JPS586389A - Method of operating dust collector - Google Patents

Method of operating dust collector

Info

Publication number
JPS586389A
JPS586389A JP56101286A JP10128681A JPS586389A JP S586389 A JPS586389 A JP S586389A JP 56101286 A JP56101286 A JP 56101286A JP 10128681 A JP10128681 A JP 10128681A JP S586389 A JPS586389 A JP S586389A
Authority
JP
Japan
Prior art keywords
dust
venturi scrubber
dust collector
multiplier
dust collection
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
JP56101286A
Other languages
Japanese (ja)
Inventor
岸田 正坦
阿部 英彦
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 JP56101286A priority Critical patent/JPS586389A/en
Publication of JPS586389A publication Critical patent/JPS586389A/en
Pending legal-status Critical Current

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  • Separation Of Particles Using Liquids (AREA)
  • Electrostatic Separation (AREA)
  • Blast Furnaces (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 ん器とを直列に配置してなる集じんシステムの効率的な
操業方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an efficient method of operating a dust collection system in which a dust collection device and a dust collection device are arranged in series.

一般に転炉′発生ガス、高炉発生ガス等可燃性ガスの乗
じんは、二段ベンチュリ−スクラバ一方式で行われてい
ることが多い。そして高集じん性能を達成するためには
多大な圧力如損失が必要であり、省エネ上好ましくない
。しかし反面高温ガスに対しての大容量冷却器としての
機能を有している。
Generally, combustible gases such as converter gas and blast furnace gas are often mixed using a two-stage venturi scrubber system. In order to achieve high dust collection performance, a large amount of pressure loss is required, which is not preferable in terms of energy saving. However, on the other hand, it functions as a large-capacity cooler for high-temperature gas.

一方電気乗じん器は、必要圧力損失がペンチューリース
クラバーに比し非常に少なく、かつ高乗じん性能が達成
できるため省エネ機種としてのメリノトが太きい。しか
し高温ガス集じんの場合、放電電流が多大となり省エネ
」ニテメリノトとなるため入口ガス温度をある程度捷で
冷却する冷却器を前置する必要がある。
On the other hand, electric dust multipliers require much less pressure loss than Pentury scrubbers, and can achieve high dust multiplier performance, making them highly effective as energy-saving models. However, in the case of high-temperature gas dust collection, the discharge current is large, resulting in energy savings, so it is necessary to install a cooler to cool down the inlet gas temperature to some extent.

しかして画集じん器の長所を組合わせたベンチュリース
クラバ−」一電気集じん器は高温ガスに対する冷却性能
と粗集しん性能を主としてペンチ−リースクラバーに、
最終乗じん性能を電気集じん器に分担させることにより
低圧損型で、かつ高温ガスに適した省エネ型染じんンス
テムが構成でき、今後の集じんンステムとして有望であ
る。
Therefore, the electrostatic precipitator is a venturi scrubber that combines the advantages of an art dust collector.The electrostatic precipitator is a venturi scrubber that combines the advantages of an art dust collector.
By assigning the final dust multiplication performance to the electrostatic precipitator, an energy-saving dust collection system with low pressure loss and suitable for high-temperature gases can be constructed, which is promising as a future dust collection system.

ところで、電気集じん器は、集じん極と放電極の間に電
圧を印加し電気力(主としてクーロン力)により通過ガ
ス中のダスト、ミストを集じん極に捕集し、捕集したダ
ストヲ間欠的に除去するととにより長期的に安定した集
じん性能が発揮できるものである。しかし捕集したダス
トを除去する場合、乾式、湿式いづれも果じん性能が悪
く々る欠点を有している。即ち 乾式電気束じん器の場合は、ダスト除去として一般的に
槌打方式が使われている。槌打時は集じん極に捕集され
たダストが極から剥離し重力により落下するが、このう
ち微小ダストはガス流中に再飛散し、後流側に出ていく
ため乗じん性能が悪化する。
By the way, in an electrostatic precipitator, a voltage is applied between a dust collecting electrode and a discharge electrode, and dust and mist in passing gas are collected on the dust collecting electrode using electric force (mainly Coulomb force), and the collected dust is released intermittently. By removing the dust periodically, stable dust collection performance can be achieved over a long period of time. However, when removing the collected dust, both dry and wet methods have the disadvantage of poor dust removal performance. That is, in the case of a dry electric dust duster, a hammering method is generally used to remove dust. During hammering, the dust collected on the dust collection pole separates from the pole and falls due to gravity, but the minute dust is re-dispersed into the gas flow and exits to the downstream side, which deteriorates the dust collection performance. do.

