JP2002045727A - Operation method for electric dust collector - Google Patents

Operation method for electric dust collector

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Publication number
JP2002045727A
JP2002045727A JP2000232882A JP2000232882A JP2002045727A JP 2002045727 A JP2002045727 A JP 2002045727A JP 2000232882 A JP2000232882 A JP 2000232882A JP 2000232882 A JP2000232882 A JP 2000232882A JP 2002045727 A JP2002045727 A JP 2002045727A
Authority
JP
Japan
Prior art keywords
dust
hammering
uncharged
operation method
dust collector
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
JP2000232882A
Other languages
Japanese (ja)
Inventor
Hidetoshi Yamauchi
秀敏 山内
Hideaki Sato
秀明 佐藤
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP2000232882A priority Critical patent/JP2002045727A/en
Publication of JP2002045727A publication Critical patent/JP2002045727A/en
Pending legal-status Critical Current

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  • Electrostatic Separation (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an operation method for an electric dust collector whereby the problems caused by the combustion of oily components and carbon in dust are solved and the decrease in dust collection efficiency can be prevented even when the percentage of added quick lime is increased. SOLUTION: This operation method is characterized in that in doing uncharged continuous hammering at regular intervals, a charged section is divided into a plurality of groups and the hammering is continuously carried out for a fixed time by shifting the hammering start time of each group.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、操業条件の変更等
により集塵効率が低下する場合、集塵効率を向上させる
ことのできる電気集塵装置の運転方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for operating an electric precipitator capable of improving dust collection efficiency when the dust collection efficiency is reduced due to a change in operating conditions or the like.

【0002】[0002]

【従来の技術】一般に、電気集塵装置では、稼働時間が
長くなればなるほど、集塵板表面にダストが堆積して集
塵効率が低下するから、この低下を抑制し、良好な集塵
効率を維持するために、図6に示すように、集塵板5を
槌打装置6により間欠的に槌打を行って付着、堆積した
ダストを機械的に除去している。
2. Description of the Related Art Generally, in an electric dust collector, as the operation time becomes longer, dust accumulates on the surface of a dust collecting plate to lower the dust collecting efficiency. As shown in FIG. 6, the dust collecting plate 5 is intermittently hammered by a hammering device 6 to mechanically remove the adhered and deposited dust, as shown in FIG.

【0003】しかし、焼結機の排ガスを処理する電気集
塵装置においては、原料の配合条件や操業条件によって
排ガスに含まれるダストの濃度、ダスト中に含まれる油
分、アルカリ成分、ダスト中水分が変化する。例えば、
ダスト中のアルカリ成分(Na,K)が、原料の通気性向上
のために、焼結原料の生石灰添加%によって、図5に示
すように大きく変わる。この場合は、ダスト中のアルカ
リ成分が、生石灰添加%が3.5%を越えると急激に増
加する傾向がある。
However, in an electric precipitator for treating exhaust gas from a sintering machine, the concentration of dust contained in the exhaust gas, oil content, alkali components, and moisture in the dust are reduced depending on the mixing conditions and operating conditions of the raw materials. Change. For example,
As shown in FIG. 5, the alkali components (Na, K) in the dust vary greatly depending on the quicklime addition percentage of the sintering raw material in order to improve the permeability of the raw material. In this case, the alkali component in the dust tends to increase rapidly when the percentage of quicklime added exceeds 3.5%.

【0004】特に、ダスト中に含まれる油分、アルカリ
成分およびダスト中水分は、槌打による集塵板堆積ダス
トの剥離を困難にしていると考えられている。この中、
ダスト中の油分に起因する剥離困難を解消する方法が、
特開平1−266866号で提案されている。これは、
電気集塵装置の入口ガス温度を150℃〜200℃に上
昇させ、この温度を長時間維持しながら、集塵板の連続
槌打を行い、集塵板に付着した含油ダスト層を除去した
後、集塵を再開するものである。
[0004] In particular, it is considered that oil, alkali components and moisture in the dust contained in the dust make it difficult to separate the dust deposited on the dust collecting plate by hammering. Among them,
A method to eliminate the difficulty of peeling due to oil in the dust,
It is proposed in Japanese Patent Application Laid-Open No. Hei 1-266866. this is,
After raising the inlet gas temperature of the electric precipitator to 150 ° C. to 200 ° C. and continuously maintaining the temperature for a long time, hammering the precipitating plate to remove the oil-containing dust layer attached to the precipitating plate , To resume dust collection.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、電気集
塵装置の入口ガス温度を上昇させて長時間保持して行う
特開平1−266866号の方法は、油分で集塵板に付
着、堆積したダストを剥離し易い性状に変えることがで
きるが、次のような点で問題がある。
However, the method disclosed in Japanese Patent Application Laid-Open No. 1-266866, in which the temperature of the inlet gas of the electric precipitator is raised and maintained for a long time, is disclosed in Japanese Patent Application Laid-Open No. Hei 1-266866. Can be changed to an easily peelable property, but there are problems in the following points.

