JPH09310832A - Starting control method of garbage incinerator and garbage incinerator - Google Patents

Starting control method of garbage incinerator and garbage incinerator

Info

Publication number
JPH09310832A
JPH09310832A JP12690096A JP12690096A JPH09310832A JP H09310832 A JPH09310832 A JP H09310832A JP 12690096 A JP12690096 A JP 12690096A JP 12690096 A JP12690096 A JP 12690096A JP H09310832 A JPH09310832 A JP H09310832A
Authority
JP
Japan
Prior art keywords
bag filter
furnace
dust
hopper
control means
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
JP12690096A
Other languages
Japanese (ja)
Inventor
Kazuo Nagahama
和男 長濱
Toshiyuki Hamanaka
敏之 浜中
Yoshihiro Matsuda
圭博 松田
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP12690096A priority Critical patent/JPH09310832A/en
Publication of JPH09310832A publication Critical patent/JPH09310832A/en
Pending 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste

Landscapes

  • Incineration Of Waste (AREA)
  • Chimneys And Flues (AREA)

Abstract

PROBLEM TO BE SOLVED: To keep a combustion state in an incinerator satisfactory without discharging a harmful matter preventing dew condensation from being produced on a bag filter upon starting of a garbage incinerator. SOLUTION: A hopper cover 2b is closed and is kept at the state where waste gas is prevented from flowing to a bag filter 4a. In this state, an induction air fan mechanism 5 is operated, and pressure in an incinerator is maintained within a predetermined range with incinerator internal pressure control means. Further, after inlet temperature of the bag filter 4a by a heating mechanism 8 reaches a predetermined reference temperature, operation conditions for the induction air fan mechanism 5 by the in-incinerator pressure control means are fixed and the hopper cover 2b is opened to introduce garbage into the garbage hopper 2. Further, after sealing completion of an opening 2a by the introduced garbage into the garbage hopper 2 is detected, the bag filter 4a is changed over to a bag filter ventilation state to restart the control of the incinerator internal pressure into the predetermined range by the incinerator internal pressure control means.

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、ゴミ焼却炉の立上
げ制御方法及びゴミ焼却炉に関し、詳しくは、火炉を外
部に対してシール可能なホッパ蓋体を設けるとともに、
下端部に前記火炉への開口部を設けて構成された、前記
火炉への投入ゴミを受け入れるゴミホッパと、前記火炉
を加熱する加熱機構と、前記火炉からの燃焼排ガスを流
通させて浄化するバグフィルタ通気状態と、前記燃焼排
ガスをバイパスさせるバグフィルタ休止状態とに切換可
能なバグフィルタと、前記バグフィルタの下流側から前
記燃焼排ガスを誘引する誘引送風機構と、前記誘引送風
機構を制御して前記火炉内の圧力を調節する炉内圧制御
手段を備えてあるゴミ焼却炉の立上げ制御方法及びその
立上げ制御手段を備えるゴミ焼却炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust incinerator start-up control method and a dust incinerator, and more particularly, to a hopper lid capable of sealing the furnace to the outside,
A dust hopper configured to provide an opening to the furnace at a lower end thereof, for receiving dust to be charged into the furnace, a heating mechanism for heating the furnace, and a bag filter for circulating and purifying combustion exhaust gas from the furnace. A ventilation state, a bag filter that can be switched to a bag filter resting state that bypasses the combustion exhaust gas, an induction blower mechanism that attracts the combustion exhaust gas from the downstream side of the bag filter, and the induction blower mechanism is controlled to control the blower. The present invention relates to a dust incinerator start-up control method including a furnace pressure control unit for adjusting the pressure in the furnace, and a dust incinerator including the start-up control unit.

