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JP3228867B2 - Waste gas incinerator exhaust gas collection equipment and its operation method - Google Patents

Waste gas incinerator exhaust gas collection equipment and its operation method

Info

Publication number
JP3228867B2
JP3228867B2 JP00530996A JP530996A JP3228867B2 JP 3228867 B2 JP3228867 B2 JP 3228867B2 JP 00530996 A JP00530996 A JP 00530996A JP 530996 A JP530996 A JP 530996A JP 3228867 B2 JP3228867 B2 JP 3228867B2
Authority
JP
Japan
Prior art keywords
exhaust gas
white smoke
temperature
air
bag filter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP00530996A
Other languages
Japanese (ja)
Other versions
JPH09192430A (en
Inventor
正友 木原
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen 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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP00530996A priority Critical patent/JP3228867B2/en
Publication of JPH09192430A publication Critical patent/JPH09192430A/en
Application granted granted Critical
Publication of JP3228867B2 publication Critical patent/JP3228867B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

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

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)

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、バグフィルタおよ
び白煙防止装置を備えたごみ焼却炉の排ガス集塵設備お
よびその運転方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas collection system for a refuse incinerator provided with a bag filter and a white smoke prevention device, and a method of operating the same.

【0002】[0002]

【従来の技術】従来、ごみ焼却炉の起動・停止時や炉内
清掃時に排ガスの温度が低下すると、バグフィルタにお
いて排ガスの水分が凝縮し、ろ布の塩化カルシウムが潮
解して目詰まりが生じたり、ケーシングや管に露点腐食
が発生する。その対策として、 バグフィルタの排ガス入口と出口管にバイパス管を接
続し、低温の排ガスをバイパス管を介してバグフィルタ
をバイパスして排出するように構成されている。また、
バグフィルタの複数に区画して、その一部を低温排ガ
ス専用に使用するように構成することもある。さらに、
炉内清掃時には、汚染排ガスが発生した場合、バイパ
ス管を介してそのまま排出するか、または常時運転用の
バグフィルタとは別の清掃時専用バグフィルタを設置
し、これを通して排出する。
2. Description of the Related Art Conventionally, when the temperature of exhaust gas decreases when the incinerator is started / stopped or when the inside of the furnace is cleaned, moisture in the exhaust gas condenses in the bag filter, and calcium chloride in the filter cloth deliquesces, causing clogging. And dew-point corrosion on casings and pipes. As a countermeasure, a bypass pipe is connected to the exhaust gas inlet and outlet pipes of the bag filter, so that low-temperature exhaust gas is discharged by bypassing the bag filter via the bypass pipe. Also,
In some cases, the bag filter is divided into a plurality of parts, and a part of the bag filter is used exclusively for low-temperature exhaust gas. further,
When cleaning the inside of the furnace, if polluted exhaust gas is generated, the polluted exhaust gas is discharged as it is through a bypass pipe, or a dedicated bag filter for cleaning is provided separately from a bag filter for constant operation and discharged through the filter.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記のよう
に排ガスをバイパスさせると、起動・停止時など低温排
ガスによる大気汚染の問題が生じる。バグフィルタを
複数に区画すると製造コストが嵩むとともに、使用する
区画のろ布の閉塞や腐食は避けられない。では、設備
コストの増大や設置スペースの増大の問題がある。
However, if the exhaust gas is bypassed as described above, a problem of air pollution due to the low-temperature exhaust gas occurs at the time of starting and stopping. If the bag filter is divided into a plurality of sections, the manufacturing cost increases, and the filter cloth in the section to be used is inevitably blocked or corroded. Then, there is a problem of an increase in equipment cost and an installation space.

【0004】ところで、近年のごみ焼却施設では、煙突
から排出される排ガス中に水分が多く含まれると、特に
冬季など大気温度が低い場合、煙突から白煙が長く形成
される。これを防止するために、排ガス中に高温空気を
吹き込んで水分を希釈させてから排出する白煙防止装置
を装備することが多い。
[0004] In recent refuse incineration facilities, if the exhaust gas discharged from the chimney contains a large amount of water, white smoke is formed from the chimney for a long time especially when the atmospheric temperature is low such as in winter. In order to prevent this, a white smoke prevention device that blows high-temperature air into the exhaust gas to dilute the water and then discharges the diluted water is often provided.

