JP2587750B2 - Dust treatment method for blast furnace dry dust collector - Google Patents

Dust treatment method for blast furnace dry dust collector

Info

Publication number
JP2587750B2
JP2587750B2 JP4137619A JP13761992A JP2587750B2 JP 2587750 B2 JP2587750 B2 JP 2587750B2 JP 4137619 A JP4137619 A JP 4137619A JP 13761992 A JP13761992 A JP 13761992A JP 2587750 B2 JP2587750 B2 JP 2587750B2
Authority
JP
Japan
Prior art keywords
dust
gas
blast furnace
dust collector
dry
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 - Lifetime
Application number
JP4137619A
Other languages
Japanese (ja)
Other versions
JPH05311222A (en
Inventor
清 清水
博文 尾上
裕次 北村
雅彦 浜田
保彦 尾松
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.)
NITSUTETSU PURANTO SETSUKEI KK
Nippon Steel Corp
Original Assignee
NITSUTETSU PURANTO SETSUKEI KK
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 NITSUTETSU PURANTO SETSUKEI KK, Nippon Steel Corp filed Critical NITSUTETSU PURANTO SETSUKEI KK
Priority to JP4137619A priority Critical patent/JP2587750B2/en
Publication of JPH05311222A publication Critical patent/JPH05311222A/en
Application granted granted Critical
Publication of JP2587750B2 publication Critical patent/JP2587750B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • Y02A50/2351Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust

Landscapes

  • Blast Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は高炉用の乾式集塵装置で
捕集したダストの処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating dust collected by a dry dust collector for a blast furnace.

【0002】[0002]

【従来の技術】従来高炉乾式集塵装置で捕集したダスト
は、特開昭59−59234号公報で示される如く均圧
弁、排圧弁を備えた中間ホッパーを集塵機のホッパーの
下部に設け、高圧の高炉ガスをシールしながら排出して
いた。しかし、中間ホッパーやその上下に均排圧するた
めの遮断弁や切出し用のロータリーバルブ等を設けてい
るため、集塵装置全体の背が高くなると共に、バルブや
ロータリーバルブ等の可動部分が多く、操作及びメンテ
ナンスも複雑なものとなっている。
2. Description of the Related Art Conventionally, dust collected by a blast furnace dry dust collector is provided with an intermediate hopper provided with a pressure equalizing valve and an exhaust pressure valve below the hopper of the dust collector as disclosed in Japanese Patent Application Laid-Open No. 59-59234. Was discharged while sealing the blast furnace gas. However, since the intermediate hopper and the shut-off valve for equalizing the pressure above and below it and a rotary valve for cutting out are provided, the height of the entire dust collector is increased, and many movable parts such as valves and rotary valves are provided. Operation and maintenance are also complicated.

【0003】そこで本発明者等は、メンテナンスをほと
んど必要としないダスト輸送装置を備えた高炉用乾式集
塵装置を開発し、実開昭62−144524号公報で、
またその改善策を実開平1−174026で紹介した。
その高炉乾式集塵装置で捕集されたダストはセメントの
原料等に再利用されるが、そのまま使用するとCl,N
a、K分が多く再利用生産物の品質に影響を与えるの
で、乾式集塵装置で捕集したダストを水洗しその後脱水
処理をして使用しているのが現状である。
Accordingly, the present inventors have developed a dry dust collector for a blast furnace equipped with a dust transport device requiring little maintenance, and disclosed in Japanese Utility Model Laid-Open No. 62-144524.
The improvement measures were introduced in Japanese Utility Model Laid-Open No. 1-174026.
The dust collected by the blast furnace dry dust collector is reused as raw material for cement, etc.
Since the amount of a and K is large and affects the quality of the recycled product, the dust collected by a dry dust collector is washed with water and then dewatered before use.