【0002】[0002]

【従来の技術】従来のゴミ焼却炉及びその立上げ制御に
ついて、図5に示したゴミ焼却炉の一例に沿って説明す
れば、ゴミ焼却炉10には、火炉1を外部に対してシー
ル可能なホッパ蓋体2bを設けるとともに、下端部に前
記火炉1への開口部2aを設けて構成された、前記火炉
1への投入ゴミを受け入れるゴミホッパ2を備え、前記
火炉1からの燃焼排ガスを排出する煙道3に、前記火炉
1からの燃焼排ガスを処理する排ガス処理装置4と、前
記排ガス処理装置4の下流側から前記燃焼排ガスを誘引
する誘引送風機構5に誘引送風機5Aと、送風量調整用
のダンパを備えており、前記燃焼排ガスは煙突6を経て
大気中に排出される。前記火炉1には、可動式火床11
を備え、投入されたゴミを乾燥する乾燥帯A、前記乾燥
帯Aで乾燥したゴミを燃焼させる燃焼帯B、前記燃焼帯
Bで燃焼したゴミの燃焼残渣を灰化させる後燃焼帯Cに
領域分けされ、前記可動式火床11は、前記乾燥帯Aに
設けられた乾燥帯ストーカ11aと、前記燃焼帯Bに設
けられた燃焼帯ストーカ11bと、前記後燃焼帯Cに設
けられた後燃焼帯ストーカ11cとに分けて構成され、
前記乾燥帯ストーカ11aから前記燃焼帯ストーカ11
bを経て、前記後燃焼帯ストーカ11cへと投入された
ゴミが燃焼しつつ搬送され、ゴミの燃焼残渣の灰は、前
記後燃焼帯ストーカ11cの終端部から下方に投下さ
れ、灰ピットに排出される。前記火床11上でゴミが燃
焼して発生する燃焼ガスを前記火床11の上方空間で二
次燃焼させて、その熱を回収するための廃熱ボイラ13
が、前記上方空間の下流側に設けられている。前記廃熱
ボイラ13で発生した蒸気は、発電装置に送られ、蒸気
タービンを駆動して発電に供される。また、前記火炉1
を加熱する加熱機構8としてのガスバーナ8Aを設けて
あり、前記火炉1の予熱と、前記火炉1内に投入された
ゴミへの着火に供される。前記排ガス処理装置4は、前
記燃焼排ガスを流通させて浄化するバグフィルタ4a
と、前記浄化後の燃焼排ガスを洗浄する洗煙装置4bと
から構成されている。前記煙道3には、前記バグフィル
タ4aに対するバイパス路3aを備えており、前記火炉
1からの燃焼排ガスを流通させて浄化するバグフィルタ
通気状態と、前記燃焼排ガスをバイパス路3aに流通さ
せるバグフィルタ休止状態とに切換可能な排ガス路切換
機構9としての流路切換ダンパ9Aを設けてある。そし
て、火炉1に備える炉内圧検出手段24としての大気圧
と比較する微差圧計24Aからの検出結果に基づき、炉
内圧制御手段として機能する、設定火炉内圧力(−10
mmaq)を基準として前記誘引送風機5AをPID制御し
て前記火炉1内の圧力を調節する送風機構制御手段21
としてのインバータ制御器21Aを設け、炉内圧をほぼ
一定に維持するように構成してある。尚、前記可動式火
床11の下方から一次燃焼用給気或いは乾燥用空気を供
給する押込送風機構7を設けてあり、前記押込送風機構
7には、押込送風機7Aと、その押込送風機7Aからの
空気を予熱する空気予熱器と供給風量を制御し、且つ、
予熱温度を調節するダンパ機構とを備えており、前記送
風機構制御手段21は、これら押込送風機構7をも同時
に制御するように構成してある。
2. Description of the Related Art A conventional refuse incinerator and its startup control will be described with reference to an example of the refuse incinerator shown in FIG. 5, and the refuse incinerator 10 can seal the furnace 1 to the outside. A hopper lid 2b is provided and a lower end is provided with an opening 2a to the furnace 1, which is provided with a dust hopper 2 for receiving dust to be charged into the furnace 1 and discharging combustion exhaust gas from the furnace 1. An exhaust gas processing device 4 for processing combustion exhaust gas from the furnace 1, an induction blower mechanism 5 for inducing the combustion exhaust gas from a downstream side of the exhaust gas treatment device 4 to the flue 3, and an induction blower 5A and an air flow rate adjustment. The combustion exhaust gas is discharged into the atmosphere through the chimney 6. The furnace 1 includes a movable fire bed 11
And a post-combustion zone C for ashing the combustion residue of the dust burned in the combustion zone B. The movable fire bed 11 is divided into a dry zone stoker 11a provided in the dry zone A, a combustion zone stoker 11b provided in the combustion zone B, and a post combustion zone provided in the post combustion zone C. It is configured separately from the obi stoker 11c,