湿式電気乗じん器の場合は、ダスト除去として一般的に
洗浄方式が使われている。洗浄時は乗じん極に捕集され
たダストが水で洗浄されスラリー流として極表面を流下
し下部に排出する。しかし洗浄時は荷電電圧が不安定と
なるため一般的に荷電室圧を低下又は遮断するため集じ
ん性能が悪化する。
In the case of wet type electric dust multipliers, a cleaning method is generally used to remove dust. During cleaning, the dust collected on the dust electrode is washed with water, flows down the electrode surface as a slurry stream, and is discharged to the bottom. However, during cleaning, since the charging voltage becomes unstable, the charging chamber pressure is generally lowered or cut off, which deteriorates the dust collection performance.

以上の如く、電気乗じん器はダストを除去する期間集じ
ん性能が悪くなるため、ベンチュリースクラバーと電気
乗じん器で構成される乗じんシステム全体としての東じ
ん性能も悪くなる。
As described above, since the dust collection performance of the electric dust multiplier deteriorates during the period of dust removal, the dust collection performance of the dust multiplier system as a whole consisting of the venturi scrubber and the electric dust multiplier also deteriorates.

本発明はこれらの問題点を解消し極めて効果的な集じん
装置の操業方法を提供せんとするものである。
The present invention aims to solve these problems and provide an extremely effective method of operating a dust collector.

以下本発明を説明する。The present invention will be explained below.

ベンチュリースクラバーの乗じん性能は第1図に示す如
く圧力損失を大きくするほど良くなるが反面運転費は高
くなる。一方布気集じん器の集じん性能は第2図に示す
如く同一極間の場合荷電電圧を高くするほど良く々る。
As shown in Figure 1, the dust multiplication performance of the Venturi scrubber improves as the pressure loss increases, but on the other hand, the operating cost increases. On the other hand, as shown in FIG. 2, the dust collection performance of the cloth air dust collector improves as the charging voltage is increased when the electrodes are of the same type.

従って、ペンチ−リースクラバーと電気乗じん器を直列
に配置した集じんシステムにおいては、運転費を少なく
するため通常ベンチュリースクラバーの圧力損失を少な
くシ、電気乗じん器の荷電室圧を高くして操業する方法
が好ましい。
Therefore, in a dust collection system in which a venturi scrubber and an electric dust multiplier are arranged in series, in order to reduce operating costs, the pressure loss of the venturi scrubber is usually reduced, and the charging chamber pressure of the electric dust multiplier is increased. A method of operating is preferred.

しかるに電気乗じん器で捕集したダストを集じん極、放
電極から除去する期間は電気乗じん器の集じん性能が低
下するだめ、システム出口ダストの濃度が増える。
However, during the period when the dust collected by the electrostatic precipitator is removed from the dust collecting electrode and the discharge electrode, the dust collection performance of the electrostatic precipitator decreases, and the concentration of the dust at the system exit increases.

本発明の操業方法では第3図に示す如く電気乗じん器の
乗じん性能が悪化した場合、その悪化分音ベンチュリー
スクラバーの圧損を太きくシ、乗じん性能を良くするこ
とにより、装置全体としての集じん性能を維持しようと
するものである。
In the operating method of the present invention, when the dust multiplier performance of the electric dust multiplier deteriorates as shown in Fig. 3, the pressure drop of the Venturi scrubber is increased to compensate for the deterioration and the dust multiplier performance is improved, thereby improving the dust multiplier performance as a whole. The aim is to maintain the dust collection performance of

尚第4図に集じん極、放電極同時洗浄方式の湿式電気乗
じん器の洗浄中、洗浄前後におけるベンチュリースクラ
バーの圧損制御ループの一例を示す。
FIG. 4 shows an example of the pressure drop control loop of a venturi scrubber before and after cleaning during cleaning of a wet electrostatic multiplier that uses a simultaneous cleaning method for dust collecting electrodes and discharge electrodes.