【0004】図3はその機器構成を示すもので高炉1で
発生した排ガスは、粗集塵機2で比較的粒径の大きなダ
ストが除去された後、複数並列された乾式集塵機3に搬
送される。乾式集塵機3の下部ホッパー4には、ダスト
切出し弁5及びダスト切出し管6が設けられており、そ
の出口はダスト輸送管7を介してダストホッパー8に接
続されている。
FIG. 3 shows the configuration of the apparatus. Exhaust gas generated in the blast furnace 1 is conveyed to a plurality of parallel dry dust collectors 3 after dust having a relatively large particle size is removed by a coarse dust collector 2. A dust extraction valve 5 and a dust extraction pipe 6 are provided in a lower hopper 4 of the dry dust collector 3, and the outlet thereof is connected to a dust hopper 8 via a dust transport pipe 7.

【0005】そして、乾式集塵機3から出口ガス管9を
経て排出されたガスの一部を、昇圧ブロア10及びキャ
リアガス配管11を介してダスト輸送管7に吹込んでい
る。このガスはキャリアガスとして働き、乾式集塵機3
で捕集されたダストをダストホッパー8にスムーズに気
流搬送する。
[0005] A part of the gas discharged from the dry dust collector 3 through the outlet gas pipe 9 is blown into the dust transport pipe 7 through the pressurizing blower 10 and the carrier gas pipe 11. This gas acts as a carrier gas and is used as a dry dust collector 3
The dust collected in the step is smoothly transported to the dust hopper 8 by airflow.

【0006】該ダストホッパーに搬送されたダストは上
部に設けられた乾式のダスト分級機12(例えばバグフ
ィルター)でキャリアガスから分離され、下部に設けら
れたダスト排出弁13により系外に排出される。排出時
には発塵を伴うのでそれを防止するため、加湿機14で
適度の水分が添加され、その後、スラリーピット15に
て洗浄水が給水され捕集ダスト中のCl,Na,K分等
を水洗する。スラリーピット15にてスラリー状になっ
たダストはスラリーポンプ16にて脱水装置17へと送
られる。
The dust conveyed to the dust hopper is separated from the carrier gas by a dry dust classifier 12 (eg, a bag filter) provided at an upper portion, and is discharged out of the system by a dust discharge valve 13 provided at a lower portion. You. During discharge, dust is generated. To prevent this, an appropriate amount of water is added by the humidifier 14, and then washing water is supplied at the slurry pit 15 to wash the Cl, Na, and K components in the collected dust. I do. The dust turned into a slurry in the slurry pit 15 is sent to a dewatering device 17 by a slurry pump 16.

【0007】一方、乾式集塵機で洗浄化された高炉ガス
はタービン18にてそのエネルギーを回収され清浄ガス
管20を経て次工程へ送られる。符号19はタービン1
8が稼動しない時の高炉の炉頂圧を制御する炉頂圧制御
弁、21はキャリアガスの流量を制御するキャリアガス
流量調整弁を示す。
On the other hand, the energy of the blast furnace gas cleaned by the dry dust collector is recovered by the turbine 18 and sent to the next step through the clean gas pipe 20. Reference numeral 19 denotes the turbine 1
Reference numeral 21 denotes a furnace top pressure control valve for controlling the furnace top pressure of the blast furnace when the furnace 8 does not operate, and reference numeral 21 denotes a carrier gas flow control valve for controlling the flow rate of the carrier gas.

【0008】図4は乾式のダスト分級機12としてバグ
フィルターを使用した場合の例で、ホッパー部分の結露
に対するダスト付着を防止するための保温材30、排出
部の棚吊り防止装置22、及びダスト排出終了後のガス
リーク防止のための遮断弁23等が必要となる。
FIG. 4 shows an example in which a bag filter is used as the dry dust classifier 12, and a heat insulating material 30 for preventing dust from adhering to dew condensation on the hopper portion, a shelving prevention device 22 for a discharge section, and a dust filter. A shutoff valve 23 and the like for preventing gas leakage after the discharge is completed are required.