【0005】本発明は、装備された白煙防止装置に着目
して、上記問題点を解決できるごみ焼却炉の排ガス集塵
設備およびその運転方法を提供することを目的とする。
An object of the present invention is to provide a waste gas incinerator exhaust gas collecting apparatus and a method for operating the same, which can solve the above-mentioned problems by focusing on the installed white smoke preventing apparatus.

【0006】[0006]

【課題を解決するための手段】上記目的を達成するため
に本発明のごみ焼却炉の排ガス集塵設備は、ごみ焼却炉
の排ガス管の途中に、集塵用バグフィルタが介在される
とともに、白煙防止装置から白煙防止用の高温空気を供
給する白煙防止空気供給管が排ガス管の排出部側に接続
されたごみ焼却炉の排ガス集塵設備において、基端部が
前記白煙防止空気供給管に接続されて先端部がバグフィ
ルタ入口の排ガス管に接続された加熱空気供給管を設
け、白煙防止空気供給管の先端側に第1開閉手段を介装
するとともに、加熱空気供給管の先端側に第2開閉手段
を介装し、ごみ焼却炉の起動時、停止時および炉内清掃
時に、バグフィルタ入口に設けられた排ガス温度検出手
段の信号に基づいて第1開閉手段および第2開閉手段を
操作し、バグフィルタ入口の排ガス中に白煙防止装置か
ら高温空気を供給して加熱し、排ガスの温度を制御する
排ガス温度制御装置を設けたものである。
Means for Solving the Problems To achieve the above object, a waste gas incinerator for a refuse incinerator according to the present invention has a dust filter and a dust filter interposed in the exhaust gas pipe of the refuse incinerator. A white smoke prevention air supply pipe for supplying high temperature air for preventing white smoke from a white smoke prevention device is connected to the discharge side of an exhaust gas pipe. A heating air supply pipe connected to the air supply pipe and having a distal end connected to an exhaust gas pipe at the bag filter inlet is provided, and a first opening / closing means is interposed at the distal end side of the white smoke prevention air supply pipe, and a heated air supply pipe is provided. A second opening / closing means is interposed at the end of the pipe, and the first opening / closing means is provided based on a signal from exhaust gas temperature detecting means provided at the bag filter inlet when starting up, shutting down, and cleaning the inside of the incinerator. Operate the second opening / closing means, and Heated by supplying hot air to the white smoke prevention device in the inlet of the exhaust gas, it is provided with a flue gas temperature control device for controlling the temperature of the exhaust gas.

【0007】またごみ焼却炉の排ガス集塵設備の運転方
法は、ごみ焼却炉の排ガス管の途中に集塵用バグフィル
タが介在され、排ガス管の排出部側に白煙防止装置から
白煙防止用の高温空気が供給されるごみ焼却炉の排ガス
集塵設備を運転するに際し、ごみ焼却炉の起動時、停止
時および炉内清掃時に、白煙防止装置により生成された
高温空気をバグフィルタの入口の排ガス中に導入して排
ガスを加熱し、排ガス温度を適性温度に保持するもので
ある。
[0007] The method of operating the flue gas dust collection equipment of a refuse incinerator is such that a dust filter is interposed in the exhaust gas pipe of the refuse incinerator, and a white smoke prevention device is provided on the discharge side of the exhaust gas pipe. When operating the waste gas incinerator of a refuse incinerator to which high-temperature air is supplied, the high-temperature air generated by the white smoke prevention device must be It is introduced into the exhaust gas at the inlet and heats the exhaust gas to maintain the temperature of the exhaust gas at an appropriate temperature.

【0008】上記構成によれば、白煙防止装置により生
成される高温空気を利用して排ガスを加熱することによ
り、新たな設備や高コストな特殊バグフィルタを使用し
なくても、バグフィルタに導入される排ガスを加熱して
除塵することができ、塩化カルシウムの潮解によるろ布
の目詰まりやケーシングや配管の露点腐食を防止できる
とともに、汚染された排ガスの大気への放出を防止する
ことができる。
[0008] According to the above configuration, the exhaust gas is heated by using the high-temperature air generated by the white smoke prevention device, so that the bag filter can be used without using a new facility or an expensive special bag filter. The introduced exhaust gas can be heated to remove dust, preventing clogging of the filter cloth and dew-point corrosion of casings and pipes due to deliquescence of calcium chloride, and preventing the release of polluted exhaust gas to the atmosphere. it can.