From the dry zone stoker 11a to the combustion zone stoker 11
Through b, the dust thrown into the post-combustion zone stoker 11c is conveyed while burning, and the ash of the combustion residue of the dust is dropped downward from the end portion of the post-combustion zone stoker 11c and discharged to the ash pit. To be done. A waste heat boiler 13 for secondary combustion of combustion gas generated by burning dust on the fire bed 11 in the space above the fire bed 11 to recover the heat.
Is provided on the downstream side of the upper space. The steam generated in the waste heat boiler 13 is sent to a power generator and drives a steam turbine to be used for power generation. Also, the furnace 1
A gas burner 8A serving as a heating mechanism 8 for heating the furnace is provided, and is used for preheating the furnace 1 and igniting dust introduced into the furnace 1. The exhaust gas treatment device 4 is a bag filter 4a for circulating and purifying the combustion exhaust gas.
And a smoke washing device 4b for washing the purified combustion exhaust gas. The flue 3 is provided with a bypass passage 3a for the bag filter 4a, and a bag filter ventilation state in which the combustion exhaust gas from the furnace 1 is circulated and purified, and a bug in which the combustion exhaust gas is circulated in the bypass passage 3a. A flow path switching damper 9A is provided as an exhaust gas path switching mechanism 9 capable of switching to a filter resting state. Then, based on the detection result from the minute differential pressure gauge 24A that compares the atmospheric pressure as the furnace internal pressure detection means 24 provided in the furnace 1, the set furnace internal pressure (−10) that functions as the furnace internal pressure control means.
mmaq) as a reference, the blower mechanism control means 21 for controlling the pressure in the furnace 1 by PID control of the induction blower 5A.
The inverter controller 21A is provided to maintain the furnace pressure substantially constant. A push air blower 7 for supplying primary combustion air or drying air from below the movable fire 11 is provided. The push air blower 7 includes a push blower 7A and the push blower 7A. Control the air preheater to preheat the air and supply air volume, and
A damper mechanism for adjusting the preheating temperature is provided, and the blower mechanism control means 21 is configured to control the forced blower mechanism 7 at the same time.