【0009】[0009]

【発明が解決しようとする課題】上述した従来の機器構
成では、ダスト排出時の発塵を完全に押さえられなく且
つ、高炉ガスのリークも完全に防げないので環境対策上
好ましくないという問題点があった。更に機器構成も複
雑であり設備費、運転費共に高い上に、ダストを取扱う
回転機器がありそのメンテナンスが煩わしいという問題
点もあった。そこで本発明は上記の問題点を解決するこ
とを目的としている。
However, the above-mentioned conventional equipment configuration has a problem that dust generation at the time of dust discharge cannot be completely suppressed and a blast furnace gas leak cannot be completely prevented. there were. Further, the equipment configuration is complicated, the equipment cost and the operation cost are high, and there is a problem that there is a rotating equipment for handling dust and the maintenance is troublesome. Therefore, an object of the present invention is to solve the above problems.

【0010】[0010]

【課題を解決するための手段】本発明は前記課題を解決
するものであって、高炉から発生するガスを乾式集塵装
置にて除塵した後、タービンにてその発生ガスのエネル
ギーを回収する高炉ガスエネルギー回収装置における乾
式集塵装置で捕集したダストの処理方法であって、前記
乾式集塵装置の下部ホッパーとタービン出側の清浄ガス
管とを気流輸送管で接続し、その途中に湿式のダスト分
級機を設置し、該湿式ダスト分級機にて乾ダストを気流
より分離すると共に、ダストの洗浄を行いスラリーとし
て系外に排出することを特徴とする高炉乾式集塵装置の
ダスト処理方法である。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to provide a blast furnace in which a gas generated from a blast furnace is dust-removed by a dry dust collector and then the energy of the generated gas is recovered by a turbine. A method for treating dust collected by a dry dust collector in a gas energy recovery device, wherein a lower hopper of the dry dust collector is connected to a clean gas pipe on a turbine outlet side by an air flow transport pipe, and a wet type A dust treatment method for a blast furnace dry dust collector, comprising: installing a dust classifier of the type, separating dry dust from an air stream by the wet dust classifier, washing the dust, and discharging the dust outside the system. It is.

【0011】[0011]

【作用】乾式集塵装置で捕集されたダストは乾式集塵装
置内の圧力とタービン出側配管内の圧力の差により気流
輸送管内を高炉ガスの一部と共に気流輸送される。その
気流輸送管の途中に湿式のダスト分級機を設置すること
により乾ダストは気流から分離されると共に洗浄されス
ラリーとなり系外に排出される。なお、スラリーは排出
部に貯留されながら排出されるので、ダスト分級機内の
ガスは水封され、発塵がないことはもとよりガスのリー
クも皆無の状態で排出される。
The dust collected by the dry dust collector is pneumatically transported together with part of the blast furnace gas in the pneumatic transport pipe due to the difference between the pressure in the dry dust collector and the pressure in the turbine outlet pipe. By installing a wet dust classifier in the middle of the airflow pipe, the dry dust is separated from the airflow and washed to be a slurry, which is discharged out of the system. Since the slurry is discharged while being stored in the discharge section, the gas in the dust classifier is sealed with water, and discharged without any dust generation or gas leakage.

【0012】[0012]

【実施例】図1は本発明の実施例を示す図で、前記した
図3の装置を本発明を実施するように改良した例であ
る。図1において乾式集塵機3の下部ホッパー4とター
ビン18の出側清浄ガス管20とをダスト輸送管7で接
続しその途中に気液接触装置25と気液分離装置26か
ら構成される湿式のダスト分級機を設けている。図2は
湿式のダスト分級機の詳細を示す図で気液接触装置25
の内部には洗浄ノズル24が設けられており水の供給配
管がなされている。
FIG. 1 is a view showing an embodiment of the present invention, which is an example in which the above-described apparatus of FIG. 3 is improved to carry out the present invention. In FIG. 1, the lower hopper 4 of the dry dust collector 3 and the outlet clean gas pipe 20 of the turbine 18 are connected by a dust transport pipe 7, and a wet dust composed of a gas-liquid contact device 25 and a gas-liquid separation device 26 A classifier is provided. FIG. 2 is a diagram showing details of a wet dust classifier, and is a gas-liquid contact device 25.
Is provided with a washing nozzle 24, and a water supply pipe is provided.

