JPS62227418A - Dust collecting method for molten iron pretreatment plant - Google Patents

Dust collecting method for molten iron pretreatment plant

Info

Publication number
JPS62227418A
JPS62227418A JP7218086A JP7218086A JPS62227418A JP S62227418 A JPS62227418 A JP S62227418A JP 7218086 A JP7218086 A JP 7218086A JP 7218086 A JP7218086 A JP 7218086A JP S62227418 A JPS62227418 A JP S62227418A
Authority
JP
Japan
Prior art keywords
dust
filter cloth
containing gas
hot metal
collected
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
JP7218086A
Other languages
Japanese (ja)
Inventor
Katsuhiro Ichiji
伊知地 勝弘
Hiromitsu Miki
三樹 博光
Koichiro Ito
伊藤 絋一郎
Tsunetaro Sugino
恒太郎 杉野
Masayuki Okamoto
正行 岡本
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 AIR FILTER KK
SHINWA TEC KK
Nippon Steel Corp
Original Assignee
NIPPON AIR FILTER KK
SHINWA TEC 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 NIPPON AIR FILTER KK, SHINWA TEC KK, Nippon Steel Corp filed Critical NIPPON AIR FILTER KK
Priority to JP7218086A priority Critical patent/JPS62227418A/en
Publication of JPS62227418A publication Critical patent/JPS62227418A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/02Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2273/00Operation of filters specially adapted for separating dispersed particles from gases or vapours
    • B01D2273/12Influencing the filter cake during filtration using filter aids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Filtering Of Dispersed Particles In Gases (AREA)
  • Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

Abstract

PURPOSE:To easily regenerate filter cloth collecting dust of dust-containing gas coming out of a molten iron pretreatment plant by adhering to the filter cloth a precoating agent to protect filter cloth from getting deliquenscence of collecting dust. CONSTITUTION:Dust-containing gas generated from a molten iron predetermined plant is guided into a guide duct 5. At that time, a precoating agent such as purple oxide or the like to protect filter cloths 3 of the primary dampers 6a-6d from getting deliquenscence of collecting dust is adhered beforehand to form a protecting layer. In guiding the precoating agent in, high-temperature clean air is guided out of a blower 14 through a guide duct 13 to form the precoating agent supplied from a storage tank 17 on the filter cloth 3. Therefore, provided dust containing calcium chloride is introduced in, sticky collected dust can be protected from adhering to the filter cloth, and heat of dust-containing gas is utilized effectively to prevent deliquenscence.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) この発明は、製鋼所等の溶銑予備処理設備から発生する
含塵ガスを濾布を用いたバグフィルタ等の集塵機で濾過
集塵処理する集塵方法に関する。
[Detailed Description of the Invention] [Objective of the Invention] (Industrial Application Field) This invention is a method for filtering dust-containing gas generated from hot metal pretreatment equipment at a steel mill, etc., using a dust collector such as a bag filter using a filter cloth. This invention relates to a dust collection method for dust collection processing.

(従来の技術) 一般に、製鋼技術の向上と高品質の鋼の生産を目的とし
て、高炉から受銑したトピードカーを溶銑予備処理設備
に移動し、そこで該トピードカーにランスを介して窒素
ガスと共に各種副原料(酸化カルシウム、塩化カルシウ
ム、フッ化カルシウム、並びに粉焼結鉱など)を吹込ん
で、溶銑の脱硅、脱燐、脱硫等の予備処理を行なう。こ
うした溶銑予備処理時に高温の多量の含塵ガスが発生す
るので、吸煙フードを介して集塵機に導入して集塵処理
し、作業環境の浄化を図る必要がある。
(Prior art) Generally, for the purpose of improving steelmaking technology and producing high-quality steel, a torpedo car that receives pig iron from a blast furnace is moved to a hot metal pretreatment facility, where it is passed through a lance to the torpedo car along with nitrogen gas and various Raw materials (calcium oxide, calcium chloride, calcium fluoride, powdered sintered ore, etc.) are injected to perform preliminary treatments such as desiliconization, dephosphorization, and desulfurization of hot metal. Since a large amount of high-temperature dust-containing gas is generated during such pretreatment of hot metal, it is necessary to introduce it into a dust collector through a smoke hood and collect the dust to purify the working environment.

(発明が解決しようとする間居点) しかしながら、上記溶銑予備処理設備から発生する含塵
ガス中には上述した各予備処理時に副原料の一部が飛散
混入する。特に脱燐行程において使用される副原料の塩
化カルシウムは非常に潮解性が大であり、その含塵ガス
中の塩化カルシウムの含有率が高かいと周囲の水分を吸
湿してベトベトとなる潮解現象が激しく発生する。この
為に濾布を用いたバグフィルタ等の集塵機では、バグの
濾布面や機内で潮解現象が発生し、該濾布がベトベトに
湿ってダストの固着堆積や目詰りが激しく・捕集ダスト
の払い落とし濾布再生の不能等を招き、また払い落とし
ダストの下部ホッパーからの排出や搬送等がスムーズに
できないことから、バグフィルタによる集塵が不可能で
あった。
(Issues to be Solved by the Invention) However, some of the auxiliary raw materials are scattered and mixed into the dust-containing gas generated from the hot metal pretreatment equipment during each of the above-mentioned pretreatments. In particular, calcium chloride, an auxiliary raw material used in the dephosphorization process, is extremely deliquescent, and if the content of calcium chloride in the dust-containing gas is high, it absorbs moisture from the surrounding area and becomes sticky. occurs violently. For this reason, in dust collectors such as bag filters that use filter cloth, a deliquescence phenomenon occurs on the filter cloth surface of the bag or inside the machine, and the filter cloth becomes sticky and sticky, resulting in severe accumulation of dust and clogging. It has been impossible to collect dust using a bag filter because it makes it impossible to regenerate the filter cloth, and it also makes it impossible to smoothly discharge and transport the dust from the lower hopper.