第4図において■、■、■、■の各点は以下の動作を示
す。
In FIG. 4, the points ■, ■, ■, and ■ indicate the following operations.

■点;洗浄指令タイマー ON。■Point: Cleaning command timer is ON.

この位置でベンチュリースクラバー圧損上限設定値にな
るよう可動ダンパー駆動指令ON。
At this position, turn on the movable damper drive command so that the venturi scrubber pressure drop upper limit setting value is reached.

■点;ベンチーリースクラバー圧損上限設定完了と同時
に洗浄開始 ■点;洗浄完了と同時にベンチュリースクラバー圧損下
限設定値になるよう可動ダンパー駆動指令ON。
Point ■: Cleaning starts as soon as the venturi scrubber pressure drop upper limit setting is completed.■ point: The movable damper drive command is turned ON so that the venturi scrubber pressure drop lower limit setting value is reached as soon as cleaning is completed.

■点;ベンチュリースクラバー圧損下限位置尚ペンテ−
リースクラバー上、下限圧損設定値は、ガス量等系の状
態量が安定している場合は開度設定にしても良い。
■Point: Venturi scrubber pressure drop lower limit position
The upper and lower limit pressure loss setting values for the lease scrubber may be set to the opening degree if the state quantities of the system, such as the gas amount, are stable.

次に本操業方法を高炉ガス清浄システムに適用した場合
についでその利点を述べる。
Next, we will discuss the advantages of this operating method when applied to a blast furnace gas cleaning system.

高炉ガス清浄装置は一般にダストキャツチャ−(DC)
+ilベンチュチュスクラバー十第2ペンチ−リースク
ラバーで構成されているが近年の省エネニーズによシ炉
頂圧力回収タービ2(TRT)が後流側に設置され清浄
ガスの余剰圧力を電力として回収している。しかるに上
記ガス清浄装置のヶEEヮ、わ、。八%。い、必要とさ
れている。
Blast furnace gas cleaning equipment is generally a dust catcher (DC).
It consists of a ventilator scrubber and a ventilator scrubber, but due to recent energy saving needs, a furnace top pressure recovery turbine 2 (TRT) is installed on the downstream side to recover the excess pressure of the clean gas as electricity. ing. However, the gas purifier mentioned above is... Eight%. Yes, it is needed.

一方、高炉ガス清浄装置としてダストキャツチャ−(D
C)+第1ベンチュリースクラバー十電気集じん器を使
った場合、全圧損は約500 mmAqで良く。約35
oommAq の圧力が炉頂圧力回収タービンの電力増
に結びつく、シかるに電気乗じん器は前述した如く捕集
したダストを除去する期間集じん性能が悪くなるため出
口台じん量が多くなる。このダストにより炉頂圧力回収
タービンのダスト(・ラブル、又、後流側高炉ガス利用
設備のダストトラブルが発生し、時にはタービン羽根の
破壊につながる問題となるため未だにこの/ステムは高
圧高炉で実機化されていない。
On the other hand, a dust catcher (D
C) + 1st Venturi Scrubber When using an electrostatic precipitator, the total pressure drop should be approximately 500 mmAq. Approximately 35
The pressure of oommAq leads to an increase in the electric power of the furnace top pressure recovery turbine.However, as mentioned above, the dust collection performance of the electric dust multiplier deteriorates during the period of removing the collected dust, so the amount of dust at the outlet increases. This dust causes dust (rubble) in the top pressure recovery turbine and dust troubles in the blast furnace gas utilization equipment on the downstream side, sometimes leading to the destruction of the turbine blades. has not been standardized.

