JPH11319630A - Dry process electric duct collector and operation thereof - Google Patents

Dry process electric duct collector and operation thereof

Info

Publication number
JPH11319630A
JPH11319630A JP15389398A JP15389398A JPH11319630A JP H11319630 A JPH11319630 A JP H11319630A JP 15389398 A JP15389398 A JP 15389398A JP 15389398 A JP15389398 A JP 15389398A JP H11319630 A JPH11319630 A JP H11319630A
Authority
JP
Japan
Prior art keywords
gas flow
flow path
dust
gas
rated
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.)
Granted
Application number
JP15389398A
Other languages
Japanese (ja)
Other versions
JP3626344B2 (en
Inventor
Atsushi Katagawa
篤 片川
Toshio Katsube
利夫 勝部
Ryoichi Miyataka
良一 宮高
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP15389398A priority Critical patent/JP3626344B2/en
Publication of JPH11319630A publication Critical patent/JPH11319630A/en
Application granted granted Critical
Publication of JP3626344B2 publication Critical patent/JP3626344B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To prevent a dry process electric dust collector from being an excessive design at a normal rated operational time and also to prevent concentration of soot and dust at the outlet of the dust collector from being over a regulated value at the overshoot time. SOLUTION: A gas flow passage 4 consisting of plural numbers of chambers arranged in parallel is provided in the dry process electric dust collector 2, and the gas flow passage 4 is provided in excessive one chamber for hammering a dust collection electrode plate, besides the gas flow passage group provided with a space corresponding to the rated gas flow rate at the normal operation time. At the hammering time of the dust collection electrode in the rated gas flow rate time at a periodical normal operation time of respective chambers, a gas flow in the gas flow passage 4 of the excessive one chamber is shut down and exhaust gas of the rated flow rate is subjected to a dust collection treatment without any trouble by utilizing other whole chambers, and in the case that the gas flow rate is over the rated gas flow rate in the overshoot time in a load increasing process of a combustion device, the exhaust gas is introduced to the whole chambers of the gas flow passage 4 including the excessive one chamber to collect the dust, and during this time the periodical hammering of the dust collection electrode in the whole chamber is not performed.

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、ボイラ等の燃焼装
置の排ガス処理装置及びその一構成要素である乾式電気
集塵装置に係り、特に燃焼装置の負荷上昇におけるオー
バーシュート時の乾式電気集塵装置の過負荷を防止する
のに好適な乾式電気集塵装置の運用方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas treatment apparatus for a combustion apparatus such as a boiler and a dry electric dust collector which is one of the components thereof, and more particularly to a dry electric dust collector at the time of overshooting when the load of the combustion apparatus rises. The present invention relates to a method for operating a dry electric precipitator suitable for preventing overload of the apparatus.

【0002】[0002]

【従来の技術】大気汚染防止のため、ボイラ排ガス処理
装置として排ガス中の煤塵を除去する乾式電気集塵装置
が広く実用化されている。このボイラ排ガス処理装置の
中の一構成装置である乾式電気集塵装置を図5に示す。
火力発電所等のボイラから発生した排ガス1はボイラ排
ガス流路の後流側に設置された乾式電気集塵装置22に
おいて煤塵が除去され、処理ガス3は必要に応じて乾式
電気集塵装置22の後流に設置された図示しない脱硫装
置において硫黄酸化物(SO2)が除去され、その後、
煙突より排出される。
2. Description of the Related Art In order to prevent air pollution, dry-type electric precipitators for removing dust in exhaust gas have been widely used as boiler exhaust gas treatment devices. FIG. 5 shows a dry-type electrostatic precipitator, which is a component of the boiler exhaust gas treatment apparatus.
Exhaust gas 1 generated from a boiler such as a thermal power plant is subjected to removal of dust in a dry electric precipitator 22 installed on the downstream side of the boiler exhaust gas passage. Sulfur oxide (SO 2 ) is removed by a desulfurization device (not shown) installed downstream of
Emitted from the chimney.

【0003】乾式電気集塵装置22では集塵電極板上に
捕集された煤塵を回収するために定期的に集塵電極板
(図示せず)の槌打を行い、集塵電極板に衝撃を与えて
煤塵を下方に落下させて煤塵を回収している。
In the dry electric precipitator 22, a dust collecting electrode plate (not shown) is regularly hammered to collect dust collected on the precipitating electrode plate, and an impact is applied to the precipitating electrode plate. To collect the dust by dropping the dust downward.