【0009】[0009]

【発明の実施の形態】ここで、本発明に係るごみ焼却炉
の排ガス集塵設備の実施の形態を図1に基づいて説明す
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Here, an embodiment of an exhaust gas collecting apparatus for a refuse incinerator according to the present invention will be described with reference to FIG.

【0010】ごみ焼却炉1の排ガス管2には、上流側か
ら排ガス中に水を噴霧して排ガス温度を調整する調温塔
3と、バグフィルタ4と排気ファン5と排気用煙突6が
介在設置されている。このバグフィルタ4には、ごみ焼
却炉1の休止中の温度低下による結露により露点腐食を
防止するための温風循環装置7が設けられており、また
煙突から排出される排ガスの白煙を防止するための白煙
防止装置8が装備されている。
In the exhaust gas pipe 2 of the refuse incinerator 1, a temperature control tower 3 for spraying water into the exhaust gas from the upstream side to adjust the exhaust gas temperature, a bag filter 4, an exhaust fan 5, and an exhaust chimney 6 are interposed. is set up. The bag filter 4 is provided with a hot air circulation device 7 for preventing dew point corrosion due to dew condensation due to a decrease in temperature during a period when the refuse incinerator 1 is stopped, and also prevents white smoke of exhaust gas discharged from the chimney. White smoke prevention device 8 is provided.

【0011】前記温風循環装置7は、バグフィルタ4と
排気ファン5の間の流量調整用第2エアダンパ11の上
流から、温風ガス加熱器12に接続された温風ガス回収
管13Aと、排ガス回収管13Aに介在された循環ファ
ン14と、循環空気加熱器12からバグフィルタ4の入
口に接続された温風ガス循環管13Bとが順次具備され
ている。そして温風ガス回収管13Aと温風ガス循環管
13Bには、温風ガスの流量調整用の温風エアダンパ1
5A,15Bがそれぞれ介在され、バグフィルタ4の出
口の排ガス管2の第2排ガス温度検出器16の検出値に
基づいて、温風ガス加熱器12のヒータによる加熱温度
が制御されるとともに、循環ファン13による循環温風
量が制御されて循環温風ガスを約150℃に保持するよ
うに構成される。
The hot-air circulation device 7 includes a hot-air gas recovery pipe 13A connected to a hot-air gas heater 12 from upstream of the flow rate adjusting second air damper 11 between the bag filter 4 and the exhaust fan 5. A circulation fan 14 interposed in the exhaust gas recovery pipe 13A and a hot air gas circulation pipe 13B connected from the circulation air heater 12 to the inlet of the bag filter 4 are sequentially provided. The hot air gas damper 1 for adjusting the flow rate of the hot air gas is provided in the hot air gas recovery pipe 13A and the hot air gas circulation pipe 13B.
5A and 15B are interposed respectively, and based on the detection value of the second exhaust gas temperature detector 16 of the exhaust gas pipe 2 at the outlet of the bag filter 4, the heating temperature of the heater of the hot air gas heater 12 is controlled and circulated. The amount of circulating hot air by the fan 13 is controlled to maintain the circulating hot air gas at about 150 ° C.

【0012】起動時・停止時および炉内清掃時など、除
塵したい排ガスが結露や塩化カルシウムの潮解を生じる
おそれがある低温時に、この排ガスに高温ガスを吹き込
んで加熱するための加熱ガスの条件としては、 (a)ガス
中に有害物質、特にHCl,SOX ,NOX が少ない
か、またはないこと、 (b)新たに装置を設置しないで、
加熱空気を利用できること、 (c)加熱空気量が排ガスを
充分に加熱できるとともに、バグフィルタ4の容量をオ
ーバーしない量であることが挙げられる。
When the exhaust gas to be removed is at a low temperature at which dew condensation or calcium chloride deliquesce may occur, such as during start-up / stop and when cleaning the furnace, conditions of the heating gas for blowing high-temperature gas into the exhaust gas to heat the exhaust gas are as follows. (A) The gas contains little or no harmful substances, especially HCl, SO x , NO x , and (b) no new equipment is installed.
(C) The amount of heated air can sufficiently heat the exhaust gas, and the amount of heated air does not exceed the capacity of the bag filter 4.