【0006】焼結装置は不可避的に発生する漏風が多
く、排ガス中の酸素濃度が高いので、ダスト中の油分が
多いと、高温によりダスト中の油分や炭素分が燃焼する
ことがある。特に集塵板のダスト付着分布は一様でない
から、このような燃焼が発生すれば、集塵板が不均一な
加熱を受けるため曲損し、荷電できなくなり、集塵能力
が大幅に低下する。
In a sintering apparatus, a large amount of air leaks inevitably occur and the oxygen concentration in the exhaust gas is high. If the oil content in the dust is large, the oil content and the carbon content in the dust may be burned due to the high temperature. In particular, since the dust deposition distribution on the dust collecting plate is not uniform, if such combustion occurs, the dust collecting plate is subjected to uneven heating and thus bends, cannot be charged, and the dust collecting ability is greatly reduced.

【0007】また、図3に示すように、焼結原料の生石
灰添加%を増加してゆくと、ダストの移動速度ω(m/se
c)(集塵板に向かってダストが移動する速度、「ドイッ
チェ式:数1」より求められる。)が、A(0.03〜
0.04m/sec)からB(0.01m/sec)に減少するた
め、集塵効率が低下するという問題がある。
Further, as shown in FIG. 3, as the percentage of quicklime added to the sintering raw material is increased, the moving speed of dust ω (m / se
c) (the speed at which dust moves toward the dust collecting plate, which is obtained from the “Deutsch equation: Equation 1”), is A (0.03 to
Since it is reduced from 0.04 m / sec) to B (0.01 m / sec), there is a problem that the dust collection efficiency is reduced.

【0008】[0008]

【数1】 (Equation 1)

【0009】本発明は、ダスト中の油分、炭素分の燃焼
による問題を解消し、また、生石灰添加%を増加しても
集塵効率の低下を防止することのできる電気集塵装置の
運転方法を提供することを目的とする。
[0009] The present invention solves the problems caused by the burning of oil and carbon in dust, and also operates an electric precipitator capable of preventing a reduction in dust collection efficiency even when the amount of quicklime added is increased. The purpose is to provide.

【0010】[0010]

【課題を解決するための手段】本発明は上記の目的を、
以下の方法によって達成する。
SUMMARY OF THE INVENTION The present invention provides the above object,
This is achieved by the following method.

【0011】請求項1の方法は、一定間隔で無荷電連続
槌打を実施するにあたり、荷電区画を複数グループに分
け、各グループの槌打開始時間をずらして一定時間継続
して行うものである。
According to the first aspect of the present invention, when carrying out uncharged continuous hammering at regular intervals, the charged sections are divided into a plurality of groups, and the hammering start time of each group is shifted to perform the hammering continuously. .

【0012】この方法によれば、通常の間欠荷電槌打で
は剥離しないダスト層を、確実に剥離させることができ
る。また、各グループ毎に槌打開始時間をずらしている
ので、出口ダスト濃度の上昇を抑制することができる。
According to this method, the dust layer which does not peel off by ordinary intermittent charging hammer can be reliably peeled off. Further, since the hammering start time is shifted for each group, it is possible to suppress an increase in the outlet dust concentration.

【0013】請求項2の方法は、請求項1の方法におい
て、電気集塵装置入口ガス温度を130℃以下に維持し
て行うものである。
[0013] The method of claim 2 is the method of claim 1, wherein the temperature of the gas at the inlet of the electrostatic precipitator is maintained at 130 ° C or less.