そこで、この発明は上記事情に鑑みなされ、濾布面での
潮解現象に起因する濾布の吸湿及び目詰等の不具合を防
止できて、捕集ダストの払い落とし濾布再生等が容易に
図れ、何ら支承なく溶銑予備処理設備からの含塵ガスの
バグフィルタによる濾過集塵が効率良く行ない得るよう
になる集塵方法を提供することを目的とする。
Therefore, the present invention was developed in view of the above circumstances, and can prevent problems such as moisture absorption and clogging of the filter cloth caused by deliquescence on the filter cloth surface, and can easily regenerate the filter cloth by brushing off the collected dust. It is an object of the present invention to provide a dust collection method that allows dust-containing gas from a hot metal pretreatment facility to be efficiently filtered and collected using a bag filter without any support.

〔発明の構成〕[Structure of the invention]

(問題を解決するための手段及び作用)この発明の集塵
方法は、上記目的を達成すべく、溶銑予備処理設備から
発生する含塵ガスを導入する際に、捕集ダスト中の塩化
カルシウムによる潮解現象から濾布を保護するための酸
化鉄粉等のプレコート剤を予め導入して濾布表面に付着
させて保護層を形成し、その後に上記溶銑予備処理設備
からの含塵ガスを導入して該濾布面上の保護層で濾過集
塵するようにしたものである。
(Means and effects for solving the problem) In order to achieve the above object, the dust collection method of the present invention uses calcium chloride in the collected dust when introducing dust-containing gas generated from hot metal pretreatment equipment. A pre-coat agent such as iron oxide powder to protect the filter cloth from deliquescence is introduced in advance and adhered to the surface of the filter cloth to form a protective layer, and then dust-containing gas from the hot metal pretreatment equipment is introduced. The protective layer on the surface of the filter cloth is used to collect dust by filtration.

(実施例) 以下この発明の一実施例を説明する。(Example) An embodiment of this invention will be described below.

まず説明の便宜上、第1図によりこの発明に使用したバ
グフィルタである集塵機の構成から先に説明すると、図
中1は吸込型集塵機の装置本体で、この内部は複数室に
区画され、その各区画室2a。
First, for convenience of explanation, the configuration of the dust collector, which is a bag filter used in this invention, will be explained with reference to FIG. Art room 2a.

2b、2c、2d内にそれぞれ円筒状をなすバグ3が多
数本ずつ垂下する状態に並設されている。
Inside 2b, 2c, and 2d, a large number of cylindrical bugs 3 are arranged in parallel in a hanging state.

また各区画室2a〜2dの下部にはそれぞれホッパー4
a、4b、4c、4dが設けられ、これら下部ホッパー
4a〜4dに溶銑予備処理設備(図示せず)から発生し
た高温の含塵ガスを捕集フード等を介して吸煙導通して
くる含塵ガス導入ダクト5が各々−次ダンパー5a、5
b、  6c、B’dを介して接続されている。一方上
記各区画室2a〜2dの上部には排気ダクト7が接続さ
れ、この排気ダクト7の端末側がサクションブロワ8に
接続されて屋外等に二次側りJランエアーを排気するよ
うになっている。また上部に逆洗式の捕集ダスト払い落
とし機構9が設けられ、これが上記両サイドの区画室2
a、2dにサーキュレーションダンパー10a、10d
を介して接続されていると共に、該払い落とし機構9の
逆洗用ダクト11が各々二次ダンパー12 a、  1
2 b、  12 c。
In addition, a hopper 4 is provided at the bottom of each compartment 2a to 2d.
a, 4b, 4c, and 4d are provided, and high-temperature dust-containing gas generated from hot metal pretreatment equipment (not shown) is sucked and conducted to these lower hoppers 4a to 4d via a collection hood, etc. The gas introduction ducts 5 each have a secondary damper 5a, 5
b, 6c, and B'd. On the other hand, an exhaust duct 7 is connected to the upper part of each compartment 2a to 2d, and the terminal side of the exhaust duct 7 is connected to a suction blower 8 to exhaust the secondary side J run air to the outdoors or the like. In addition, a backwashing type dust collecting mechanism 9 is provided at the top, and this is used to remove the collected dust from the compartments 2 on both sides.
Circulation dampers 10a and 10d on a and 2d
The backwashing duct 11 of the brushing-off mechanism 9 is connected to the secondary dampers 12a and 1, respectively.
2 b, 12 c.

12dを介して各区画室2a〜2dの上部に接続されて
いる。
It is connected to the upper part of each compartment 2a to 2d via 12d.