【0003】上記のゴミ焼却炉の立上げに際しては、図
6に手順をフローチャートとして一例を示すように、バ
グフィルタ入口温度を調べて、前記バグフィルタ入口温
度が基準温度(燃焼排ガスの露点を基準とした、一例と
して160℃)未満の場合には流路切換ダンパ9Aを切
換えて、排出ガスをバイパス路3aに流通させるように
し、バグフィルタ4aをバグフィルタ休止状態に保持し
て、誘引送風機5Aを運転して火炉1内の空気を誘引
し、炉内圧制御手段としての送風機制御手段21によっ
て前記誘引送風機5Aを制御して、火炉1内の圧力を大
気圧に対して負圧にし、絶対圧で約99kPa(約−1
0mmaq)に維持しつつ、前記ガスバーナ8Aに点火し、
火炉1内の予熱を開始する。その後、前記ホッパ蓋体2
bを開いて、ゴミを前記ゴミホッパ2に投入し、前記開
口部2aがゴミによってシールされた後に、前記火炉1
内圧力を絶対圧で約99kPaに静定させて、前記バグ
フィルタ4aの入口温度が160℃以上になるのを待
つ。尚、前記流路切換ダンパ9Aを、予め前記バイパス
路3a側に流路を切換えてあるのは、結露を避けるため
の対策であり、燃焼排ガスの露点が高いことに由来し
て、前記バグフィルタ4aのバグに結露を生じ、前記バ
グフィルタ4aに障害を誘起することを防止するためで
ある。火炉1内の温度が上昇するに伴って、前記バグフ
ィルタ4aの入口温度が160℃以上になると、前記流
路切換ダンパ9Aを切換えて、前記燃焼排ガスを前記バ
グフィルタ4aに通気するバグフィルタ通気状態に切換
え、前記ゴミホッパ2の下端部に備えるプッシャ2cを
駆動して、火炉1内へ前記開口部2aから前記乾燥帯ス
トーカ11aにゴミを投入し、押込送風機構7を構成す
る押込送風機7Aを運転して各ストーカ11の下方の風
箱から空気を供給し、乾燥後のゴミが前記燃焼帯ストー
カ11bに至ったところで、前記ガスバーナ8Aにより
ゴミに点火し、ゴミ焼却炉の操業を開始する。尚、前記
バグフィルタ入口温度が160℃に達しておれば、前記
流路切換ダンパ9Aを、最初からバグフィルタ通気状態
に切換えて、排出ガスをバグフィルタ4aに流通させる
ようにし、誘引送風機5Aを運転して火炉1内の圧力を
絶対圧で約99kPaに維持した後、前記ホッパ蓋体2
bを開いて、ゴミを前記ゴミホッパ2に投入し、前記開
口部2aがゴミによってシールされた後に、前記火炉1
内圧力を絶対圧で約99kPaに静定させて、前記ガス
バーナ8Aに点火し、前記プッシャ2cを駆動して、前
記乾燥帯ストーカ11aにゴミを投入し、押込送風機7
Aを運転して各ストーカ11の下方の風箱から空気を供
給し、乾燥後のゴミが前記燃焼帯ストーカ11bに至っ
たところで、前記ガスバーナ8Aによりゴミに点火し、
ゴミ焼却炉の操業を開始する。
At the time of starting up the above dust incinerator, the bag filter inlet temperature is checked as shown in the flow chart of FIG. 6 as an example, and the bag filter inlet temperature is determined to be a reference temperature (combustion exhaust gas dew point as a reference. When the temperature is lower than 160 ° C.), the flow path switching damper 9A is switched to allow the exhaust gas to flow through the bypass passage 3a, the bag filter 4a is held in the bag filter resting state, and the induction blower 5A is operated. To induce the air in the furnace 1 and control the induced blower 5A by the blower control means 21 as the furnace pressure control means to make the pressure in the furnace 1 a negative pressure with respect to the atmospheric pressure, and the absolute pressure. About 99 kPa (about -1
0 mmaq) while igniting the gas burner 8A,
Preheating in the furnace 1 is started. Then, the hopper lid 2
After opening b, dust is put into the dust hopper 2, and after the opening 2a is sealed with dust, the furnace 1
The internal pressure is allowed to settle at about 99 kPa in absolute pressure, and the temperature at the inlet of the bag filter 4a is waited to reach 160 ° C. or higher. The passage of the passage switching damper 9A is switched to the bypass passage 3a side in advance as a measure for avoiding dew condensation, and because of the high dew point of the combustion exhaust gas, the bag filter This is to prevent dew condensation on the bug 4a and inducing a trouble in the bug filter 4a. When the temperature inside the furnace 1 rises and the inlet temperature of the bag filter 4a becomes 160 ° C. or higher, the flow path switching damper 9A is switched to vent the combustion exhaust gas to the bag filter 4a. Switching to the state, the pusher 2c provided at the lower end of the dust hopper 2 is driven to throw dust into the furnace 1 from the opening 2a to the dry zone stoker 11a, and the push blower 7A constituting the push blower mechanism 7 is operated. Air is supplied from the wind box under each stoker 11 by driving, and when the dried dust reaches the combustion zone stoker 11b, the gas burner 8A ignites the dust to start the operation of the dust incinerator. If the bag filter inlet temperature reaches 160 ° C., the flow path switching damper 9A is switched to the bag filter ventilation state from the beginning so that the exhaust gas is circulated to the bag filter 4a, and the induction blower 5A is turned on. After operating to maintain the pressure in the furnace 1 at an absolute pressure of about 99 kPa, the hopper lid 2
After opening b, dust is put into the dust hopper 2, and after the opening 2a is sealed with dust, the furnace 1
The internal pressure is allowed to settle at about 99 kPa in absolute pressure, the gas burner 8A is ignited, the pusher 2c is driven, dust is thrown into the dry zone stoker 11a, and the forced draft blower 7 is used.
A is operated to supply air from a wind box below each stoker 11, and when the dried dust reaches the combustion zone stoker 11b, the gas burner 8A ignites the dust,
Commenced operation of garbage incinerator.