【0004】ここで、集塵電極板の槌打時に煤塵が排ガ
ス中へ飛散するのを防ぐため、乾式電気集塵装置22内
部は複数のガス流路24を形成する室が並列配置されて
おり、各室ごとにガス流れを遮断できるダンパ25、2
6が各ガス流路24の入口および/または出口に設けら
れている。
Here, in order to prevent dust from being scattered into the exhaust gas when the dust collecting electrode plate is hammered, chambers forming a plurality of gas passages 24 are arranged in parallel inside the dry electric dust collecting device 22. , Dampers 25, 2 that can shut off gas flow for each chamber
6 are provided at the inlet and / or outlet of each gas flow path 24.

【0005】そして、集塵電極板の槌打は各室のガス流
路24毎に行われるが、集塵電極板の槌打時には、各ガ
ス流路24の入口および/または出口に設けられたダン
パ25、26を閉じて排ガス流れを遮断することにより
煤塵が排ガス中へ再飛散するのを防止している。このた
め、図5に示すように常時、集塵電極板の槌打をするガ
ス流路24の一室は排ガスの流れが遮断されるので、乾
式電気集塵装置22を設計する上では、ボイラ排ガスの
全流量の流通に必要なスペースに対応した室数のガス流
路24の他に一室分の余分なガス流路24が設けられて
いる。
[0005] The dust collecting electrode plate is hammered for each gas passage 24 in each chamber. When the dust collecting electrode plate is hammered, the dust collecting electrode plate is provided at the inlet and / or outlet of each gas flow passage 24. By closing the dampers 25 and 26 to shut off the exhaust gas flow, the dust is prevented from re-scattering into the exhaust gas. For this reason, as shown in FIG. 5, the flow of the exhaust gas is always shut off in one chamber of the gas flow path 24 where the dust collecting electrode plate is hammered. An extra gas passage 24 for one chamber is provided in addition to the number of gas passages 24 corresponding to the space required for the flow of the entire flow rate of the exhaust gas.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、ボイラ
負荷立上げ経過時間またはボイラ負荷増加経過時間とボ
イラ出口ガス流量の関係を図3に示すが、ボイラの負荷
が上昇してオーバーシュートになると一時的に定格ガス
流量を超えた排ガス流量となる場合があり、その場合に
は乾式電気集塵装置が過負荷となるため、煤塵の除去効
率が低下して乾式電気集塵装置出口煤塵濃度が規制値を
超えてしまう問題があった。
However, FIG. 3 shows the relationship between the boiler load rise elapsed time or the boiler load increase elapsed time and the boiler outlet gas flow rate. The exhaust gas flow rate may exceed the rated gas flow rate in such a case.In this case, the dry type dust collector will be overloaded, so the dust removal efficiency will decrease and the dust concentration at the outlet of the dry type dust collector will fall below the regulated value. There was a problem that exceeded.

【0007】また、あらかじめオーバーシュートを考慮
して、その時に乾式電気集塵装置出口煤塵濃度が規制値
を超えないように乾式電気集塵装置を設計した場合に
は、通常の定格運転時に対して乾式電気集塵装置には未
使用の装置部分ができ、過剰設計となり設備費が増加す
る問題があった。
Further, in consideration of the overshoot in advance, if the dry-type electrostatic precipitator is designed so that the dust concentration at the outlet of the dry-type electric precipitator does not exceed the regulation value at that time, the normal operation of the dry-type electrostatic precipitator may be reduced. The dry type electrostatic precipitator has a problem that an unused device part is formed, which is excessively designed and increases equipment costs.

【0008】本発明の課題は、通常の定格運転時に対し
て乾式電気集塵装置が過剰設計とならずに、かつオーバ
ーシュート時に乾式電気集塵装置出口煤塵濃度が規制値
を超えないようにすることにある。
An object of the present invention is to prevent the dry electric precipitator from being excessively designed with respect to a normal rated operation and to prevent the concentration of dust at the outlet of the dry electric precipitator from exceeding a regulation value during overshoot. It is in.