【0013】そこでダスト切出し弁5を開にすると集塵
機内のダストは乾式集塵機3の下部ホッパー4内の圧力
とタービン18の出側清浄ガス管20内の圧力差により
気流輸送管7を経て気液接触装置25へと気流輸送さ
れ、該気液接触装置にて洗浄ノズル24から散水された
洗浄水によりCl,Na,K分が洗浄されると共にダス
トは洗浄水中へと移行する。そのダストを含んだ洗浄水
は後段の気液分離装置26にて気流より分離され、スラ
リーとして系外へ排出されスラリーポンプ16にて脱水
装置17へと送られる。図2の湿式のダスト分級機の詳
細図に示すように気液分離装置26から内部のガスが系
外に洩れないように下部貯留水の水位を一定に保つべく
水位計31と補給水流量制御弁27を設けている。
When the dust extraction valve 5 is opened, the dust in the dust collector passes through the gas flow pipe 7 due to the difference between the pressure in the lower hopper 4 of the dry dust collector 3 and the pressure in the clean gas pipe 20 on the outlet side of the turbine 18. The gas is transported to the contact device 25 by air flow, and the Cl, Na, and K components are washed by the washing water sprayed from the washing nozzle 24 by the gas-liquid contact device, and the dust is transferred to the washing water. The cleaning water containing the dust is separated from the gas stream by a gas-liquid separator 26 at the subsequent stage, discharged out of the system as a slurry, and sent to a dehydrator 17 by a slurry pump 16. As shown in the detailed view of the wet dust classifier of FIG. 2, the water level meter 31 and the make-up water flow rate control to keep the level of the lower stored water constant so that the gas inside from the gas-liquid separator 26 does not leak out of the system. A valve 27 is provided.

【0014】なお、図1における符号10はダストの気
流輸送を円滑に行なわせるため、乾式集塵機3から出口
ガス管9を経て排出されたガスの一部をキャリアガスと
してキャリアガス配管11を介してダスト輸送管7に送
り込む昇圧ブロワーであるが、乾式集塵機3と湿式ダス
ト分級機の距離が短いときや、乾式集塵機内の圧力が高
い場合にはキャリアガス管11と共に省略することがで
きる。
In FIG. 1, reference numeral 10 designates a portion of the gas discharged from the dry dust collector 3 through the outlet gas pipe 9 as a carrier gas through a carrier gas pipe 11 in order to smoothly carry the air stream of the dust. The booster blower is fed into the dust transport pipe 7, but can be omitted together with the carrier gas pipe 11 when the distance between the dry dust collector 3 and the wet dust classifier is short or when the pressure inside the dry dust collector is high.

【0015】[0015]

【発明の効果】以上説明したように、本発明は乾式集塵
機のホッパーとタービン出側の清浄ガス管とを気流輸送
管で接続し、その途中に湿式のダスト分級機を設置する
という簡単な構造により、乾式集塵機で捕集したダスト
を洗浄し有害成分を除去すると共に発塵及び高炉ガスの
リークを皆無の状態で系外へ排出することができる。ま
た、装置構成が簡単なため、設備費、運転費を低減する
と共にダストを取扱う回転機器も無くメンテナンスもほ
とんど必要としない。
As described above, the present invention has a simple structure in which the hopper of the dry dust collector is connected to the clean gas pipe on the turbine outlet side by the pneumatic transport pipe, and a wet dust classifier is installed in the middle of the pipe. Accordingly, the dust collected by the dry dust collector can be washed to remove harmful components, and can be discharged out of the system without any dust generation and blast furnace gas leak. Further, since the apparatus configuration is simple, equipment costs and operation costs are reduced, and there is no rotating equipment for handling dust, so that almost no maintenance is required.

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

【図1】本発明の実施例を示す系統図FIG. 1 is a system diagram showing an embodiment of the present invention.

【図2】図1における湿式ダスト分級機の詳細を示す図FIG. 2 is a diagram showing details of a wet dust classifier in FIG. 1;

【図3】従来例を示す系統図FIG. 3 is a system diagram showing a conventional example.