【0004】[0004]

【発明が解決しようとする課題】上記従来のゴミ焼却炉
及びその立上げにおいては、バグフィルタ4aの入口温
度が160℃以下の場合には、結露を避けるために、燃
焼排ガスが前記バグフィルタ4aを流通しないようにし
て、前記バイパス路3aを経て排出されるので、炉の立
上げの間は、ゴミの燃焼が開始されると、燃焼排ガスに
同伴する有害物質がそのまま排出されるという問題が生
じている。そこで、ゴミの投入に先立ち、ホッパ蓋体2
bを閉じておいて誘引送風機5Aを運転し、送風機制御
手段21によって火炉内圧を制御しながら火炉1内をガ
スバーナ8Aにより予熱し、バグフィルタ4aの入口温
度が160℃以上になるのを待って、バグフィルタ4a
をバグフィルタ通気状態にしてゴミを投入するようにす
ると、燃焼排ガスに同伴する有害物質の排出は防げるも
のの、開口部2aがゴミによってシールされない状態で
ホッパ蓋体2bを開くことになるので、火炉内圧が急激
に変動し、送風機制御手段21によって誘引送風機5A
を制御しようとしても、所謂オーバーシュートに陥り、
火炉内圧の目標範囲(上記例に於いては、絶対圧約99
kPa)への収束性が悪化してしまうという新たな問題
が生ずる。そこで、本発明のゴミ焼却炉の立上げ制御方
法及びゴミ焼却炉は、上記の問題点を解決し、ゴミ焼却
炉の立上げに際して、結露に誘起されるバグフィルタの
障害を防止出来ながら、有害物質を排出すること無く、
且つ、火炉内圧を安定制御可能な、従って、火炉内の燃
焼状態を良好に維持することが可能なゴミ焼却炉の立上
げ制御方法並びにゴミ焼却炉を提供することを目的とす
る。
In the above-mentioned conventional refuse incinerator and its start-up, when the inlet temperature of the bag filter 4a is 160 ° C. or less, the combustion exhaust gas is changed to the bag filter 4a in order to avoid dew condensation. Is discharged through the bypass passage 3a so that no harmful substances are entrained in the combustion exhaust gas when the combustion of dust is started during the startup of the furnace. Has occurred. Therefore, prior to throwing in the trash, the hopper lid 2
With b closed, the induction blower 5A is operated, the furnace internal pressure is controlled by the blower control means 21, the furnace 1 is preheated by the gas burner 8A, and the inlet temperature of the bag filter 4a waits for 160 ° C or more. , Bug filter 4a
If the bag is ventilated and dust is introduced, the discharge of harmful substances accompanying the combustion exhaust gas can be prevented, but the hopper lid 2b is opened in a state where the opening 2a is not sealed by the dust. The internal pressure suddenly fluctuates, and the blower control means 21 causes the induced blower 5A.
Even if you try to control the
Target range of furnace pressure (absolute pressure of about 99 in the above example)
A new problem arises that the convergence to kPa) deteriorates. Therefore, the refuse incinerator startup control method and the refuse incinerator of the present invention solve the above problems, and at the time of startup of the garbage incinerator, while preventing the obstacle of the bag filter induced by dew condensation, harmful Without discharging the substance,
Moreover, it is an object of the present invention to provide a startup control method for a refuse incinerator and a refuse incinerator that can stably control the internal pressure of the furnace and therefore can maintain a good combustion state in the furnace.

【0005】[0005]

【課題を解決するための手段】[Means for Solving the Problems]