また、上記各区画室2a〜2dに接続して二次側高温ク
リーンエアーの導出ダクト13が設けられ、これにブロ
ワ14を介してプレコート剤の供給ダクト15が接続さ
れ、この供給ダクト15途中に粉体切出し装置16を介
して接続してプレコート剤の貯溜タンク17が設けられ
、且つその供給ダクト15が上記各下部ホッパー4a〜
4dに各々プレコートダンパー18a、18b、18c
Further, a secondary side high temperature clean air outlet duct 13 is connected to each of the compartments 2a to 2d, and a precoat agent supply duct 15 is connected to this via a blower 14. A precoat agent storage tank 17 is connected via the body cutting device 16, and its supply duct 15 is connected to each of the lower hoppers 4a to 4a.
4d respectively pre-coated dampers 18a, 18b, 18c
.

18dを介して接続されている。なお各下部ホッパー4
a〜4dは下端部に払い落としダストを機外に排出する
排出弁などを有している。
18d. In addition, each lower hopper 4
A to 4d have a discharge valve or the like at the lower end for discharging the dust to the outside of the machine.

而して、上述した構成のバグフィルタを用いて溶銑予備
処理設備から発生した含塵ガスの濾過集塵処理を行なう
方法を述べると、まずプレコート剤として酸化鉄粉を貯
溜タンク17内に投入して置く。この酸化鉄粉は同製鋼
所内で最も手軽に安定供給が図れるものとして、製鋼転
炉換気集塵や高炉鋳床集塵等により捕集して回収したも
のを使用する。
To describe a method for filtering and collecting dust-containing gas generated from hot metal pre-treatment equipment using the bag filter having the above-mentioned configuration, first, iron oxide powder is introduced into the storage tank 17 as a pre-coating agent. Leave it there. This iron oxide powder is the easiest and most stable supply within the steelworks, and is collected and recovered through steelmaking converter ventilation dust collection, blast furnace cast bed dust collection, etc.

そして本集塵設備の立上り運転時、まず導入ダクト5の
各−次ダンパー6a〜6dを開き、二次ダンパー12a
〜12dを閉じ、サーキュレーションダンパー10a、
10dを閉じ、プレコートダンパー18a〜18dを開
く。その状態でサクションブロワ8を稼働してこの吸引
により導入ダクト5の末端フード側(図示せず)から外
気を導入する。これと平行してブロワ14を稼働して、
機内の二次クリーン側のエアーを導出ダクト13から導
出して供給ダクト15に送り、その途中で粉体切出し装
置16により上記貯溜タンク17内のプレコート剤であ
る酸化鉄粉を混合する。ように送り出して、該酸化鉄粉
をエアー搬送により各下部ホッパー4a〜4dに導入す
る。こうして各下部ホッパ−4a〜4d内に導入したプ
レコート剤を上記導入ダクト5からの外気と共に混合搬
送して各区画室2a〜2d内の各バグ3の濾布面に保護
層を形成する。
When starting up the dust collection equipment, first open each secondary damper 6a to 6d of the introduction duct 5, and then open the secondary damper 12a.
~12d is closed, the circulation damper 10a,
10d and open the precoat dampers 18a to 18d. In this state, the suction blower 8 is operated to introduce outside air from the end hood side (not shown) of the introduction duct 5 by this suction. In parallel with this, the blower 14 is operated,
Air from the secondary clean side of the machine is led out from the outlet duct 13 and sent to the supply duct 15, and on the way there, the powder cutting device 16 mixes iron oxide powder, which is a pre-coating agent, in the storage tank 17. The iron oxide powder is introduced into each of the lower hoppers 4a to 4d by air conveyance. The precoat agent thus introduced into each of the lower hoppers 4a to 4d is mixed and conveyed with the outside air from the introduction duct 5 to form a protective layer on the filter cloth surface of each bag 3 in each of the compartments 2a to 2d.

こうして各バグ3の濾布面に充分に保護層を形成した時
点で溶銑予備処理設備からの高温の含塵ガスの吸煙集塵
態勢に入る。つまり上記各プレコートダンパー13a〜
18dを閉じると共に粉体切出し装置16及びブロワ1
4を停止する。また−次ダンバー6a〜6dを開き、二
次ダンパー12a〜12d及びサーキュレーションダン
パー10a、10dを閉じる。この状態でサクションブ
ロワ8の吸煙作用により溶銑予備処理設備から発生した
高温含塵ガスを導入ダクト5から各下部ホッパー4a〜
4dを介して各区画室2a〜2dに吸引導入する。これ
にて塩化カルシウム含を含塵ガスは各バグ3の濾布面に
生成した保護層表面で濾過捕集される。その濾過集塵に
より清浄化した空気は二次側クリ−エアーとして上部か
ら排気ダクト7を介してサクションブロア8に吸引導出
して屋外等に排出する。
In this way, when a protective layer is sufficiently formed on the filter cloth surface of each bag 3, the system enters the state of sucking and collecting the high temperature dust-containing gas from the hot metal pretreatment equipment. In other words, each pre-coat damper 13a~
18d is closed and the powder cutting device 16 and blower 1 are closed.
Stop 4. Further, the secondary dampers 6a to 6d are opened, and the secondary dampers 12a to 12d and the circulation dampers 10a and 10d are closed. In this state, high-temperature dust-containing gas generated from the hot metal pretreatment equipment is introduced from the duct 5 to each lower hopper 4a through the suction blower 8.
4d into each of the compartments 2a to 2d. In this way, the dust-containing gas containing calcium chloride is filtered and collected on the surface of the protective layer formed on the filter cloth surface of each bag 3. The air purified by the filtration and dust collection is suctioned from the upper part through the exhaust duct 7 to the suction blower 8 and discharged outdoors as secondary clean air.