【0014】この方法によれば、集塵板に付着したダス
ト中の油分、炭素分の燃焼によって発生する集塵板の曲
損、荷電不可状態を無くすことができる。このことは、
電気集塵装置入口ガス温度を130℃以下に限定する理
由でもある。
According to this method, it is possible to eliminate bending of the dust collecting plate caused by combustion of oil and carbon in dust attached to the dust collecting plate and a state in which charging is impossible. This means
This is also the reason for limiting the gas temperature at the inlet of the electrostatic precipitator to 130 ° C. or lower.

【0015】請求項3の方法は、請求項1または2の方
法において、焼結原料に生石灰を3.5%以上添加する
とき行うものである。
[0015] The method of claim 3 is performed in the method of claim 1 or 2 when 3.5% or more of quicklime is added to the sintering raw material.

【0016】この方法によれば、生石灰を多く添加した
ときに生じる集塵効率の低下を防止することができる。
According to this method, it is possible to prevent a reduction in dust collection efficiency caused when a large amount of quicklime is added.

【0017】[0017]

【発明の実施の形態】本発明は、前述した問題を解消す
るために、以下の条件下において運転することを特徴と
している。すなわち、その一つは、ダスト中の油分、炭
素分の燃焼によって発生する集塵板の曲損を防止するた
めに、電気集塵装置の入口ガス温度を通常温度(100
℃〜110℃)に維持する。その二は、集塵板の表面に
油分等により強固に付着したダスト層を剥離除去するた
めに、無荷電状態で行う無荷電連続槌打を一定間隔で行
う。その三は、無荷電連続槌打を広い範囲の集塵板につ
いて同時に行うことによる電気集塵装置出口ダスト濃度
の急激な上昇を防ぐために、無荷電連続槌打を同時に行
う集塵板範囲をできるだけ小範囲に設定する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention is characterized by operating under the following conditions in order to solve the above-mentioned problems. That is, one of them is to reduce the gas temperature at the inlet of the electric precipitator to a normal temperature (100 ° C.) in order to prevent the dust collecting plate from being bent due to the burning of oil and carbon in the dust.
C. to 110 C.). Second, in order to peel off and remove a dust layer firmly attached to the surface of the dust collecting plate due to oil or the like, uncharged continuous hammering performed in an uncharged state is performed at regular intervals. Third, in order to prevent a sudden increase in the dust concentration at the outlet of the electrostatic precipitator by simultaneously performing uncharged continuous hammering on a wide range of dust collectors, the range of dust collectors that simultaneously perform uncharged continuous hammering should be minimized. Set to a small range.

【0018】ここに、無荷電連続槌打とは、30〜40
分毎に1回の槌打を行う通常の間欠荷電槌打に対して、
無荷電状態で1分〜2分毎に1回槌打を行うものを言
う。
Here, uncharged continuous hammering means 30 to 40
For the usual intermittent charging hammer that performs one hammer every minute,
A hammer is performed once every 1 to 2 minutes in an uncharged state.

【0019】次に、本発明の実施の形態を図面に基づい
て説明する。先ず、電気集塵装置の荷電区画構成の一例
を、図2により説明する。この例の電気集塵装置1は、
平面で見て、中央に各々二つの集塵室を有するNo.1
集塵機とNo.2集塵機を配置し、No.1およびN
o.2集塵機の外側にNo.3集塵機のNo.3a集塵
室とNo.3b集塵室を配設している。各集塵室は、図
に示すように、荷電をオン・オフできる四つのセクショ
ン1s〜4sを持っている。
Next, an embodiment of the present invention will be described with reference to the drawings. First, an example of the configuration of the charging compartment of the electric precipitator will be described with reference to FIG. The electric precipitator 1 of this example has:
When viewed in a plane, No. 2 has two dust collecting chambers at the center. 1
Dust collector and No. No. 2 dust collector, and 1 and N
o. No. 2 on the outside of the dust collector. No. 3 dust collector No. 3a dust collection chamber and No. 3 3b A dust collection chamber is provided. As shown in the figure, each dust collection chamber has four sections 1 s to 4 s that can be turned on and off.