【0009】[0009]

【課題を解決するための手段】上記課題を達成するため
本発明の構成は以下のとおりである。燃焼装置から排出
する排ガス流路に設けられ、複数の室に分割されて並列
配置されたガス流路群と、各ガス流路の入口および/ま
たは出口ごとに設けられたガス流れを遮断するダンパを
備えた乾式電気集塵装置において、定格ガス流量時に各
ガス流路ごとに順次行う定期的な集塵電極板槌打時に
は、当該集塵電極板槌打を行うガス流路の入口および/
または出口に設けたダンパを閉じてガス流路を遮断し、
燃焼装置の負荷上昇におけるオーバーシュート時に定格
ガス流量を超えたガス流量となる場合には全室のガス流
路に排ガスを導いて集塵を行い、この間は各室での前記
集塵電極板槌打を行わない乾式電気集塵装置の運用方法
である。
The structure of the present invention to achieve the above object is as follows. A gas flow path group provided in an exhaust gas flow path discharged from a combustion device, divided into a plurality of chambers, and arranged in parallel, and a damper for shutting off a gas flow provided for each inlet and / or outlet of each gas flow path In a dry-type electrostatic precipitator equipped with: a regular dust collecting electrode plate hammer that is sequentially performed for each gas channel at a rated gas flow rate, the inlet of the gas channel performing the dust collecting electrode plate hammer and / or
Or close the gas path by closing the damper provided at the outlet,
If the gas flow exceeds the rated gas flow at the time of overshoot in the load rise of the combustion device, the exhaust gas is guided to the gas passages of all the rooms to collect dust, and during this time, the dust collecting electrode plate hammer in each room is used. This is a method of operating a dry electric precipitator without hitting.

【0010】このとき、燃焼装置の負荷信号とあらかじ
め定められた燃焼装置の負荷上昇パターンに基づき、オ
ーバーシュートとなる時期を予測し、オーバーシュート
となる前に全室のガス流路の入口および/または出口に
設けたダンパを全開として全室のガス流路に排ガスを導
いて集塵を行うことが望ましい。
At this time, the timing of overshoot is predicted based on the load signal of the combustion device and a predetermined load rise pattern of the combustion device, and before the overshoot occurs, the inlets and / or the gas flow paths of the gas passages of all the chambers are set. Alternatively, it is desirable to collect dust by fully opening the damper provided at the outlet and guiding the exhaust gas to the gas passages of all the rooms.

【0011】従って、本発明の乾式電気集塵装置におい
ては、集塵電極板槌打を行う一室以外の全室のガス流路
の集塵負荷の合計が定格ガス流量に対応し、集塵電極板
槌打を行う室を設けない状態での全室のガス流路の集塵
負荷の合計がオーバーシュート時のガス流量に対応する
ように設計される。
Therefore, in the dry electric precipitator according to the present invention, the sum of the dust collection loads of the gas passages in all the chambers except the one in which the dust collecting electrode plate is hammered corresponds to the rated gas flow rate. It is designed such that the total dust collection load of the gas passages of all the chambers in a state where no chamber for performing the electrode plate hammering is provided corresponds to the gas flow rate at the time of overshoot.

【0012】また、上記乾式電気集塵装置の運用方法を
実現するためには、次のような乾式電気集塵装置が用い
られる。すなわち、燃焼装置からの負荷信号に基づき定
格ガス流量であると判断された時には定格運転パターン
信号により各ガス流路ごとに順次定期的に集塵電極板槌
打を行うために、当該集塵電極板槌打を行うガス流路の
入口および/または出口に設けたダンパを閉じてガス流
路を遮断し、燃焼装置からの負荷信号に基づきボイラ負
荷上昇時と判断された時には、あらかじめ定めたボイラ
負荷上昇パターン信号により、オーバーシュートとなる
時期を予測し、オーバーシュートとなる前に全室の入口
および/または出口に設けたダンパを全開として、全て
のガス流路にガスを導入する制御を行う制御装置と、前
記制御装置により駆動制御される各室の入口および/ま
たは出口に設けたダンパをそれぞれ開閉するための開閉
装置とを設けた乾式電気集塵装置である。
Further, in order to realize the operation method of the above-mentioned dry electric dust collector, the following dry electric dust collector is used. That is, when it is determined that the gas flow rate is the rated gas flow rate based on the load signal from the combustion device, the dust collection electrode plate is hammered periodically for each gas flow path in accordance with the rated operation pattern signal. A damper provided at the inlet and / or outlet of the gas flow channel for hammering is closed to shut off the gas flow channel, and when it is determined that the boiler load is increasing based on a load signal from the combustion device, a predetermined boiler is set. The overshoot timing is predicted based on the load rise pattern signal, and before the overshoot occurs, the dampers provided at the entrances and / or exits of all the chambers are fully opened to control the gas to be introduced into all gas flow paths. A dry-type electric power collector provided with a control device and opening and closing devices for respectively opening and closing dampers provided at an entrance and / or an exit of each of the rooms driven and controlled by the control device. It is a device.