また上述した集塵運転中にタイマーやバグ3の圧損抵抗
検知器等からの信号でダスト払い落とし時期が来たこと
が知らされると、逆洗式の捕集ダスト払い落とし機構9
により各区画室2a〜2dを一区画毎に順々に逆洗モー
ドに切替えてバグ3の捕集ダストの逆洗払い落としを行
う。
Furthermore, when it is notified that the dust dust removal time has come by a signal from the timer or the pressure loss resistance detector of the bug 3 during the above-mentioned dust collection operation, the backwash type collecting dust removal mechanism 9
Thus, each of the compartments 2a to 2d is sequentially switched to the backwash mode one by one, and the dust collected from the bugs 3 is backwashed off.

その方法は、例えば第1の区画室2aから逆洗払い落と
しを行なう場合、それ以外の各区画室2b〜2dは上記
同様に集塵運転を続けたままにして置き、第2図に示す
如く該第1の区画室の一次ダンパー6aを閉じると共に
、サーキュレーションダンパー10dを開き、二次ダン
パー12aを間歇的に複数回開くことで、該区画室2a
内の各バグ3の収縮・膨張を繰返して、その捕集ダスト
を払い落とす。この逆洗のエアー源としてサーキュレー
ションダンパー10dから逆洗用ダクト11に取出した
機内二次側の高温クリーンエアーを使う。この逆洗エア
ーにより該バグ3の濾布に捕集されているダストを保護
層と共に払い落として、下部ホッパー4aから機外に排
出する。
For example, when backwashing is performed from the first compartment 2a, the other compartments 2b to 2d are left in the same dust collection operation as described above, and the dust collection operation is continued as shown in FIG. By closing the primary damper 6a of the first compartment, opening the circulation damper 10d, and intermittently opening the secondary damper 12a multiple times, the compartment 2a is closed.
The collected dust is brushed off by repeatedly contracting and expanding each bag 3 inside. As the air source for this backwashing, high-temperature clean air from the secondary side of the machine taken out from the circulation damper 10d to the backwashing duct 11 is used. This backwashing air blows off the dust collected on the filter cloth of the bag 3 together with the protective layer, and discharges it out of the machine from the lower hopper 4a.

こうして捕集ダストの払い落としによりバグ3の再生を
終了した第1の区画室2aは、再度含塵ガスを導入して
濾過集塵を行なう。この時の方法は上記逆洗終了後に二
次ダンパー12aと共にサーキュレーションダンパー1
0dを閉じ、プレコートダンパー18aを開き、その状
態でブロワ14を稼働させて、機内の二次側高温クリー
ンエアーを導出ダクト13に取出して供給ダクト15に
送り、その途中で貯溜タンク17から切出し装置16に
よりプレコート剤である酸化鉄粉を供給して該区画室2
aの下部ホッパー4a内にエアー搬送し、これと同時に
一次ダンパー6aを開いて導入ダクト5から高温含塵ガ
スを同下部ホッパー4a内に吸引導入して、その高温含
塵ガスと酸化゛鉄粉を混入した二次側クリーンエアーと
をラップした状態で約1〜2分間該区画室2a内に供給
し、これにて塩化カルシウム濃度が5%以下になるよう
に酸化鉄と混合した状態で各バグ3の濾布面に保護層を
作る。こうした後に切出し装置16並びにブロワ14を
停止し、且つプレコートダンパー18aを閉じて、高温
含塵ガスを連続的に吸引導入して濾過集塵を再開する。
In this way, the first compartment 2a, in which the bug 3 has been regenerated by blowing off the collected dust, introduces the dust-containing gas again to perform filtration and dust collection. The method at this time is to use the circulation damper 1 together with the secondary damper 12a after the above-mentioned backwashing is completed.
0d is closed, the pre-coat damper 18a is opened, and in this state, the blower 14 is operated to take out the high temperature clean air on the secondary side inside the machine to the outlet duct 13 and send it to the supply duct 15. 16 supplies iron oxide powder, which is a pre-coating agent, to the compartment 2.
At the same time, the primary damper 6a is opened to suck and introduce the high-temperature dust-containing gas into the lower hopper 4a from the introduction duct 5, and the high-temperature dust-containing gas and iron oxide powder are conveyed into the lower hopper 4a. is supplied into the compartment 2a for about 1 to 2 minutes in a wrapped state with secondary clean air mixed with iron oxide. Create a protective layer on the filter cloth surface of Bug 3. After this, the cutting device 16 and the blower 14 are stopped, the precoat damper 18a is closed, and the high-temperature dust-containing gas is continuously sucked and introduced to resume filtration and dust collection.