【0013】これを満足するものとして、本発明では白
煙防止装置8が利用されている。この白煙防止装置8
は、大気が低温の冬季などに排ガスに含まれる水分によ
り排ガスが白煙となって排出されるのを防止するため
に、200℃前後の高温空気を排ガス中に吹き込み、排
ガス中の水分を希釈させるものである。そしてこの白煙
防止装置8では、最大加熱空気量がごみ焼却炉1の最大
焼却時の排ガスに対して白煙を防止できる量に設定され
るため、起動時や停止時あるいは炉内清掃時に発生する
排ガス量が最大焼却時の排ガス量に比べて極めて少な
く、したがって排ガスを充分に加熱昇温することがで
き、バグフィルタ4の容量をオーバーすることもない。
To satisfy this, the present invention utilizes a white smoke prevention device 8. This white smoke prevention device 8
In order to prevent the exhaust gas from being emitted as white smoke due to the moisture contained in the exhaust gas in winter when the atmosphere is cold, high-temperature air at around 200 ° C is blown into the exhaust gas to dilute the moisture in the exhaust gas. It is to let. In the white smoke prevention device 8, since the maximum amount of heated air is set to an amount capable of preventing white smoke from the exhaust gas at the time of maximum incineration of the refuse incinerator 1, the maximum amount of generated air is generated at the time of startup, shutdown, or cleaning of the furnace. The amount of exhaust gas generated is extremely smaller than the amount of exhaust gas at the time of maximum incineration. Therefore, the exhaust gas can be sufficiently heated and heated, and the capacity of the bag filter 4 does not exceed the capacity.

【0014】すなわち前記白煙防止装置8は、送風ファ
ン21により供給される空気を約200℃前後に加熱可
能な白煙防止用空気加熱器22と、空気加熱器22から
排気ファン5と排気用煙突6の間の排ガス管2に高温の
白煙防止空気を供給する白煙防止空気供給管23とを備
え、白煙防止空気供給管23の出口側近傍には、第1開
閉手段である第1加熱空気用エアダンパ24が介在され
るとともに、白煙防止空気の流量検出器25が設けられ
ている。前記空気加熱器22に加熱源供給管26から供
給される加熱源は、運転中の他のごみ焼却炉からの高温
の低圧/高圧蒸気や都市ガス/灯油バーナの燃焼ガスが
使用される。
That is, the white smoke prevention device 8 includes a white smoke prevention air heater 22 capable of heating the air supplied by the blower fan 21 to about 200 ° C .; A white smoke prevention air supply pipe 23 for supplying high-temperature white smoke prevention air to the exhaust gas pipe 2 between the chimneys 6, and a first opening / closing means as a first opening / closing means near the outlet side of the white smoke prevention air supply pipe 23. 1 An air damper 24 for heated air is interposed, and a flow detector 25 for white smoke prevention air is provided. The heating source supplied from the heating source supply pipe 26 to the air heater 22 is high-temperature low-pressure / high-pressure steam from another incinerator in operation or combustion gas from a city gas / kerosene burner.

【0015】前記白煙防止装置8には、起動時、停止時
および炉内清掃時に、白煙防止用の高温空気を、排ガス
加熱に使用する本発明に係る加熱空気供給管31が設け
られている。すなわち、加熱空気供給管31の基端部は
白煙防止空気供給管23に接続され、先端部は第1エア
ダンパ17とバグフィルタ4の間の排ガス管2に接続さ
れており、排ガス管2の接続部近傍に第2開閉手段であ
る第2加熱空気用エアダンパ32が介在されている。ま
たこの接続部下流側の排ガス管2には、排ガス温度検出
手段である第1排ガス温度検出器18が介在され、この
第1排ガス温度検出器18の検出信号に基づいて第2加
熱空気用エアダンパ32を操作する排ガス温度制御装置
33が設けられ、これにより加熱空気の流量が制御され
て排ガスの温度をバグフィルタ4に適正な温度に制御す
ることができる。19は調温塔3から排出される排ガス
の流量を検出する排ガス流量検出器である。
The white smoke prevention device 8 is provided with a heated air supply pipe 31 according to the present invention, which uses hot air for white smoke prevention for exhaust gas heating during startup, shutdown, and furnace cleaning. I have. That is, the base end of the heated air supply pipe 31 is connected to the white smoke prevention air supply pipe 23, and the front end is connected to the exhaust gas pipe 2 between the first air damper 17 and the bag filter 4. A second heated air air damper 32 as a second opening / closing means is interposed in the vicinity of the connection portion. Further, a first exhaust gas temperature detector 18 as exhaust gas temperature detecting means is interposed in the exhaust gas pipe 2 on the downstream side of the connecting portion, and based on a detection signal of the first exhaust gas temperature detector 18, a second heated air air damper is provided. An exhaust gas temperature control device 33 for operating the exhaust gas 32 is provided, whereby the flow rate of the heated air is controlled so that the temperature of the exhaust gas can be controlled to an appropriate temperature for the bag filter 4. Reference numeral 19 denotes an exhaust gas flow rate detector that detects the flow rate of the exhaust gas discharged from the temperature control tower 3.

