JPS5987016A - Dust removing device of blast furnace - Google Patents

Dust removing device of blast furnace

Info

Publication number
JPS5987016A
JPS5987016A JP19734682A JP19734682A JPS5987016A JP S5987016 A JPS5987016 A JP S5987016A JP 19734682 A JP19734682 A JP 19734682A JP 19734682 A JP19734682 A JP 19734682A JP S5987016 A JPS5987016 A JP S5987016A
Authority
JP
Japan
Prior art keywords
dust
gas
blast furnace
hopper
removing device
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
JP19734682A
Other languages
Japanese (ja)
Inventor
Minoru Kosugi
小杉 實
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 JP19734682A priority Critical patent/JPS5987016A/en
Publication of JPS5987016A publication Critical patent/JPS5987016A/en
Pending legal-status Critical Current

Links

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)
  • Blast Furnaces (AREA)

Abstract

PURPOSE:To prevent the dust generation during dust delivery and the leakage of noxious gas, by a method a reticulated partition plate is provided in a dust storage hopper while rising gas is blown into said hopper to fluidize the stored dust which is, in turn, delivered by the internal pressure of a dust removing device. CONSTITUTION:A porous plate 11 is provided to the lower part of the dust storage hopper 5 of a gravitational precipitation type dust removing device 3 and inert gas from a system 12 or gas obtained by compressing the gas generated from a blast furnace and subjected to dust removal by a secondary dust collector is introduced into the hopper to fluidize the stored dust. When dust is delivered, a cut-off valve 14 of a dust delivery pipe 13 is opened and dust is delivered to a dispersing device 15 at high concn. by the pressure in the dust removing device 3. High pressure gas is blown into the dispersing device 15 from a system 16 to dilute the high concn. dust and the diluted dust is conveyed to a sintering factory for re-utilizing the dust in a solid-gas two-phase stream through a conveying pipe 17. In order to prevent a large lumpy charged stock material accompanied by furnace top gas from being mixed in the delivery pipe 13 when abnormal blowing-through is generated during the operation of the blast furnace, a reticulated partition plate 10 is provided in the hopper 5 and the large lump is taken out from a manhole 18 during the idle time of the blast furnace.

Description

【発明の詳細な説明】 本発明はダスト切出機構葡有した溶鉱炉の重力沈降式除
展器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a gravity settling type deexpanding device for a blast furnace having a dust cutting mechanism.

第1図は従来の除り器にあって、(ハ)部に貯蔵された
ダストの切出方法の一例を示している。溶鉱炉の炉頂で
発生するカスは装入原料の粉り全多量に含みダウンカマ
ー1を通シ除塵器3に入る。炉頂ガスはダウンカマーl
に後続する拡り管2の下端開放部で流れ方向を反転し低
速で除雇器3内を上昇し除厘器出口管4全通ってベンチ
ュリースクラバー、或いは電気集献器等の二次集塵装置
へ導かれるっ炉頂ガスに同伴される大半のダストは除鵬
器内でその流れ方向會反転する時に比重差によシ炉頂ガ
スより分離され除践器下部のダスト貯蔵ホッパー5円に
堆積する。該ホッパー内のダストは通常、溶鉱炉操業中
に定期的(一般に1日に1〜3回)にダスト切出管6V
′−設置される遮断弁7゜8を開き電動機により回転す
る旋回板を内蔵するバッグミル9を介してトラック(又
は貨車)へ切出され、ダス)k再利用する所定の場所(
例えは焼結工場やペレット工場)へ運はれる。
FIG. 1 shows an example of a method for cutting out dust stored in section (C) of a conventional remover. The scum generated at the top of the blast furnace is included in the total amount of powder of the charged raw material and passes through the downcomer 1 and enters the dust remover 3. Furnace top gas is downcomer
The flow direction is reversed at the lower end open part of the expanding pipe 2 following the flow, and the flow rises at a low speed inside the eliminator 3, passes through the entire eliminator outlet pipe 4, and is used for secondary dust collection such as a Venturi scrubber or an electric concentrator. Most of the dust entrained in the top gas led to the device is separated from the top gas due to the difference in specific gravity when the flow direction is reversed in the dust remover and stored in a dust storage hopper at the bottom of the dust remover. accumulate. The dust in the hopper is normally removed from the dust cutting pipe 6V periodically (generally 1 to 3 times a day) during blast furnace operation.
' - The installed shutoff valve 7°8 is opened, and the bag mill 9, which has a built-in turning plate rotated by an electric motor, is cut into a truck (or freight car) and placed at a predetermined place for reuse.
For example, it is transported to a sintering factory or a pellet factory).

