using a dust collector, operating costs can be significantly reduced compared to conventional and improved dust collection systems, which greatly contributes to energy conservation.

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

第1図、第2図は従来方式の説明図、第3図〜
第7図は本発明の実施例を示し、第3図は全体説
明図、第4図は第3図の側面図、第5図は集塵ダ
クトの水平部に設けた発塵ガス分配ノズル部の詳
細図、第6図及び第7図は、第3図及び第4図に
示した他のレイアウトの平面図である。 11…高炉、12a,12b,12c,12d
…出銑口、13…フード又はカバー、14a,1
4b,16a,16b…集塵ダクト、15…排風
機、17…建家、18a,18b,18c,18
d…電気集塵機、19…分配ノズル、23…連結
ダクト、24〜28…切替ダンパー。
Figures 1 and 2 are explanatory diagrams of the conventional method, and Figures 3~
Fig. 7 shows an embodiment of the present invention, Fig. 3 is an overall explanatory view, Fig. 4 is a side view of Fig. 3, and Fig. 5 is a dust gas distribution nozzle section provided in the horizontal part of the dust collection duct. 6 and 7 are plan views of the other layouts shown in FIGS. 3 and 4. 11...Blast furnace, 12a, 12b, 12c, 12d
...Tackle mouth, 13...Hood or cover, 14a, 1
4b, 16a, 16b...dust collection duct, 15...exhaust fan, 17...building, 18a, 18b, 18c, 18
d...Electrostatic precipitator, 19...Distribution nozzle, 23...Connection duct, 24-28...Switching damper.

Claims (1)

【特許請求の範囲】[Claims] 1 高炉の建家上に複数基の電気集塵機を搭載
し、一方複数の出銑口毎の通常出銑時の発塵個所
に集塵フード又はカバーを設置し、このフード又
はカバーと上記電気集塵機の下方部とを排風機を
介して集塵ダクトにより連結すると共に電気集塵
機の下方部に位置する集塵ダクトに合塵ガスの分
配ノズルを設け、更に各集塵ダクトを切替弁を有
する連結ダクトにより連結したことを特徴とする
高炉鋳床集塵設備。
1 Multiple electrostatic precipitators are installed on the blast furnace building, and a dust collection hood or cover is installed at the point where dust is generated during normal tapping for each of the multiple tap holes, and this hood or cover and the above electrostatic precipitator are installed. A dust collection duct is connected to the lower part of the electrostatic precipitator via an exhaust fan, and a dust collection duct located at the lower part of the electrostatic precipitator is provided with a distribution nozzle for the combined dust gas, and each dust collection duct is connected to a connecting duct with a switching valve. Blast furnace casthouse dust collection equipment characterized by being connected by.
JP56116707A 1981-07-25 1981-07-25 Dust collecting installation for hearth of blast furnace Granted JPS5819418A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56116707A JPS5819418A (en) 1981-07-25 1981-07-25 Dust collecting installation for hearth of blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56116707A JPS5819418A (en) 1981-07-25 1981-07-25 Dust collecting installation for hearth of blast furnace

Publications (2)

Publication Number Publication Date
JPS5819418A JPS5819418A (en) 1983-02-04
JPS6140004B2 true JPS6140004B2 (en) 1986-09-06

Family

ID=14693829

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56116707A Granted JPS5819418A (en) 1981-07-25 1981-07-25 Dust collecting installation for hearth of blast furnace

Country Status (1)

Country Link
JP (1) JPS5819418A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2608928B2 (en) * 1988-07-01 1997-05-14 松下電器産業株式会社 Machine tool
JPH0215937A (en) * 1988-07-01 1990-01-19 Matsushita Electric Ind Co Ltd Machine tool
JP2506977B2 (en) * 1988-08-17 1996-06-12 松下電器産業株式会社 Machine tool
GR1001117B (en) * 1989-02-06 1993-04-28 Kloeckner Stahl Gmbh Method for avoiding the creation of combustion gases in metallurgical processes of liquid metals from a metallurgical pot in an effusion pot and mechanic arrangement therefor

Also Published As

Publication number Publication date
JPS5819418A (en) 1983-02-04

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