ところが本発明の操業方法を使えば、電気乗じん型洗浄
時は炉頂圧力回収タービンの回収圧力エネルギーは減少
するものの炉頂圧力回収タービンその他機器のダストト
ラブルは防止できるためその信頼性が上りベンチュリー
スクラバー十電気集じん器システムを高炉ガス清浄装置
として問題なく使えるようになシそのメリットは大きい
However, if the operating method of the present invention is used, although the recovery pressure energy of the top pressure recovery turbine decreases during electroplating type cleaning, it is possible to prevent dust troubles in the top pressure recovery turbine and other equipment, increasing its reliability. The scrubber 10 electrostatic precipitator system can now be used as a blast furnace gas cleaning device without any problems, and the benefits are great.

尚ベンチュリースクラバーの圧損金変える方法としては
種々存在するが主なものを例示すると1)可動ダンパー
開度を変える方法 2)マルチスロートの通ガス数を変える方法3)給水量
を変える方法等がある。
There are various ways to change the pressure loss of a Venturi scrubber, but the main ones include 1) changing the opening of the movable damper, 2) changing the number of gases through the multi-throat, and 3) changing the amount of water supplied. .

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

第1図はベンチュリースクラバーの圧損と集じん効率の
関係を示す図 第2図は電気乗じん器の荷電電圧と集じん効率の関係を
示す図 第3図は本発明の詳細な説明するグラフ第4図は本発明
方法の一実施例全説明するグラフである。
Figure 1 shows the relationship between the pressure drop and dust collection efficiency of a venturi scrubber. Figure 2 shows the relationship between the charging voltage and dust collection efficiency of an electric dust multiplier. Figure 3 is a graph explaining the details of the present invention. FIG. 4 is a graph fully illustrating one embodiment of the method of the present invention.

Claims (1)

【特許請求の範囲】[Claims] ペンチ−リースクラバーと電気集じん器を直列に配置し
てなる集じん/ステムに於いて、電気集じん器の集じん
極や放電極に旧着したダストを除去する期間のベンチュ
リースクラバーの圧力損失を、該ゲスl−k除去しない
期間のべ/チュリースクラバーの圧力損失より大きくす
ることを特徴とする集じん装置の操業方法
In a dust collector/stem consisting of a venturi scrubber and an electrostatic precipitator arranged in series, the pressure loss of the venturi scrubber during the period of removing old dust attached to the collecting electrode or discharge electrode of the electrostatic precipitator. A method for operating a dust collector, characterized in that the pressure drop is made larger than the pressure loss of the Baturi scrubber during the period in which the gas l-k is not removed.
JP56101286A 1981-07-01 1981-07-01 Method of operating dust collector Pending JPS586389A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56101286A JPS586389A (en) 1981-07-01 1981-07-01 Method of operating dust collector

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56101286A JPS586389A (en) 1981-07-01 1981-07-01 Method of operating dust collector

Publications (1)

Publication Number Publication Date
JPS586389A true JPS586389A (en) 1983-01-13

Family

ID=14296607

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56101286A Pending JPS586389A (en) 1981-07-01 1981-07-01 Method of operating dust collector

Country Status (1)

Country Link
JP (1) JPS586389A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008202071A (en) * 2007-02-19 2008-09-04 Nippon Steel Engineering Co Ltd Method for operating blast furnace gas cleaning facility
JP2008208405A (en) * 2007-02-24 2008-09-11 Nippon Steel Engineering Co Ltd Facility for cleaning blast furnace gas and operation method therefor

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5014504A (en) * 1973-06-13 1975-02-15
JPS5521545A (en) * 1978-08-02 1980-02-15 Nippon Steel Corp Blast furnace gas purifying facility

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5014504A (en) * 1973-06-13 1975-02-15
JPS5521545A (en) * 1978-08-02 1980-02-15 Nippon Steel Corp Blast furnace gas purifying facility

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008202071A (en) * 2007-02-19 2008-09-04 Nippon Steel Engineering Co Ltd Method for operating blast furnace gas cleaning facility
JP2008208405A (en) * 2007-02-24 2008-09-11 Nippon Steel Engineering Co Ltd Facility for cleaning blast furnace gas and operation method therefor

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