以下同様にして次々と順番に第2、第3、第4の区画室
2b〜2dの逆洗濾布再生及び保護層生成並びに含塵ガ
ス濾過集塵再開を繰返して行く。
Thereafter, backwash filter cloth regeneration and protective layer generation in the second, third, and fourth compartments 2b to 2d, and dust-containing gas filtration and dust collection restart are repeated in the same manner one after another.

なお、上記保護層生成を、プレコート剤を混入したクリ
ーンエアーと共に含塵ガスをラップして導入する混合希
釈方法で行なったが、−次ダンパーを閉じたまま含塵ガ
スを導入せずに、上記プレコート剤を混入したクリーン
エアーのみの導入により行なうようにしても可である。
The above protective layer was formed by a mixed dilution method in which the dust-containing gas was wrapped and introduced together with clean air mixed with a pre-coat agent, but the above-mentioned method was performed without introducing the dust-containing gas with the damper closed. It is also possible to carry out the process by introducing only clean air mixed with a pre-coating agent.

ところで、上記溶銑予備処理設備から発生してくる含塵
ガスは、前述した如く該溶銑予備処理の脱燐行程におい
て副原料の潮解性大なる塩化カルシウムが含まれて来る
。この塩化カルシウムを含んだダストは時間の経過と共
に潮解現象が発生する。即ち回りの水分を吸湿して重量
が増加してベトベトな状態となる。特に該塩化カルシウ
ムの含有率が高い程潮解現象が激しく、また温度もかな
り影響して高温から常温に下がって来る程生じ易い。し
かるに上記溶銑予備設備から発生した含塵ガス中の塩化
カルシウムの含有率は通常含塵量2g/N77Z3中に
10〜30%程度とかなり多い。
Incidentally, the dust-containing gas generated from the hot metal pretreatment equipment contains highly deliquescent calcium chloride, which is an auxiliary raw material, in the dephosphorization process of the hot metal pretreatment, as described above. This dust containing calcium chloride deliquesces over time. That is, it absorbs moisture from its surroundings, increasing its weight and becoming sticky. In particular, the higher the content of calcium chloride, the more severe the deliquescence phenomenon is, and the temperature also has a considerable effect on the deliquescence, which is more likely to occur as the temperature drops from high temperature to room temperature. However, the content of calcium chloride in the dust-containing gas generated from the hot metal preliminary equipment is usually quite high, about 10 to 30% per dust content of 2 g/N77Z3.

この時のガス発生温度は数百度で非常に高く直ぐに潮解
現象を引き起こすことは無いが、しかし集塵機本体1内
に来ると130℃から常温の範囲にあり、また−回の発
塵ガスの処理時間は約20〜80分で、しかもこの処理
が生産計画によって連続的の場合もあれば、ある時間待
ってから行なわれる場合もあり、更には集塵機の定期点
検等時には長時間の休転もある。従って上述した保護層
を生成せずにバグ3に濾過集塵すると、捕集ダストが潮
解現象を起こして該バグ3の濾布にベトベトに付着して
、濾布の目詰りが激しく、且つその捕集ダストの払い落
としが困難で濾布再生ができなくなるばかりか、捕集ダ
ストの機外への排出も困難で、バグフィルタによる集塵
処理は不可能である。
The gas generation temperature at this time is several hundred degrees, which is very high and does not immediately cause deliquescence, but when it comes to the dust collector body 1, it ranges from 130 degrees Celsius to room temperature, and the processing time of the dust gas is - This process takes approximately 20 to 80 minutes, and depending on the production plan, this process may be continuous, or may be performed after a certain period of time, and may also be stopped for a long time during periodic inspections of the dust collector. Therefore, if the dust is filtered and collected in the bag 3 without forming the above-mentioned protective layer, the collected dust will cause a deliquescent phenomenon and stick to the filter cloth of the bag 3, resulting in severe clogging of the filter cloth and Not only is it difficult to shake off the collected dust, making it impossible to regenerate the filter cloth, but it is also difficult to discharge the collected dust outside the machine, making it impossible to collect dust using a bag filter.

そこで、上述した如く常に含塵ガスの導入前にバグ3の
濾布面に酸化鉄粉による保護層を形成して、その後から
含塵ガスを導入して濾過集塵することで、その捕集ダス
ト中の塩化カルシウムの潮解により発生した水分を保護
層の酸化鉄粉が吸収し、直接濾布に触れないようにでき
る。これで捕集ダストのベトベトした状態での濾布への
付着を防止できて、該濾布の目詰りを軽減し得ると共に
、逆洗エアーの導入による捕集ダストの払い落としが容
易にできて、濾布再生を可能となせる。更には払い落と
したダストの下部ホッパーからの機外への排出・搬送も
スムーズに出来るようになる。
Therefore, as mentioned above, a protective layer of iron oxide powder is always formed on the filter cloth surface of the bag 3 before introducing the dust-containing gas, and then the dust-containing gas is introduced and filtered and collected. The iron oxide powder in the protective layer absorbs moisture generated by the deliquescence of calcium chloride in the dust, preventing it from coming into direct contact with the filter cloth. This prevents the collected dust from sticking to the filter cloth in a sticky state, reduces clogging of the filter cloth, and allows the collected dust to be easily blown off by introducing backwash air. , filter cloth can be regenerated. Furthermore, the dust that has been brushed off can be smoothly discharged and transported from the lower hopper to the outside of the machine.