【0016】次に上記ごみ焼却炉の排ガス集塵設備の運
転方法を説明する。 1.ごみ焼却炉1の休止中は、温風ガス循環装置7によ
り、暖気運転される。すなわち第1エアダンパ17およ
び第2エアダンパ11が閉じられ、温風エアダンパ15
A,15Bが開かれる。そして、循環ファン14が起動
されるとともに、温風ガス加熱器12に加熱電源が供給
されて循環ガスが加熱され、第2排ガス温度検出器16
の検出信号により、循環ファン14の出力と温風ガス加
熱器12の加熱温度が制御されて循環温風ガスの温度が
約150℃前後に保持され、水蒸気の凝縮による露点腐
食などが防止される。
Next, an operation method of the exhaust gas dust collecting equipment of the above waste incinerator will be described. 1. While the refuse incinerator 1 is at rest, the warm air gas circulation device 7 performs a warm-up operation. That is, the first air damper 17 and the second air damper 11 are closed, and the warm air air damper 15 is closed.
A and 15B are opened. Then, while the circulation fan 14 is started, heating power is supplied to the hot air gas heater 12 to heat the circulation gas, and the second exhaust gas temperature detector 16
The output of the circulating fan 14 and the heating temperature of the hot air gas heater 12 are controlled by the detection signal to maintain the temperature of the circulating hot air gas at about 150 ° C., thereby preventing dew point corrosion and the like due to condensation of water vapor. .

【0017】2.ごみ焼却炉1の運転中で大気温度が低
く、排ガスによる水蒸気により煙突6から白煙が排出さ
れる状態では、白煙防止装置8が運転される。すなわ
ち、送風ファン21が起動されるとともに、空気加熱器
22に加熱源が供給され、第1加熱空気用エアダンパ3
2が開けられて排ガス中に高温の白煙防止用空気が供給
され、排ガス中の水分が希釈される。
2. In the state where the atmospheric temperature is low during the operation of the refuse incinerator 1 and the white smoke is discharged from the chimney 6 by the steam from the exhaust gas, the white smoke prevention device 8 is operated. That is, while the blower fan 21 is started, a heating source is supplied to the air heater 22 and the first heated air damper 3 is turned on.
2 is opened, high-temperature white smoke prevention air is supplied into the exhaust gas, and the moisture in the exhaust gas is diluted.