【0013】また、本発明には上記乾式電気集塵装置を
燃焼装置から排出する排ガスの流路に配置した排ガス処
理装置も含まれる。また、上記燃焼装置としては、ボイ
ラ、ゴミ焼却炉、熱風炉などであり、燃焼装置の負荷信
号としては、排ガス流量、ボイラ発電出力要求量、燃料
指令などである。
The present invention also includes an exhaust gas treating apparatus in which the above-mentioned dry type electrostatic precipitator is arranged in a flow path of exhaust gas discharged from a combustion device. The combustion device is a boiler, a refuse incinerator, a hot blast stove, or the like, and the load signal of the combustion device is an exhaust gas flow rate, a required amount of boiler power generation output, a fuel command, or the like.

【0014】[0014]

【作用】上記したように、本発明の乾式電気集塵装置に
おいて、複数の室からなるガス流路群の合計スペースを
通常運転時の定格ガス流量分に対応させ、前記ガス流路
群以外に、集塵電極板槌打を行うための余分な一室分の
ガス流路を設けておき、各室の定期的な通常運転時の定
格ガス流量時における集塵電極板槌打時には、前記余分
な一室のガス流路の入口および/または出口に設けたダ
ンパを全閉とし、当該ガス流路内でのガス流れを遮断
し、定格の排ガス流量はその他の全室を利用して支障無
く集塵処理を行うことができる。
As described above, in the dry electrostatic precipitator of the present invention, the total space of the gas flow path group consisting of a plurality of chambers is made to correspond to the rated gas flow rate during normal operation, and the space other than the gas flow path group is used. In addition, an extra gas flow path for one chamber for hammering the dust collecting electrode plate is provided, and when the hammering the dust collecting electrode plate at the rated gas flow rate during regular normal operation of each chamber, the extra The dampers provided at the inlet and / or outlet of one of the gas flow paths are fully closed to shut off the gas flow in the gas flow path, and the rated exhaust gas flow rate can be safely used by using all other chambers. Dust collection processing can be performed.

【0015】また、燃焼装置の負荷上昇過程におけるオ
ーバーシュート時に乾式電気集塵装置の定格ガス流量を
超えたガス流量となる場合には、前記余分の一室を含
め、ガス流路の全室に排ガスを導いて集塵を行い、この
間は全室において定期的な集塵電極板槌打を行わないこ
とにより、通常運転時には乾式電気集塵装置が過剰設計
とならずに、かつオーバーシュート時に乾式電気集塵装
置出口煤塵濃度が規制値を超えない運転が可能となる。
If the gas flow rate exceeds the rated gas flow rate of the dry electric precipitator at the time of overshoot in the process of increasing the load of the combustion device, if the gas flow rate exceeds the rated gas flow rate of the dry electric precipitator, all the chambers of the gas flow path, including the extra chamber, will Dust is collected by guiding the exhaust gas.During this period, the regular dust collecting electrode plate is not hammered in all rooms. Operation in which the dust concentration at the outlet of the electric precipitator does not exceed the regulation value becomes possible.