また、上記潮解現象は温度低下によっても起り易いので
、機内を極力保温することが潮解防止を図るのにを効と
なる。しかるに上述した方法では高温で導入される含塵
ガスの熱を前動に利用して機内の保温が図れて更に潮解
防止に効果がある。
Furthermore, since the above-mentioned deliquescence phenomenon is likely to occur due to a drop in temperature, keeping the inside of the machine as warm as possible is effective in preventing deliquescence. However, in the method described above, the heat of the dust-containing gas introduced at high temperature is used for the forward motion to keep the inside of the machine warm, which is also effective in preventing deliquescence.

つまり、プレコート剤の導入に際し、外気を用いずに、
機内の二次側高温クリーンエアーを導出ダクト13を介
してブロワ14により導出し、この高温クリーンエアー
に貯溜タンク17から供給した潮解防止剤を乗せて再度
機内に送って各バグ3の濾布面に保護層を生成させるこ
とから、外部冷気が機内に入らず、各バグ並びに機内の
保温が図れる。また逆洗エアーによる捕集ダストの払い
落とし時にも、払い落とし機構9に機内の二次測高l:
iAクリーンエアーを導出して、これを逆洗エアーとし
て挿入するので、バグ並びに機内を冷却することなく保
温状態のままダスト払い落としができて潮解防止に役立
つようになる。
In other words, when introducing the precoat agent, without using outside air,
The secondary side high temperature clean air inside the machine is led out by the blower 14 through the outlet duct 13, and the high temperature clean air is loaded with the deliquescent inhibitor supplied from the storage tank 17 and sent back into the machine, and then the filter cloth surface of each bag 3 is delivered. By forming a protective layer on the air, cold air from the outside does not enter the cabin, keeping each bug and the inside of the cabin warm. Also, when the collected dust is brushed off by backwashing air, the dust removal mechanism 9 is used to measure the secondary height inside the machine.
Since iA clean air is extracted and inserted as backwash air, dust can be removed without cooling the bugs or the inside of the machine while keeping it warm, which helps prevent deliquescence.

次に、第3図乃至第4図によりこの発明の他の実施例を
説明する。ここでは上記実施例の吸込型集塵機と異なり
押込型集塵機を用いている。なお上記実施例のものと同
一構成をなすものには同一符号を付して説明の簡略化を
図る。しかしてこの実施例の場合、溶銑予備処理設備か
らの含塵ガスはサクションブロワ8により導入ダクト5
を介して各下部ホッパー4a〜4dに送り込み、そこか
・ら各区画室2a〜2d内のバグ3に入れて、そのバグ
3の濾布面の保護層に濾過集塵させる。その各バグ3の
濾布に捕集されたダストは各区画室2a〜2d毎に順に
逆洗により下部ホッパー4a〜4dに払い落とされて排
出する。その逆洗払い落としは、各下部ホッパー4a〜
4dに二次ダンパー12a〜12dを介して接続した吸
引ダクト20を設け、この吸引ダクトの端部を上記含塵
ガス導入ダクト5のサクションブロワ8より上流側に接
続しておき、そして例えば第1の区画室2aの捕集ダス
ト払い落とし時期が来たら、二次ダンパー12aと一次
ダンパー6aとを第4図に示す如く交互に複数回開閉す
ることで、該区画室2a内の各バグ3を収縮・膨張を繰
返して、その捕集ダストを払い落とす。
Next, another embodiment of the present invention will be described with reference to FIGS. 3 and 4. Here, unlike the suction type dust collector of the above embodiment, a push type dust collector is used. Components having the same configuration as those in the above embodiment are given the same reference numerals to simplify the explanation. However, in the case of this embodiment, the dust-containing gas from the hot metal pretreatment equipment is transferred to the inlet duct 5 by the suction blower 8.
It is fed into each of the lower hoppers 4a to 4d through the hoppers 4a to 4d, and from there, it is introduced into the bag 3 in each of the compartments 2a to 2d, where it is filtered and collected on the protective layer of the filter cloth surface of the bag 3. The dust collected on the filter cloth of each bag 3 is sequentially backwashed into the lower hoppers 4a to 4d and discharged from each compartment 2a to 2d. The backwashing is done in each lower hopper 4a~
4d is provided with a suction duct 20 connected via secondary dampers 12a to 12d, and the end of this suction duct is connected to the upstream side of the suction blower 8 of the dust-containing gas introduction duct 5, and for example, the first When it is time to dust off the collected dust in the compartment 2a, the secondary damper 12a and the primary damper 6a are alternately opened and closed multiple times as shown in FIG. 4 to remove each bug 3 in the compartment 2a. By repeatedly contracting and expanding, the collected dust is brushed off.