〔第1特徴構成〕上記の目的のための本発明のゴミ焼却
炉の立上げ制御方法の第1特徴構成は、請求項1に記載
の如く、火炉を外部に対してシール可能なホッパ蓋体を
設けるとともに、下端部に前記火炉への開口部を設けて
構成された、前記火炉への投入ゴミを受け入れるゴミホ
ッパと、前記火炉を加熱する加熱機構と、前記火炉から
の燃焼排ガスを流通させて浄化するバグフィルタ通気状
態と、前記燃焼排ガスをバイパスさせるバグフィルタ休
止状態とに切換可能なバグフィルタと、前記バグフィル
タの下流側から前記燃焼排ガスを誘引する誘引送風機構
と、前記誘引送風機構を制御して前記火炉内の圧力を調
節する炉内圧制御手段を備えてあるゴミ焼却炉におい
て、前記ホッパ蓋体を閉じ、且つ、前記バグフィルタを
前記バグフィルタ休止状態に保持しながら前記誘引送風
機構を運転し、前記炉内圧制御手段により火炉内圧が所
定範囲内に保持され、且つ、前記加熱機構による前記バ
グフィルタ入口温度が予め定められた基準温度に達した
後に、前記炉内圧制御手段による前記誘引送風機構に対
する運転条件を固定するとともに、前記ホッパ蓋体を開
いて前記ゴミホッパにゴミを投入し、前記ゴミホッパへ
の投入ゴミによる前記開口部のシール完了を検出した後
に前記バグフィルタを前記バグフィルタ通気状態に切換
えて、前記炉内圧制御手段による火炉内圧の前記所定範
囲内への制御を再開する点にある。 〔第1特徴構成の作用効果〕上記第1特徴構成によれ
ば、バグフィルタ入口温度が予め定められた基準温度に
達する迄はホッパ蓋体を閉じ、且つ、バグフィルタをバ
グフィルタ休止状態に保持しながら誘引送風機構を運転
するので、粉塵等の有害物質を誘引することがなく、従
って、前記有害物質を大気中に放出するおそれはない。
また、何等かの原因で前記バグフィルタ入口温度が低下
した場合に於いても、前記バグフィルタが前記バグフィ
ルタ休止状態に保持されるので、バグへの結露によって
バグフィルタに障害が誘起されることを防止可能とな
る。しかも、前記バグフィルタ入口温度が前記基準温度
に達すれば、前記誘引送風機構の制御条件を炉内圧制御
手段により火炉内圧が所定範囲内に保持された条件で、
運転条件を固定するので、仮にホッパ内にゴミがなく、
前記ホッパ蓋体を開いて、火炉内を大気開放した状態に
しても、前記炉内圧制御手段の制御に対する外乱とはな
らない。さらに、前記ホッパ蓋体を開いて前記ゴミホッ
パにゴミを投入し、前記ゴミホッパへの投入ゴミによる
前記開口部のシール完了を検出した後に前記バグフィル
タを前記バグフィルタ通気状態に切換えて、火炉内圧が
静定したところで前記炉内圧制御手段による火炉内圧の
前記所定範囲内への制御を再開すれば、前記炉内圧制御
手段に於けるオーバーシュートは回避出来、バグフィル
タは、バグフィルタ通気状態に切換えてあるので、前記
開口部のシールの際に粉塵を引き込んだとしても、その
まま排出されることを防止できる。その結果、結露に誘
起されるバグフィルタの障害を防止出来ながら、有害物
質を排出すること無く、しかも、火炉内圧を安定制御可
能となり、従って、火炉内の燃焼状態を良好に維持する
ことが可能になった。 〔第2特徴構成及び作用効果〕尚、本発明のゴミ焼却炉
の立上げ制御方法の第2特徴構成は、請求項2に記載の
如く、前記第1特徴構成に記載のゴミ焼却炉の立ち上げ
に際して、前記バグフィルタ入口温度が前記基準温度以
上の場合に優先して、前記バグフィルタを前記バグフィ
ルタ通気状態に保持しながら、前記ホッパ蓋体を開いて
前記ゴミホッパにゴミを投入し、前記ゴミホッパへの投
入ゴミによる前記開口部のシールを行った後に前記誘引
送風機構を運転し、前記炉内圧制御手段により火炉内圧
が所定範囲内に保持された後に、前記加熱機構による加
熱を開始する点にある。従って、バグフィルタが通気除
塵に支障の無い状態、即ち、バグへの結露のおそれのな
い状態であれば、予熱の必要がなく、直ちにバグフィル
タ通気状態に保持するので、仮に排出気流があったとし
ても粉塵等の排出を予防出来て、ゴミホッパへのゴミの
投入を早期に実行出来る。さらに、投入ゴミによる開口
部のシールを行った後に誘引送風機構を運転するので、
誘引空気量の増加を抑制出来るので、粉塵等の燃焼排ガ
スへの同伴を防止出来、且つ、火炉内圧の変動も抑制可
能で、炉内圧制御手段に対する外乱を低減出来る。しか
も、火炉内圧が所定範囲内に保持された後に、前記加熱
機構による加熱を開始するので、火炉内での燃焼条件は
安定する。その結果、ゴミ焼却炉の立上げに際して、結
露に誘起されるバグフィルタの障害を防止出来ながら、
有害物質を排出すること無く、しかも、火炉内圧を安定
制御可能となり、従って、火炉内の燃焼状態を一層良好
に維持することが可能になり、同時に、バグフィルタの
保護と有害物質の大気中への放出の防止とを共に図りな
がら、炉の操業停止期間を短縮することが可能になっ
た。 〔第3特徴構成及び作用効果〕また、本発明のゴミ焼却
炉の立上げ制御方法の第3特徴構成は、請求項3に記載
の如く、前記第1特徴構成におけるゴミ焼却炉の立ち上
げに際して、前記バグフィルタ入口温度が前記基準温度
以上の場合に優先して、前記バグフィルタを前記バグフ
ィルタ通気状態に保持しながら前記誘引送風機構を運転
し、前記ホッパ蓋体を開いて前記ゴミホッパにゴミを投
入して前記ゴミホッパへの投入ゴミによる前記開口部の
シールを行い、前記炉内圧制御手段により火炉内圧が所
定範囲内に保持された後に、前記加熱機構による加熱を
開始する点にある。従って、バグフィルタが通気除塵に
支障のない状態、即ち、バグへの結露のおそれのない状
態であれば、予熱の必要がなく、直ちにバグフィルタ通
気状態に保持するので、直ちに誘引送風機構を運転して
も粉塵等の排出を予防出来て、ゴミホッパへのゴミの投
入を早期に実行出来る。さらに、バグフィルタ通気状態
で誘引送風機構を運転するので、ホッパ蓋体を開閉して
も、バグフィルタの通気抵抗によって誘引空気量が極端
に多くなることを避けることが出来、ゴミ投入に伴う粉
塵等の大気中への放出を防止出来、且つ、火炉内圧の急
激な変動は回避可能で、炉内圧制御手段に対する外乱を
低減出来る。しかも、火炉内圧が所定範囲内に保持され
た後に、前記加熱機構による加熱を開始するので、火炉
内での燃焼条件は安定化する。その結果、前記第2特徴
構成と同様に、ゴミ焼却炉の立上げに際して、結露に誘
起されるバグフィルタの障害を防止出来ながら、有害物
質を排出すること無く、しかも、火炉内圧を安定制御可