【0016】[0016]

【発明の実施の形態】本発明の実施の形態を図面と共に
説明する。図1、図2に示す乾式電気集塵装置は本発明
の実施の形態を示すものであり、図1に示す通り、火力
発電所等のボイラから発生した排ガス1はボイラ排ガス
流路の後流側に設置された乾式電気集塵装置2に導入さ
れた後、煤塵が除去され、処理ガス3は必要に応じて乾
式電気集塵装置2の後流に設置された図示しない脱硫装
置において硫黄酸化物(SO2)が除去され、その後煙
突より排出される。本発明では乾式電気集塵装置2は、
図2に示すように、ボイラの通常運転時には並列配置さ
れた複数のガス流路4の内の一室ごとに順次、その入口
および/あるいは出口に設けたダンパ5、6を全閉と
し、当該ガス流路4内の集塵電極板の荷電をゼロとして
槌打が行われ、定格の排ガス流量はその他の全室のガス
流路4を利用して支障無く集塵処理がなされる。
Embodiments of the present invention will be described with reference to the drawings. 1 and 2 show an embodiment of the present invention. As shown in FIG. 1, an exhaust gas 1 generated from a boiler such as a thermal power plant flows downstream of a boiler exhaust gas channel. After being introduced into the dry electric precipitator 2 installed on the side, dust is removed, and the processing gas 3 is subjected to sulfur oxidation in a desulfurizer (not shown) installed downstream of the dry electric precipitator 2 as necessary. The matter (SO 2 ) is removed and then discharged from the chimney. In the present invention, the dry electric precipitator 2 comprises:
As shown in FIG. 2, during normal operation of the boiler, the dampers 5 and 6 provided at the inlet and / or outlet of each of the plurality of gas passages 4 arranged in parallel are sequentially closed for each room. Hammering is performed by setting the charge of the dust collecting electrode plate in the gas flow path 4 to zero, and the rated exhaust gas flow rate is subjected to the dust collection processing without any trouble using the gas flow paths 4 in all other rooms.

【0017】また、ボイラ負荷上昇過程におけるオーバ
ーシュート時に定格ガス流量を超えたガス流量となる場
合には図1に示すように全室のガス流路4に排ガスを導
いて集塵を行い、この間は前記定期的な集塵電極板の槌
打を行わないこととする。
If the gas flow rate exceeds the rated gas flow rate during overshoot in the boiler load raising process, as shown in FIG. 1, the exhaust gas is guided to the gas passages 4 of all the rooms to collect dust. Shall not periodically hammer the collecting electrode plate.

【0018】例えば乾式電気集塵装置2に同一容積のガ
ス流路4が8室設けられていた場合、定格ガス流量が乾
式電気集塵装置2に導入される通常運転時には7室に通
ガスされており、負荷上昇過程におけるオーバーシュー
ト時(図3)には8室全部に通ガスすることになる。こ
の例では前記オーバーシュート時のガス流量増加に対し
て、ガス流路群の合計のスペースは8/7=1.14倍
(14%)の余裕があることになるが、これに対してオ
ーバーシュート時のガス流量増加割合は負荷上昇速度に
より異なる場合があるか、大体10%前後であるため前
記スペースで十分に対応ができる。
For example, when the dry electric precipitator 2 is provided with eight gas channels 4 having the same volume, the gas is passed through the seven chambers during normal operation in which the rated gas flow rate is introduced into the dry electric precipitator 2. During the overshoot in the load increasing process (FIG. 3), the gas flows through all eight chambers. In this example, the total space of the gas flow path group has a margin of 8/7 = 1.14 times (14%) with respect to the increase of the gas flow rate at the time of the overshoot. The rate of increase in the gas flow rate at the time of shooting may vary depending on the load rising speed, or is about 10%, so that the space can sufficiently cope with the above.

【0019】従来技術のオーバーシュート時に乾式電気
集塵装置出口煤塵濃度が規制値を超えないように過剰設
計した場合に本発明の過剰設計分(14%)にさらに過
剰設計追加分として約10%が加わるが、本発明の場合
は、この過剰設計追加分約10%が節約できる。ただ
し、オーバーシュート時に集塵電極板の槌打を行わない
分、集塵効率が低下することが考えられるが、オーバー
シュート時間は5分間程度であるので、このオーバーシ
ュート時間は通常運転時における各室の集電板の槌打ち
時間、例えば、8区画を2時間おきに槌打ち作業を行う
とすれば、約15分間以上に比べて短いので、集塵電極
板の槌打ちを行わないことによる集塵効率の低下は無視
しうる範囲である。
In the case of overshooting according to the prior art, when the dust concentration at the outlet of the dry-type electrostatic precipitator is overdesigned so as not to exceed the regulation value, about 10% is added to the overdesigned amount (14%) of the present invention and further overdesigned additional amount. However, in the case of the present invention, it is possible to save about 10% of this extra design addition. However, it is conceivable that dust collection efficiency is reduced by not hammering the dust collecting electrode plate during overshoot. However, since the overshoot time is about 5 minutes, this overshoot time is different from that in normal operation. The hammering time of the current collector plate in the room, for example, if hammering work is performed every two hours in eight sections, it is shorter than about 15 minutes or more. The reduction in dust collection efficiency is within a negligible range.