こうして捕集ダストの払い落とし終了後は、二次ダンパ
ー12aを閉じ、−次ダンパー6aと共にプレコートダ
ンパー18aを開いて、ブロワ14により機内の二次側
高温クリーンエアーを導出ダクト13を介して導出し、
それに貯溜タンク17から切出し装置16によりプレコ
ート剤である酸化鉄粉を供給して供給ダクト15から下
部ホッパー4a内にエアー搬送し、これと同時に導入ダ
クト5から圧送されて来る高温の含塵ガスとラップして
区画室2a内の各バグ3の濾布面に捕集させ、これにて
該バグ3の濾布面に保護層を形成する。その後切出し装
置16及びブロワ14を止め、プレコートダンパー18
aを閉じ、そのまま高温含塵ガスの導入を続けて濾過集
塵を再開する。
After the collected dust is brushed off, the secondary damper 12a is closed, the pre-coat damper 18a is opened together with the secondary damper 6a, and the secondary high-temperature clean air inside the machine is drawn out via the duct 13 by the blower 14. ,
Iron oxide powder, which is a pre-coating agent, is supplied from the storage tank 17 by the cut-out device 16 and conveyed by air from the supply duct 15 into the lower hopper 4a. It is wrapped and collected on the filter cloth surface of each bag 3 in the compartment 2a, thereby forming a protective layer on the filter cloth surface of the bag 3. After that, the cutting device 16 and blower 14 are stopped, and the precoat damper 18
Close a, continue to introduce high-temperature dust-containing gas, and restart filtration and dust collection.

これにて上記実施例同様の効果が得られてバグフィルタ
による効率の良い集塵が可能となる。
As a result, the same effects as in the above embodiment can be obtained, and efficient dust collection by the bag filter can be achieved.

なお、この押込型集塵機の場合でも上記実施例同様に各
バグ3の濾布面への保護層生成を、含塵ガスをラップせ
ずに、プレコート剤を混入したクリーンエアーのみの導
入により行なうようにしても可である。
In addition, in the case of this push-in type dust collector, as in the above embodiment, the protective layer is formed on the filter cloth surface of each bag 3 by introducing only clean air mixed with a pre-coating agent, without wrapping the dust-containing gas. It is possible to do so.

また、上述した以外に、各バグ3は捕集ダストの払い落
とし効果の良い長繊維の濾布を使用し、更に払い落とし
たダストの機外に排出する下部ホッパー4a〜4d及び
それを目的の箇所に搬送するコンベア(図示せず)を蒸
気やその他の手段で強制保温することも、ダストの排出
・搬送をスムーズにするのに有効である。
In addition to the above, each bag 3 uses a long-fiber filter cloth that has a good effect of removing collected dust, and further includes lower hoppers 4a to 4d for discharging the removed dust to the outside of the machine, and a It is also effective to forcibly insulate the conveyor (not shown) that transports the dust to the location using steam or other means to smoothly discharge and transport the dust.

更には、集塵機の休転時に機内温度の低下を防ぐべく、
機内からの二次側やバグの出口に外部冷気の侵入を遮断
するダンパーやシャッターを取付けたり、集塵機の装置
本体1や周辺機器(各種ダクト等)を断熱材で覆って保
温することもを効である。
Furthermore, in order to prevent the temperature inside the machine from dropping when the dust collector is stopped,
It is also effective to install a damper or shutter to block the intrusion of external cold air to the secondary side from the machine or the exit of the bug, or to cover the dust collector unit 1 and peripheral equipment (various ducts, etc.) with heat insulating material to keep them warm. It is.

〔発明の効果〕〔Effect of the invention〕

この発明は上述した如く、溶銑予備処理設備から発生す
る含塵ガスを導入の際に、該含塵ガスによる潮解現象か
ら濾布を保護するための酸化鉄粉等のプレコート剤を予
め導入して濾布面に付着させて保護層を形成し、その後
に上記溶銑予備処理設備からの含塵ガスを導入して該濾
布面上の保護層で濾過集塵するようにしたから、濾布面
での潮解現象に起因する濾布の吸湿及び目詰り等の不具
合を確実に防止できて、捕集ダストの払い落とし濾布再
生等が容易に図れ、何ら支承なく溶銑予備処理設備から
の含塵ガスのバグフィルタによる濾過集塵が効率良く行
ない得るようになる。
As described above, when introducing dust-containing gas generated from hot metal pretreatment equipment, a pre-coating agent such as iron oxide powder is introduced in advance to protect the filter cloth from deliquescence caused by the dust-containing gas. A protective layer was formed by adhering it to the filter cloth surface, and then the dust-containing gas from the hot metal pretreatment equipment was introduced and filtered and collected by the protective layer on the filter cloth surface. It is possible to reliably prevent malfunctions such as moisture absorption and clogging of the filter cloth caused by deliquescence phenomenon, and it is possible to easily wipe off the collected dust and regenerate the filter cloth. Gas filtering and dust collection using a bag filter can be performed efficiently.