【0020】そして、焼結機からの排ガスは、線で表し
たダクトを→のように流れ、分流して各集塵機に入り、
ここで排ガス中に含まれているダストが捕集され、清浄
とったガスは、No.1集塵機とNo.3a集塵室分が
ブロワー2aで吸引され、No.2集塵機とNo.3b
集塵室集塵室分がブロワー2bで吸引されて、煙突3に
排出されて大気放散される。
Then, the exhaust gas from the sintering machine flows through the duct represented by a line as shown by →, is divided and enters each dust collector.
Here, dust contained in the exhaust gas was collected, and the cleaned gas was No. 1; No. 1 dust collector and No. 1 No. 3a dust collection chamber is sucked by the blower 2a. No. 2 dust collector and No. 2 3b
The dust collection chamber is sucked by the blower 2b, discharged to the chimney 3, and released to the atmosphere.

【0021】発明者等は、焼結原料に生石灰を3.65
%添加して操業を行っているとき、無荷電連続槌打を実
施する間隔を、2日と4日にして本発明方法の効果を調
べた。ここでは、間隔を2日にしたときの、各セクショ
ン毎の無荷電連続槌打スケジュールの例を図1に示す。
このスケジュールは、次の条件を満足するようにして編
成した。集塵機を二つのグループに分け、一つを1日
目に、残りの一つを2日目に行う。同時に、無荷電槌
打を行うものは、2セクションとし、1セクションの無
荷電連続槌打継続時間を2.5時間として、各セクショ
ンの槌打開始時刻を1.25時間だけずらす。ここで、
無荷電連続槌打を終えたセクションは、直ちに、通常の
荷電間欠槌打による集塵状態に戻すことは言うまでもな
い。
The present inventors have found that quick lime is used as a sintering raw material in an amount of 3.65.
%, The operation of the method of the present invention was carried out at intervals of 2 days and 4 days for performing uncharged continuous hammering. Here, FIG. 1 shows an example of the uncharged continuous hammering schedule for each section when the interval is set to two days.
This schedule was organized so as to satisfy the following conditions. Divide the dust collectors into two groups, one on day 1 and the other on day 2. At the same time, the uncharged hammer performs two sections, the uncharged continuous hammering duration of one section is 2.5 hours, and the hammering start time of each section is shifted by 1.25 hours. here,
It goes without saying that a section that has been subjected to uncharged continuous hammering immediately returns to the state of dust collection by ordinary intermittent charged hammering.

【0022】無荷電槌打間隔を2日として運転したとき
の集塵装置出口ダスト濃度(mg/Nm3)の推移を図4に示
した。本発明の運転を開始する前、集塵装置出口ダスト
濃度が50mg/Nm3であったが、本発明実施後、日の経過
とともに徐々に下がり、14日目には20mg/Nm3にな
り、その後数値は横這いとなるという予想以上のよい結
果が得られた。なお、3日目、一時的に、ダスト濃度が
急上昇しているのは、それまで厚く堆積していたダスト
が多量に剥離したものであり、その後は、このような現
象は認められない。また、無荷電槌打間隔を4日とする
運転も行ったが、図3のDに示すように、移動速度ω(m
/sec)が上がらず、集塵効率の向上は認められなかっ
た。従って、無荷電槌打間隔としては、1〜3日が望ま
しい。
FIG. 4 shows the change in the dust concentration at the outlet of the dust collector (mg / Nm 3 ) when the apparatus was operated with an uncharged hammering interval of 2 days. Before starting the operation of the present invention, although the dust collecting device outlet dust concentration was 50 mg / Nm 3, after the implementation of this invention, and gradually decreases with the passage of days, become 20 mg / Nm 3 to day 14, After that, the result was better than expected that the value was flat. On the third day, the dust concentration temporarily increased suddenly because a large amount of the dust that had accumulated so far was peeled off in a large amount. Thereafter, such a phenomenon was not observed. In addition, the operation was performed with an uncharged hammering interval of 4 days. However, as shown in FIG.
/ sec) did not increase, and no improvement in dust collection efficiency was observed. Therefore, the uncharged hammering interval is preferably 1 to 3 days.