【図4】図3におけるバグフィルター近傍の詳細を示す
FIG. 4 is a diagram showing details in the vicinity of a bag filter in FIG. 3;

【符号の説明】[Explanation of symbols]

1 高炉 2 粗集塵器 3 乾式集塵機 4 下部ホッパー 7 ダスト輸送管 10 昇圧ブロア 18 タービン 20 清浄ガス管 24 洗浄ノズル 25 気液接触装置 26 気液分離装置 27 補給水流量制御弁 DESCRIPTION OF SYMBOLS 1 Blast furnace 2 Rough dust collector 3 Dry dust collector 4 Lower hopper 7 Dust transport pipe 10 Booster blower 18 Turbine 20 Clean gas pipe 24 Washing nozzle 25 Gas-liquid contact device 26 Gas-liquid separation device 27 Supply water flow control valve

フロントページの続き (72)発明者 北村 裕次 福岡県北九州市戸畑区大字中原46−59 日鐵プラント設計株式会社内 (72)発明者 浜田 雅彦 愛知県東海市東海町5−3 新日本製鐵 株式会社 名古屋製鐵所内 (72)発明者 尾松 保彦 千葉県富津市新富20−1 新日本製鐵株 式会社 技術開発本部内 (56)参考文献 特開 平3−294714(JP,A) 特開 昭59−41408(JP,A)Continuing on the front page (72) Inventor Yuji Kitamura 46-59 Ohara Nakahara, Tobata-ku, Kitakyushu-shi, Fukuoka Nippon Steel Plant Design Co., Ltd. (72) Inventor Masahiko Hamada 5-3 Tokai-cho, Tokai City, Aichi Prefecture Nippon Steel Corporation (72) Inventor Yasuhiko Omatsu 20-1 Shintomi, Futtsu City, Chiba Prefecture Nippon Steel Corporation Technology Development Division (56) References JP-A-3-294714 (JP, A) JP-A Sho 59-41408 (JP, A)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 高炉から発生するガスを乾式集塵装置に
て除塵した後、タービンにてその発生ガスのエネルギー
を回収する高炉ガスエネルギー回収装置における乾式集
塵装置で捕集したダストの処理方法であって、前記乾式
集塵装置の下部ホッパーとタービン出側の清浄ガス管と
を気流輸送管で接続し、その途中に湿式のダスト分級機
を設置し、該湿式ダスト分級機にて乾ダストを気流より
分離すると共に、ダストの洗浄を行いスラリーとして系
外に排出することを特徴とする高炉乾式集塵装置のダス
ト処理方法。
1. A method for treating dust collected by a dry dust collecting apparatus in a blast furnace gas energy collecting apparatus for removing the gas generated from a blast furnace by a dry dust collecting apparatus and then recovering the energy of the generated gas by a turbine. The lower hopper of the dry dust collector and the clean gas pipe on the turbine exit side are connected by a pneumatic transport pipe, and a wet dust classifier is installed in the middle of the pipe, and the dry dust classifier is used for the dry dust classifier. A dust treatment method for a blast-furnace dry dust collector, wherein the dust is separated from an airflow, and the dust is washed and discharged as a slurry outside the system.
JP4137619A 1992-05-01 1992-05-01 Dust treatment method for blast furnace dry dust collector Expired - Lifetime JP2587750B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4137619A JP2587750B2 (en) 1992-05-01 1992-05-01 Dust treatment method for blast furnace dry dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4137619A JP2587750B2 (en) 1992-05-01 1992-05-01 Dust treatment method for blast furnace dry dust collector

Publications (2)

Publication Number Publication Date
JPH05311222A JPH05311222A (en) 1993-11-22
JP2587750B2 true JP2587750B2 (en) 1997-03-05

Family

ID=15202913

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4137619A Expired - Lifetime JP2587750B2 (en) 1992-05-01 1992-05-01 Dust treatment method for blast furnace dry dust collector

Country Status (1)

Country Link
JP (1) JP2587750B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101694268B1 (en) 2015-12-24 2017-01-09 주식회사 포스코 Dust collecting system

Also Published As

Publication number Publication date
JPH05311222A (en) 1993-11-22

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