【0020】また、図4に示すようにボイラから負荷信
号11とあらかじめ定めたボイラ負荷上昇パターン(図
3に示すパターン)信号12に基づき、制御装置13で
オーバーシュートとなる時期を予測し、オーバーシュー
トとなる前にダンパ開閉装置14が駆動して各室の入口
および/あるいは出口に設けたダンパ5、6を全開する
とし、乾式電気集塵装置2の全室に排ガスを導いて集塵
を行うことによりオーバーシュート時のガス流量増加に
対して確実に対応できる。
As shown in FIG. 4, the controller 13 predicts the timing of overshoot on the basis of the load signal 11 from the boiler and a predetermined boiler load rise pattern (pattern shown in FIG. 3) signal 12, and the overshoot is predicted. Before the chute, the damper opening / closing device 14 is driven to fully open the dampers 5 and 6 provided at the entrance and / or the exit of each chamber, and the exhaust gas is guided to all the chambers of the dry electric dust collector 2 to collect dust. By doing so, it is possible to reliably cope with an increase in gas flow rate during overshoot.

【0021】また、通常運転時には定格運転パターン1
5が選択され、順次各ガス流路4のダンパ5、6が閉じ
られて、当該ガス流路内の集電電極板の槌打ちが行われ
る。こうして、乾式電気集塵装置2が過剰設計とならず
に、かつオーバーシュート時に乾式電気集塵装置2の出
口の煤塵濃度が規制値を超えない運転が可能となる。
In normal operation, the rated operation pattern 1
5 is selected, the dampers 5 and 6 of each gas flow path 4 are sequentially closed, and the current collecting electrode plate in the gas flow path is hammered. In this way, the dry electric precipitator 2 can be operated without being over-designed, and the dust concentration at the outlet of the dry electric precipitator 2 does not exceed the regulation value during overshoot.

【0022】[0022]

【発明の効果】本発明によれば、通常運転時に対して乾
式電気集塵装置が過剰設計とならずに、かつオーバーシ
ュート時に乾式電気集塵装置出口煤塵濃度か規制値を超
えない乾式電気集塵装置の運転が可能となる。
According to the present invention, the dry electric precipitator is not overdesigned during normal operation, and the dry electric precipitator outlet dust concentration at the time of overshoot does not exceed the regulation value. The operation of the dust device becomes possible.

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

【図1】 本発明の実施の形態の乾式電気集塵装置の説
明図である。
FIG. 1 is an explanatory diagram of a dry electric precipitator according to an embodiment of the present invention.

【図2】 本発明の実施の形態の乾式電気集塵装置の説
明図である。
FIG. 2 is an explanatory diagram of a dry electric precipitator according to an embodiment of the present invention.

【図3】 ボイラ負荷立ち上げ経過時間とボイラ処理ガ
ス流量の関係図である。
FIG. 3 is a diagram showing a relationship between a boiler load rising elapsed time and a boiler processing gas flow rate.

【図4】 本発明の実施の形態の乾式電気集塵装置の制
御系統図である。
FIG. 4 is a control system diagram of the dry electric precipitator according to the embodiment of the present invention.

【図5】 従来技術の乾式電気集塵装置の説明図であ
る。
FIG. 5 is an explanatory view of a conventional dry-type electrostatic precipitator.