【0023】[0023]

【発明の効果】本発明は、入口ガス温度を通常値にした
まま、一定間隔をもって無荷電連続槌を行うものである
から、電気集塵装置の入口ガス温度を上昇させることに
よるダスト中の油分、炭素分の燃焼による問題を解消
し、しかも、生石灰添加%の増加による集塵効率の低下
を防止できるという優れた効果が得られる。
According to the present invention, since the uncharged continuous hammer is performed at regular intervals with the inlet gas temperature kept at the normal value, the oil content in the dust by increasing the inlet gas temperature of the electrostatic precipitator is increased. In addition, it is possible to obtain an excellent effect that the problem caused by the burning of the carbon content can be solved and the dust collection efficiency can be prevented from lowering due to an increase in quicklime addition%.

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

【図1】本発明方法の各セクション毎の無荷電槌打スケ
ジュール例を示す図である。
FIG. 1 is a diagram showing an example of an uncharged hammering schedule for each section of the method of the present invention.

【図2】本発明方法を実施した電気集塵装置の荷電区画
構成を示す図である。
FIG. 2 is a diagram showing a configuration of a charged compartment of an electric dust collector in which the method of the present invention is performed.

【図3】焼結原料の生石灰添加%とダスト移動速度(m/s
ec)の関係散布図である。
Fig. 3 Sulfur raw material addition percentage of sintering raw material and dust transfer speed (m / s)
It is a relation scatter diagram of (ec).

【図4】本発明方法を実施したときの集塵装置出口ダス
ト濃度の推移図である。
FIG. 4 is a transition diagram of a dust concentration at a dust collector outlet when the method of the present invention is performed.

【図5】焼結原料の生石灰添加%とダスト中アルカリ%
の関係散布図である。
FIG. 5: Quicklime addition percentage of sintering raw material and alkali percentage in dust
FIG.

【図6】集塵板の槌打装置の斜視図である。FIG. 6 is a perspective view of a hammer of the dust collecting plate.

【符号の説明】[Explanation of symbols]

1 電気集塵装置 2a,2b ブロワー 3 煙突 1s〜4s セクション 5 集塵板 6 槌打装置 DESCRIPTION OF SYMBOLS 1 Electric dust collector 2a, 2b Blower 3 Chimney 1s-4s Section 5 Dust collecting plate 6 Hammering device

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】一定間隔で無荷電連続槌打を実施するにあ
たり、荷電区画を複数グループに分け、各グループの槌
打開始時間をずらして一定時間継続して行うことを特徴
とする電気集塵装置の運転方法。
The present invention is characterized in that, in performing uncharged continuous hammering at a constant interval, charged sections are divided into a plurality of groups, and the hammering start time of each group is shifted to perform continuous hammering. How to operate the device.
【請求項2】電気集塵装置入口ガス温度を130℃以下
に維持して行う請求項1記載の電気集塵装置の運転方
法。
2. The method for operating an electric precipitator according to claim 1, wherein the gas temperature at the inlet of the electric precipitator is maintained at 130 ° C. or lower.
【請求項3】焼結原料に生石灰を3.5%以上添加する
とき行う請求項1または2記載の電気集塵装置の運転方
法。
3. The method for operating an electric precipitator according to claim 1, wherein the operation is performed when 3.5% or more of quicklime is added to the sintering raw material.
JP2000232882A 2000-08-01 2000-08-01 Operation method for electric dust collector Pending JP2002045727A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000232882A JP2002045727A (en) 2000-08-01 2000-08-01 Operation method for electric dust collector

Publications (1)

Publication Number Publication Date
JP2002045727A true JP2002045727A (en) 2002-02-12

Family

ID=18725490

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012071280A (en) * 2010-09-29 2012-04-12 Chugoku Electric Power Co Inc:The Electrostatic dust collection system and electrostatic dust collection method
CN105880026A (en) * 2016-05-19 2016-08-24 江苏中建材环保研究院有限公司 Tapping dust cleaning time sequence of electrostatic precipitator for glass melting furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012071280A (en) * 2010-09-29 2012-04-12 Chugoku Electric Power Co Inc:The Electrostatic dust collection system and electrostatic dust collection method
CN105880026A (en) * 2016-05-19 2016-08-24 江苏中建材环保研究院有限公司 Tapping dust cleaning time sequence of electrostatic precipitator for glass melting furnace

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