従来の装置にあっては、作業面ではトラックへダストを
入れる時に粉層が発生し、でらにはトラックで輸送する
途中でも発展し、作業環境上問題があった。切出作業に
は数人の作業員を必要とじ発塵環境であると同時に有毒
な炉頂ガスが漏れる危険環境であることから安全衛生上
、省力化上も問題があった。設備面ではダスト切出装置
の下にトランクが入れるようなスペースを確保する必要
があることから除塵器本体3を地上よシか”tシ高く設
置しなければならず設備費が萬くなっている。
With conventional equipment, a layer of powder is generated when the dust is loaded into the truck, and it also develops during transport by truck, posing problems in the working environment. The cutting work required several workers, creating a dust-producing environment as well as a dangerous environment where toxic furnace top gas leaked, posing problems in terms of health and safety as well as labor-saving. In terms of equipment, it is necessary to secure a space for the trunk to fit under the dust extraction device, so the dust remover main body 3 has to be installed high above the ground, which increases the equipment cost by 10,000 yen. There is.

又、時々溶鉱炉の吹抜は等により天真の装入原料が除塵
器内に混入しダスト切出装置に詰ったシ、水分の影WE
よシ貯蔵ホンパー5内でダストが棚吊シ現Ji起したり
してダスト切出が不能になることもある。
In addition, sometimes in the blast furnace stairwell, the raw materials charged in the blast furnace get mixed into the dust remover and clog the dust removal device, and the shadow of moisture is generated.
In some cases, the dust may hang on the shelf in the storage pumper 5, making it impossible to cut out the dust.

本発明は従来式のか\る問題点を解決するために提供書
れたもので以下第2図で本発明を説明する0 ダスト貯蔵ホッパー5の下部に多孔板lユ?配設し、そ
の中心にダスト切出管13を設ける。多孔板11の下部
室に不活性ガス(例えば蟹素ガス等)又は本除路器の後
流に設置される二次集塵装置にて除塵された溶鉱炉発生
ガスを昇圧したガスを系12より導入する。これらの不
活性ガス又は溶鉱炉発生ガスは多孔板11葡通過して貯
、蔵ダストを流動化させながら上昇する。ダストを切出
す時は、ダスト切出管13に設置される遮断弁14ケ開
き除塵器3内の圧力でダストを筒濃度で分散器15に切
出す。次にこの分散器15に接続している系16よシ高
圧気体が分LR15に吹込まれ尚湿度ダストを稀釈し固
気二相流にして搬送管1’7盆経田してダスト〒再利用
する焼結工場又はペレットエ楊等の所定の場所迄搬送す
る。
The present invention has been proposed to solve the problems of the conventional method, and the present invention will be explained below with reference to FIG. A dust cutting pipe 13 is provided at the center of the pipe. In the lower chamber of the perforated plate 11, an inert gas (for example, crab gas, etc.) or a pressurized blast furnace generated gas, which has been removed by a secondary dust collector installed downstream of the main clearing device, is supplied from the system 12. Introduce. These inert gases or blast furnace generated gases pass through the perforated plate 11, are stored, and rise while fluidizing the stored dust. When cutting out dust, the shutoff valve 14 installed in the dust cutting pipe 13 is opened, and the dust is cut out at a cylinder concentration into the disperser 15 by the pressure inside the dust remover 3. Next, high-pressure gas is blown into the LR 15 through the system 16 connected to this disperser 15, which dilutes the humidity dust and turns it into a solid-gas two-phase flow, which is then transferred to the conveyor pipe 1'7 to reuse the dust. Transport it to a predetermined location such as a sintering factory or pellet factory.

溶鉱炉の操業においては、時々異常吹抜けを起すことか
ありこの時に大塊の装入原料が炉頂ガスに同伴し除厖器
に入ることがある。このような大塊物は労柩器15や搬
送管l’7を閉塞きせる危険住があるためこれン防止す
るため(で大塊物が切出’113rζ混入しないようダ
スト貯蔵ホッパー5内に網目状の仕切板10を内設する
。本仕切板上に堆積した大塊は溶鉱炉の定期的な休風時
にマンホール18から防塁器外へ取出すことが出来る。
During the operation of a blast furnace, abnormal blow-through may occur from time to time, and at this time, a large lump of charging material may be entrained in the furnace top gas and enter the deburrer. Such large lumps pose a danger of clogging the labor coffin 15 and the transport pipe l'7, so to prevent this, a mesh is installed in the dust storage hopper 5 to prevent large lumps from getting mixed in. A partition plate 10 having the shape of a shape is provided inside.The large lumps accumulated on the partition plate can be taken out from the manhole 18 to the outside of the embankment when the blast furnace is periodically shut down.

本発明による除塵器はダスト切出時の発展や有毒ガスの
漏洩を完全に防止出来、トラックや貨車によるダスト運
搬を排除出来ることがら作業環境の改善、大気汚染防止
、省力化、運搬費用の削減が可能となり、さらに防塵器
下部のトラック搬入スペースを削減することにより除展
器の地上からの高さを下げることが出来、設備費の削減
が可能となることから極めて有効な装置である。
The dust remover according to the present invention can completely prevent the development of dust during extraction and the leakage of toxic gases, and can eliminate the need to transport dust by trucks and freight cars, thereby improving the working environment, preventing air pollution, saving labor, and reducing transportation costs. This is an extremely effective device as it enables the removal of dust from the ground, and by reducing the space required to carry the truck in at the bottom of the dustproof device, the height of the de-expanding device from the ground can be lowered, thereby reducing equipment costs.