【0018】3.休止からごみ焼却炉1を立ち上げる起
動時は、 .温風ガス循環装置7が運転されている状態で、流量
検出器25により第1加熱空気用エアダンパ24が閉止
状態、第2加熱空気用エアダンパ32が閉止状態である
のが確認された後、空気加熱器22に加熱源が供給され
て暖気される。 .第1エアダンパ17および第2エアダンパ11が開
かれて排気ファン5が起動され、ごみ焼却炉1の助燃バ
ーナにより炉内が昇温される。この時の調温塔3出口の
排ガス温度は約20℃(室温)である。 .白煙防止装置8の送風ファン21を起動するととも
に、第2加熱空気用エアダンパ32を開け、加熱空気供
給管31から加熱空気を排ガス中に供給して加熱し、排
ガスの温度制御を開始する。この時の加熱空気は、20
0℃前後が望ましく、また排ガスの温度は120℃で、
第1排ガス温度検出器18の信号に基づいて排ガス温度
制御装置33により設定値になるように制御される。 .ごみ焼却炉1の加熱に伴い排ガスが120℃に達し
たら、第2加熱空気用エアダンパ32が閉じられて加熱
空気の供給が停止され、白煙防止装置8が停止される。
なおこの時、運転中の排ガスに白煙が生じるような状況
であれば、白煙防止装置8の運転が続行され、第2加熱
空気開閉ダンパ24が開けられて加熱空気が排出前の排
ガス中に供給され、白煙の発生が防止される。 .温風ガス循環装置7の温風エアダンパ15A,15
Bが閉じられ、循環ファン14が停止されるとともに、
温風ガス加熱器12が停止される。 .ごみ焼却炉1内の温度が850〜900℃になって
立ち上げが完了される。
3. When the waste incinerator 1 is started up after a pause, After the flow rate detector 25 confirms that the first heated air air damper 24 is in the closed state and the second heated air air damper 32 is in the closed state in the state where the hot air gas circulation device 7 is operating, the air A heating source is supplied to the heater 22 to be heated. . The first air damper 17 and the second air damper 11 are opened, the exhaust fan 5 is started, and the inside of the refuse incinerator 1 is heated by the auxiliary burner. At this time, the exhaust gas temperature at the outlet of the temperature control tower 3 is about 20 ° C. (room temperature). . The blower fan 21 of the white smoke prevention device 8 is started, the second heated air air damper 32 is opened, and heated air is supplied from the heated air supply pipe 31 into the exhaust gas to heat it, and the exhaust gas temperature control is started. The heating air at this time is 20
Desirably around 0 ° C, and the temperature of the exhaust gas is 120 ° C,
Based on a signal from the first exhaust gas temperature detector 18, the exhaust gas temperature control device 33 controls the exhaust gas temperature control device to become a set value. . When the exhaust gas reaches 120 ° C. due to the heating of the refuse incinerator 1, the second heated air air damper 32 is closed, the supply of the heated air is stopped, and the white smoke prevention device 8 is stopped.
At this time, if white smoke is generated in the exhaust gas during operation, the operation of the white smoke prevention device 8 is continued, the second heated air opening / closing damper 24 is opened, and the heated air is discharged from the exhaust gas before exhaust. And the generation of white smoke is prevented. . Hot air air dampers 15A, 15 of the hot air gas circulation device 7
B is closed, the circulation fan 14 is stopped,
The hot air gas heater 12 is stopped. . When the temperature in the refuse incinerator 1 reaches 850 to 900 ° C., the start-up is completed.

【0019】4.運転からごみ焼却炉1を立ち下げる停
止時は、上記と逆の手順で操作され、第1排ガス温度検
出器18の検出温度が120℃になると、第2加熱空気
用エアダンパ32を開けて加熱空気供給管31から加熱
空気を排ガス中に供給して加熱が開始され、温風ガス循
環装置7も起動される。立ち下げ完了後は、排気ファン
5を停止した後、第2加熱空気用エアダンパ32が閉じ
られ、空気加熱器22および送風ファン21が停止され
る。なお温風ガス循環装置7の運転は継続される。
4. When the refuse incinerator 1 is shut down from the operation, the operation is performed in the reverse order, and when the temperature detected by the first exhaust gas temperature detector 18 reaches 120 ° C., the second heated air air damper 32 is opened to open the heated air. Heating is started by supplying heated air into the exhaust gas from the supply pipe 31, and the hot air gas circulation device 7 is also started. After the shutdown is completed, the exhaust fan 5 is stopped, the second heated air air damper 32 is closed, and the air heater 22 and the blower fan 21 are stopped. The operation of the hot air gas circulation device 7 is continued.

【0020】5.炉内清掃により排ガスが排出される場
合にも、起動時と同様に排ガスを加熱してバグフィルタ
4に導入すればよい。
[5] Even when the exhaust gas is discharged by the cleaning inside the furnace, the exhaust gas may be heated and introduced into the bag filter 4 in the same manner as at the time of startup.

【0021】上記実施の形態によれば、ごみ焼却炉1の
起動時、停止時および炉内清掃時において発生する低温
の排ガスに、白煙防止装置8により生成された加熱空気
を供給して120℃前後に昇温し、バグフィルタ4を通
過させるので、従来のバイパス管を使用する場合のよう
に汚染排ガスを大気中に排出することがない。また、従
来のバグフィルタの一部区画に低温排ガスを通過させる
場合に生じる塩化カルシウムの潮解によるろ布の目詰ま
りや露点腐食を防止することができる。また炉内清掃時
に汚染排ガスを排出することもなく、炉内清掃専用のバ
グフィルタを設ける必要もない。
According to the above embodiment, the heated air generated by the white smoke prevention device 8 is supplied to the low-temperature exhaust gas generated when the incinerator 1 is started, when it is stopped and when the inside of the incinerator is cleaned. Since the temperature rises to about ° C. and passes through the bag filter 4, the polluted exhaust gas is not discharged into the atmosphere as in the case of using a conventional bypass pipe. Further, it is possible to prevent clogging of the filter cloth and dew point corrosion due to deliquescence of calcium chloride generated when low-temperature exhaust gas is passed through some sections of the conventional bag filter. Further, there is no need to discharge polluted exhaust gas during furnace cleaning, and it is not necessary to provide a bag filter dedicated to furnace cleaning.