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

第1図はこの発明の集塵方法に用いた集塵機の一実施例
を示す概略構成図、第2図は同集塵機の、作動を示すタ
イムチャート図、第3図は集塵機の他の実施例を示す概
略構成図、第4図は同集塵機の作動を示すタイムチャー
ト図である。 1・・・集塵機の本体、2a〜2d・・・区画室、3・
・・バグ(a布)、4a〜4d・・・下部ホッパー、5
・・・含塵ガス導入ダクト、6a〜6d・・・−次ダン
バー、7・・・排気ダクト、8・・・サクションブロワ
、9・・・逆洗式の捕集ダスト払い落とし機構、10a
。 10d・・・サーキュレーションダンパー、11・・・
逆洗用ダクト、12a〜12d・・・二次ダンパー、1
3・・・導出ダクト、14・・・ブロワ、15・・・供
給ダクト、16粉体切出し装置、17・・・プレコート
剤貯溜タンク、18a〜18d・・・プレコートダンパ
ー、20・・・1及引ダクト。
Fig. 1 is a schematic configuration diagram showing one embodiment of a dust collector used in the dust collection method of the present invention, Fig. 2 is a time chart showing the operation of the same dust collector, and Fig. 3 is a diagram showing another embodiment of the dust collector. FIG. 4 is a time chart showing the operation of the dust collector. 1... Main body of the dust collector, 2a to 2d... Compartment chamber, 3.
...Bug (a cloth), 4a-4d...lower hopper, 5
...Dust-containing gas introduction duct, 6a to 6d... - next damper, 7... Exhaust duct, 8... Suction blower, 9... Backwash type collection dust removal mechanism, 10a
. 10d... Circulation damper, 11...
Backwash duct, 12a to 12d...Secondary damper, 1
3... Derivation duct, 14... Blower, 15... Supply duct, 16 Powder cutting device, 17... Precoat agent storage tank, 18a to 18d... Precoat damper, 20... 1 and Pull duct.

Claims (4)

【特許請求の範囲】[Claims] (1)溶銑予備処理設備から発生する含塵ガスを濾布を
用いて濾過集塵する方法において、捕集ダストの潮解現
象から濾布を保護するプレコート剤を予め導入して濾布
面に付着させ、この後に溶銑予備処理設備からの含塵ガ
スを導入して濾過集塵することを特徴とする溶銑予備処
理設備における集塵方法。
(1) In a method of filtering and collecting dust-containing gas generated from hot metal pretreatment equipment using a filter cloth, a pre-coat agent is introduced in advance to protect the filter cloth from the deliquescence phenomenon of the collected dust and adheres to the surface of the filter cloth. A method for collecting dust in a hot metal pretreatment facility, characterized in that the dust-containing gas from the hot metal pretreatment facility is introduced and filtered to collect the dust.
(2)プレコート剤として酸化鉄粉を用いたことを特徴
とする特許請求の範囲第1項記載の溶銑予備処理設備に
おける集塵方法。
(2) A dust collection method in a hot metal pretreatment facility according to claim 1, characterized in that iron oxide powder is used as a precoat agent.
(3)酸化鉄粉は製鋼転炉換気集塵又は高炉鋳床集塵に
より回収したものであることを特徴とする特許請求の範
囲第2項記載の溶銑予備処理設備における集塵方法。
(3) The dust collection method in a hot metal pretreatment facility according to claim 2, wherein the iron oxide powder is collected by ventilation dust collection in a steelmaking converter or blast furnace cast bed dust collection.
(4)プレコート剤は、濾布面を冷却しないように集塵
機内二次側の高温のクリーンエアーを導出し、これに該
プレコート剤を乗せて導入して濾布面に供給することを
特徴とする特許請求の範囲第1項又は第2項記載の溶銑
予備処理設備における集塵方法。
(4) The pre-coat agent is characterized in that high-temperature clean air from the secondary side of the dust collector is led out so as not to cool the filter cloth surface, and the pre-coat agent is introduced into the air to be supplied to the filter cloth surface. A method for collecting dust in hot metal pretreatment equipment according to claim 1 or 2.
JP7218086A 1986-03-29 1986-03-29 Dust collecting method for molten iron pretreatment plant Pending JPS62227418A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7218086A JPS62227418A (en) 1986-03-29 1986-03-29 Dust collecting method for molten iron pretreatment plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7218086A JPS62227418A (en) 1986-03-29 1986-03-29 Dust collecting method for molten iron pretreatment plant

Publications (1)

Publication Number Publication Date
JPS62227418A true JPS62227418A (en) 1987-10-06

Family

ID=13481767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7218086A Pending JPS62227418A (en) 1986-03-29 1986-03-29 Dust collecting method for molten iron pretreatment plant

Country Status (1)

Country Link
JP (1) JPS62227418A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01262915A (en) * 1988-04-11 1989-10-19 Nippon Spindle Mfg Co Ltd Method for precoating filter cloth and dust collecting apparatus
JPH0556211U (en) * 1991-12-26 1993-07-27 株式会社プランテック Pre-coated bag filter device
US8584616B2 (en) 2007-08-24 2013-11-19 Durr Systems Gmbh Method for supplying a coating system with a particulate auxiliary material

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52131271A (en) * 1976-04-27 1977-11-04 Shinwa Boeki Kk Dust collector for coke furnaces
JPS5626456A (en) * 1979-08-09 1981-03-14 Mitsubishi Electric Corp Thick film intergrated circuit device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52131271A (en) * 1976-04-27 1977-11-04 Shinwa Boeki Kk Dust collector for coke furnaces
JPS5626456A (en) * 1979-08-09 1981-03-14 Mitsubishi Electric Corp Thick film intergrated circuit device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01262915A (en) * 1988-04-11 1989-10-19 Nippon Spindle Mfg Co Ltd Method for precoating filter cloth and dust collecting apparatus
JPH0556211U (en) * 1991-12-26 1993-07-27 株式会社プランテック Pre-coated bag filter device
US8584616B2 (en) 2007-08-24 2013-11-19 Durr Systems Gmbh Method for supplying a coating system with a particulate auxiliary material

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