【符号の説明】[Explanation of symbols]

1 排ガス 2 乾式電気集塵装置 3 処理ガス 4 ガス流路(室) 5、6 ダンパ 11 負荷信号 12 負荷上昇パターン 13 制御装置 14 ダンパ開閉装置 15 定格運転パターン DESCRIPTION OF SYMBOLS 1 Exhaust gas 2 Dry-type electrostatic precipitator 3 Processing gas 4 Gas flow path (chamber) 5, 6 Damper 11 Load signal 12 Load rise pattern 13 Control device 14 Damper opening / closing device 15 Rated operation pattern

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 燃焼装置から排出する排ガス流路に設け
られ、複数の室に分割されて並列配置されたガス流路群
と、各ガス流路の入口および/または出口ごとに設けら
れたガス流れを遮断するダンパを備えた乾式電気集塵装
置において、 定格ガス流量時に各ガス流路ごとに順次行う定期的な集
塵電極板槌打時には、当該集塵電極板槌打を行うガス流
路の入口および/または出口に設けたダンパを閉じてガ
ス流路を遮断し、燃焼装置の負荷上昇におけるオーバー
シュート時に定格ガス流量を超えたガス流量となる場合
には全室のガス流路に排ガスを導いて集塵を行い、この
間は各室での前記集塵電極板槌打を行わないことを特徴
とする乾式電気集塵装置の運用方法。
1. A gas flow path group provided in an exhaust gas flow path discharged from a combustion device, divided into a plurality of chambers and arranged in parallel, and a gas provided for each inlet and / or outlet of each gas flow path. In a dry-type electrostatic precipitator equipped with a damper that shuts off the flow, the gas flow path that performs the hammering operation during the regular hammering operation for each gas flow path at the rated gas flow rate If the gas flow exceeds the rated gas flow at the time of overshoot due to an increase in the load of the combustion device, the exhaust gas flows to all the chambers by closing the dampers provided at the inlet and / or outlet of And performing dust collection while the hammering of the dust collecting electrode plate in each chamber is not performed during this period.
【請求項2】 燃焼装置の負荷信号とあらかじめ定めら
れた燃焼装置の負荷上昇パターンに基づき、オーバーシ
ュートとなる時期を予測し、オーバーシュートとなる前
に全室のガス流路の入口および/または出口に設けたダ
ンパを全開として全室のガス流路に排ガスを導いて集塵
を行うことを特徴とする請求項1記載の乾式電気集塵装
置の運用方法。
2. An overshoot timing is predicted based on a load signal of a combustion device and a predetermined load rise pattern of the combustion device. 2. The method for operating a dry electric dust collecting apparatus according to claim 1, wherein the exhaust gas is guided to the gas passages of all the rooms by fully opening the damper provided at the outlet to collect dust.
【請求項3】 燃焼装置から排出する排ガス流路に設け
られ、複数の室に分割されて並列配置されたガス流路群
と、各ガス流路の入口および/または出口ごとに設けら
れたガス流れを遮断するダンパを備えた乾式電気集塵装
置において、 集塵電極板槌打を行う一室分以外の全室のガス流路の集
塵負荷の合計が定格ガス流量に対応し、集塵電極板槌打
を行う室を設けない状態での全室のガス流路の集塵負荷
の合計がオーバーシュート時のガス流量に対応するよう
に設計されたことを特徴とする乾式電気集塵装置。
3. A gas flow path group provided in an exhaust gas flow path discharged from a combustion device, divided into a plurality of chambers and arranged in parallel, and a gas provided for each inlet and / or outlet of each gas flow path. In a dry-type electrostatic precipitator equipped with a damper that shuts off the flow, the sum of the dust-collecting loads of the gas passages in all the rooms other than the room where the dust-collecting electrode plate is hammered corresponds to the rated gas flow rate. A dry-type electrostatic precipitator characterized in that the total dust-collecting load of the gas flow passages in all the chambers in a state where no chamber for hammering the electrode plate is provided corresponds to the gas flow rate during overshoot. .
【請求項4】 燃焼装置から排出する排ガスの流路に請
求項3記載の乾式電気集塵装置を配置したことを特徴と
する排ガス処理装置。
4. An exhaust gas treatment device comprising the dry electric precipitator according to claim 3, disposed in a flow path of exhaust gas discharged from the combustion device.
【請求項5】 燃焼装置から排出する排ガスに設けら
れ、複数の室に分割されて並列配置されたガス流路群
と、各ガス流路の入口および/または出口ごとに設けら
れたガス流れを遮断するダンパを備えた乾式電気集塵装
置において、 燃焼装置からの負荷信号に基づき定格ガス流量であると
判断された時には、定格運転パターン信号により各ガス
流路ごとに順次定期的に集塵電極板槌打を行うために、
当該集塵電極板槌打を行うガス流路の入口および/また
は出口に設けたダンパを閉じてガス流路を遮断し、燃焼
装置からの負荷信号に基づきボイラ負荷上昇時と判断さ
れた時には、あらかじめ定めたボイラ負荷上昇パターン
信号により、オーバーシュートとなる時期を予測し、オ
ーバーシュートとなる前に全室の入口および/または出
口に設けたダンパを全開として、全てのガス流路にガス
を導入する制御を行う制御装置と、 前記制御装置により駆動制御される各室の入口および/
または出口に設けたダンパをそれぞれ開閉するための開
閉装置とを設けたことを特徴とする乾式電気集塵装置。
5. A gas flow path group provided in an exhaust gas discharged from a combustion device, divided into a plurality of chambers and arranged in parallel, and a gas flow provided for each inlet and / or outlet of each gas flow path. In a dry-type electrostatic precipitator equipped with a shut-off damper, when it is determined that the gas flow rate is the rated gas flow rate based on the load signal from the combustion device, the dust collection electrode is periodically and periodically repeated for each gas flow path according to the rated operation pattern signal. In order to make a hammer,
When it is determined that the boiler load has risen based on a load signal from the combustion device, the damper provided at the inlet and / or outlet of the gas flow path for hammering the dust collection electrode plate is closed to shut off the gas flow path. Predict the timing of overshoot based on a predetermined boiler load rise pattern signal, and fully open the dampers provided at the entrance and / or exit of all rooms before overshoot to introduce gas into all gas flow paths A control device for performing control to perform the control, and an entrance and / or an entrance of each room that is driven and controlled by the control device
Or an opening / closing device for opening / closing a damper provided at an outlet, respectively.
【請求項6】 燃焼装置から排出する排ガスの流路に請
求項5記載の乾式電気集塵装置を配置したことを特徴と
する排ガス処理装置。
6. An exhaust gas treatment device, wherein the dry type electrostatic precipitator according to claim 5 is arranged in a flow path of exhaust gas discharged from the combustion device.
JP15389398A 1998-05-19 1998-05-19 Dry electrostatic precipitator and its operation method Expired - Fee Related JP3626344B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15389398A JP3626344B2 (en) 1998-05-19 1998-05-19 Dry electrostatic precipitator and its operation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15389398A JP3626344B2 (en) 1998-05-19 1998-05-19 Dry electrostatic precipitator and its operation method