【0022】[0022]

【発明の効果】以上に述べたごとく、本発明にかかるご
み焼却炉の排ガス集塵設備およびその運転方法によれ
ば、白煙防止装置により生成される高温空気を利用して
排ガスを加熱することにより、新たな設備や高コストな
特殊バグフィルタを使用しなくても、バグフィルタに導
入される排ガスを加熱して除塵することができ、塩化カ
ルシウムの潮解によるろ布の目詰まりやケーシングや配
管の露点腐食を防止できるとともに、汚染された排ガス
の大気への放出を防止することができる。
As described above, according to the exhaust gas dust collection equipment for a refuse incinerator and the method of operating the same according to the present invention, the exhaust gas is heated using the high-temperature air generated by the white smoke prevention device. By using this method, the exhaust gas introduced into the bag filter can be heated and dedusted without using new equipment or expensive special bag filters, clogging of the filter cloth due to deliquescence of calcium chloride, casing and piping. Dew point corrosion can be prevented, and the emission of polluted exhaust gas to the atmosphere can be prevented.

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

【図1】本発明に係るごみ焼却炉の排ガス集塵設備の実
施の形態を示す構成図である。
FIG. 1 is a configuration diagram showing an embodiment of an exhaust gas dust collection facility of a refuse incinerator according to the present invention.

【符号の説明】[Explanation of symbols]

1 ごみ焼却炉 2 排ガス管 3 調温塔 4 バグフィルタ 5 排気ファン 6 排気用煙突 7 温風ガス循環装置 8 白煙防止装置 18 第1排ガス温度検出器 21 送風ファン 22 空気加熱器 23 白煙防止空気供給管 24 第1加熱空気用エアダンパ 25 流量検出器 31 加熱空気供給管 32 第2加熱空気用エアダンパ 33 集塵排ガス温度制御装置 DESCRIPTION OF SYMBOLS 1 Waste incinerator 2 Exhaust gas pipe 3 Temperature control tower 4 Bag filter 5 Exhaust fan 6 Exhaust chimney 7 Hot air gas circulation device 8 White smoke prevention device 18 1st exhaust gas temperature detector 21 Blow fan 22 Air heater 23 White smoke prevention Air supply pipe 24 First air damper for heated air 25 Flow rate detector 31 Heated air supply pipe 32 Air damper for second heated air 33 Dust collection exhaust gas temperature control device

フロントページの続き (56)参考文献 特開 平3−87511(JP,A) 特開 平7−204433(JP,A) 特開 平1−262916(JP,A) 特開 平4−141214(JP,A) 特開 平4−168235(JP,A) 特開 平6−88113(JP,A) 実開 平5−28423(JP,U) 実開 平5−76515(JP,U) 実開 平6−7813(JP,U) (58)調査した分野(Int.Cl.7,DB名) B01D 46/00 - 46/54 Continuation of front page (56) References JP-A-3-87511 (JP, A) JP-A-7-204433 (JP, A) JP-A-1-262916 (JP, A) JP-A-4-141214 (JP) JP-A-4-168235 (JP, A) JP-A-6-88113 (JP, A) JP-A-5-28423 (JP, U) JP-A-5-76515 (JP, U) JP 6-7813 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) B01D 46/00-46/54