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

第1図は従来一般に採用されている溶鉱炉除塵器のダス
ト切出方法の一例を示す図。第2図は本発明による浴鉱
炉除塵器?示す図でおる。 1・・・・・・ダウンカマー 2・・・・・・拡り管 3・・・ ・・・除塵器 4・・ ・・・・除頭出口管 5・ ・・ ・・ダスト貯蔵ホッパー 6.13  ・・・ ダス1、切出雪・7.8.14・
 ・遮断弁 10・・・・・仕切板 Jl・・・・・多孔板 12.16・・・ガス糸 出 願 人 新日本製鐵株式会社
FIG. 1 is a diagram showing an example of a dust removal method of a blast furnace dust remover that has been generally employed in the past. Figure 2 shows the bath ore furnace dust remover according to the present invention? This is the diagram shown. 1... Downcomer 2... Expansion pipe 3... Dust remover 4... ... Head removal outlet pipe 5... Dust storage hopper 6. 13... Das 1, cut snow・7.8.14・
・Shutoff valve 10...Partition plate Jl...Perforated plate 12.16...Gas thread Applicant Nippon Steel Corporation

Claims (1)

【特許請求の範囲】[Claims] 重力沈降式除展器のダスト貯蔵ホッパー同に、網目状の
仕切板を設け、且つ該ホッパー下部より昇圧した溶鉱炉
先生ガス又は不活性ガス金層込み、貯蔵ダスHr流動化
せしめながら、除塵器内圧力によシダスIf切出し、更
に該切出し部に搬送用気体吹込み口を形成し、該気体に
よ−り所定の場所迄ダストを搬送する如くなしたことを
特徴とする溶鉱炉除塵器
A mesh-like partition plate is installed in the dust storage hopper of the gravity settling type deexpanding device, and the blast furnace gas or inert gas, which is pressurized from the bottom of the hopper, is filled with a gold layer, and the stored dust Hr is fluidized while inside the dust remover. A blast furnace dust remover, characterized in that the dust is cut out by pressure, and furthermore, a conveying gas inlet is formed in the cut out part, and the dust is conveyed to a predetermined location by the gas.
JP19734682A 1982-11-10 1982-11-10 Dust removing device of blast furnace Pending JPS5987016A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19734682A JPS5987016A (en) 1982-11-10 1982-11-10 Dust removing device of blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19734682A JPS5987016A (en) 1982-11-10 1982-11-10 Dust removing device of blast furnace

Publications (1)

Publication Number Publication Date
JPS5987016A true JPS5987016A (en) 1984-05-19

Family

ID=16372946

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19734682A Pending JPS5987016A (en) 1982-11-10 1982-11-10 Dust removing device of blast furnace

Country Status (1)

Country Link
JP (1) JPS5987016A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04110122U (en) * 1991-03-12 1992-09-24 日立造船株式会社 Dust discharge device for blast furnace gas dry dust collection equipment
JPH04278181A (en) * 1991-03-01 1992-10-02 Nippon Steel Corp Dust collecting and dust treating device
JPH04281814A (en) * 1991-03-12 1992-10-07 Hitachi Zosen Corp Method and device for discharging dust of blast furnace gas dry type dust collecting equipment
CN102974178A (en) * 2012-11-07 2013-03-20 深圳市海众热源技术有限公司 Ash discharging device with frame arch destructor
CN104729886A (en) * 2013-12-18 2015-06-24 宝山钢铁股份有限公司 Water-dust-oil automatic separation device for gas sampling
CN109625648A (en) * 2018-12-12 2019-04-16 西安美克森科技工程有限公司 Ash bucket for electrostatic and bag-type dust removal system is anti-blocking to exempt from tracing system
CN109897926A (en) * 2017-12-11 2019-06-18 上海梅山钢铁股份有限公司 Blast furnace gravitational dust collection apparatus for ash

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04278181A (en) * 1991-03-01 1992-10-02 Nippon Steel Corp Dust collecting and dust treating device
JPH04110122U (en) * 1991-03-12 1992-09-24 日立造船株式会社 Dust discharge device for blast furnace gas dry dust collection equipment
JPH04281814A (en) * 1991-03-12 1992-10-07 Hitachi Zosen Corp Method and device for discharging dust of blast furnace gas dry type dust collecting equipment
CN102974178A (en) * 2012-11-07 2013-03-20 深圳市海众热源技术有限公司 Ash discharging device with frame arch destructor
CN104729886A (en) * 2013-12-18 2015-06-24 宝山钢铁股份有限公司 Water-dust-oil automatic separation device for gas sampling
CN109897926A (en) * 2017-12-11 2019-06-18 上海梅山钢铁股份有限公司 Blast furnace gravitational dust collection apparatus for ash
CN109625648A (en) * 2018-12-12 2019-04-16 西安美克森科技工程有限公司 Ash bucket for electrostatic and bag-type dust removal system is anti-blocking to exempt from tracing system

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