Publications (2)

Publication Number Publication Date
JPH11319630A true JPH11319630A (en) 1999-11-24
JP3626344B2 JP3626344B2 (en) 2005-03-09

Family

ID=15572423

Family Applications (1)

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

Country Link
JP (1) JP3626344B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011512246A (en) * 2008-02-08 2011-04-21 アルストム テクノロジー リミテッド Method and apparatus for controlling ESP wrapping
JP2011194321A (en) * 2010-03-19 2011-10-06 Chugoku Electric Power Co Inc:The Method and device for controlling clogging of bag filter
JP2013244423A (en) * 2012-05-23 2013-12-09 Chugoku Electric Power Co Inc:The Dust collection efficiency optimization system and dust collection efficiency optimization method
CN104475255A (en) * 2014-11-26 2015-04-01 枣庄矿业(集团)有限责任公司蒋庄煤矿 Smoke distribution device in electric dust removal air inlet hood

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011512246A (en) * 2008-02-08 2011-04-21 アルストム テクノロジー リミテッド Method and apparatus for controlling ESP wrapping
JP2011194321A (en) * 2010-03-19 2011-10-06 Chugoku Electric Power Co Inc:The Method and device for controlling clogging of bag filter
JP2013244423A (en) * 2012-05-23 2013-12-09 Chugoku Electric Power Co Inc:The Dust collection efficiency optimization system and dust collection efficiency optimization method
CN104475255A (en) * 2014-11-26 2015-04-01 枣庄矿业(集团)有限责任公司蒋庄煤矿 Smoke distribution device in electric dust removal air inlet hood

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