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】ごみ焼却炉の排ガス管の途中に、集塵用バ
グフィルタが介在されるとともに、白煙防止装置から白
煙防止用の高温空気を供給する白煙防止空気供給管が排
ガス管の排出部側に接続されたごみ焼却炉の排ガス集塵
設備において、基端部が前記白煙防止空気供給管に接続
されて先端部がバグフィルタ入口の排ガス管に接続され
た加熱空気供給管を設け、白煙防止空気供給管の先端側
に第1開閉手段を介装するとともに、加熱空気供給管の
先端側に第2開閉手段を介装し、ごみ焼却炉の起動時、
停止時および炉内清掃時に、バグフィルタ入口に設けら
れた排ガス温度検出手段の信号に基づいて第1開閉手段
および第2開閉手段を操作し、バグフィルタ入口の排ガ
ス中に白煙防止装置から高温空気を供給して加熱し、排
ガスの温度を制御する排ガス温度制御装置を設けたこと
を特徴とするごみ焼却炉の排ガス集塵設備。
A dust filter is interposed in the exhaust gas pipe of a refuse incinerator, and a white smoke preventing air supply pipe for supplying high temperature air for preventing white smoke from a white smoke preventing device is provided. In the exhaust gas collection equipment of a refuse incinerator connected to the discharge section side of the heating air supply pipe having a base end connected to the white smoke prevention air supply pipe and a front end connected to the exhaust gas pipe at the bag filter inlet. The first opening / closing means is interposed at the tip end of the white smoke prevention air supply pipe, and the second opening / closing means is interposed at the tip end of the heated air supply pipe.
At the time of shutdown and cleaning of the furnace, the first opening / closing means and the second opening / closing means are operated based on the signal of the exhaust gas temperature detecting means provided at the bag filter inlet, and the white smoke prevention device detects high temperature in the exhaust gas at the bag filter inlet. An exhaust gas collection system for a refuse incinerator, comprising an exhaust gas temperature control device for supplying and heating air to control the temperature of exhaust gas.
【請求項2】ごみ焼却炉の排ガス管の途中に集塵用バグ
フィルタが介在され、排ガス管の排出部側に白煙防止装
置から白煙防止用の高温空気が供給されるごみ焼却炉の
排ガス集塵設備を運転するに際し、ごみ焼却炉の起動
時、停止時および炉内清掃時に、白煙防止装置により生
成された高温空気をバグフィルタの入口の排ガス中に導
入して排ガスを加熱し、排ガス温度を適性温度に保持す
ることを特徴とするごみ焼却炉の排ガス集塵設備の運転
方法。
2. A refuse incinerator in which a dust collecting bag filter is interposed in the exhaust gas pipe of the refuse incinerator and high-temperature air for preventing white smoke is supplied from a white smoke prevention device to a discharge portion of the exhaust gas pipe. When operating the exhaust gas dust collection equipment, when starting up, shutting down, and cleaning the inside of the incinerator, high-temperature air generated by the white smoke prevention device is introduced into the exhaust gas at the bag filter inlet to heat the exhaust gas. And a method for operating an exhaust gas collection facility of a refuse incinerator, wherein the exhaust gas temperature is maintained at an appropriate temperature.
JP00530996A 1996-01-17 1996-01-17 Waste gas incinerator exhaust gas collection equipment and its operation method Expired - Fee Related JP3228867B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP00530996A JP3228867B2 (en) 1996-01-17 1996-01-17 Waste gas incinerator exhaust gas collection equipment and its operation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP00530996A JP3228867B2 (en) 1996-01-17 1996-01-17 Waste gas incinerator exhaust gas collection equipment and its operation method

Publications (2)

Publication Number Publication Date
JPH09192430A JPH09192430A (en) 1997-07-29
JP3228867B2 true JP3228867B2 (en) 2001-11-12

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ID=11607683

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Country Status (1)

Country Link
JP (1) JP3228867B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103623649A (en) * 2013-11-07 2014-03-12 南通江潮纤维制品有限公司 High-temperature resistant flame-retardant dust removal bag
CN103961955B (en) * 2014-05-14 2016-08-24 河南龙成煤高效技术应用有限公司 A kind of cleaner unit pre-heating technique for filtering flammable dusty gas
CN104906881A (en) * 2015-06-24 2015-09-16 永兴县灿阳贵金属有限责任公司 Waste gas dust removal device capable of preventing waste gas overflowing and performing safe overhauling
CN105617783A (en) * 2016-03-31 2016-06-01 广东粤威环境技术有限公司 Flue gas control method for cloth bag filtering
CN105854449A (en) * 2016-05-17 2016-08-17 江汉大学 High-temperature high-humidity flue gas bag type dust collection and ash removal method and device thereof

Also Published As

Publication number Publication date
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