能となり、従って、火炉内の燃焼状態を一層良好に維持
することが可能になり、同時に、バグフィルタの保護と
有害物質の大気中への放出の防止とを共に図りながら、
炉の操業停止期間を短縮することが可能になった。
[First Characteristic Configuration] The first characteristic configuration of the method for controlling the startup of the refuse incinerator of the present invention for the above purpose is, as described in claim 1, a hopper lid capable of sealing the furnace to the outside. With the provision of an opening to the furnace at the lower end, a dust hopper that receives the dust input to the furnace, a heating mechanism that heats the furnace, and a combustion exhaust gas from the furnace is circulated. A bag filter which can be switched to a bag filter ventilation state for purifying and a bag filter resting state for bypassing the combustion exhaust gas, an induced air blowing mechanism for inducing the combustion exhaust gas from the downstream side of the bag filter, and the induced air blowing mechanism. In a refuse incinerator equipped with furnace pressure control means for controlling the pressure in the furnace by controlling, the hopper lid is closed, and the bag filter is closed. The induction blower mechanism is operated while maintaining the state, the furnace internal pressure is maintained within a predetermined range by the furnace internal pressure control means, and the bag filter inlet temperature by the heating mechanism reaches a predetermined reference temperature. After that, while fixing the operating conditions for the induction blower mechanism by the furnace pressure control means, open the hopper lid to throw dust into the dust hopper, and detect completion of sealing the opening due to dust thrown into the dust hopper. After that, the bag filter is switched to the bag filter ventilation state, and control of the furnace internal pressure by the furnace internal pressure control means within the predetermined range is restarted. [Operation and Effect of First Characteristic Configuration] According to the first characteristic configuration, the hopper lid is closed and the bag filter is kept in the bag filter resting state until the bag filter inlet temperature reaches a predetermined reference temperature. However, since the attracting and blowing mechanism is operated, harmful substances such as dust are not attracted, and therefore there is no risk of releasing the harmful substances into the atmosphere.
Further, even when the bag filter inlet temperature is lowered for some reason, the bug filter is held in the bag filter idle state, so that a defect may be induced in the bug filter by dew condensation on the bug. Can be prevented. Moreover, if the bag filter inlet temperature reaches the reference temperature, the control condition of the induction blower mechanism is that the furnace internal pressure is kept within a predetermined range by the furnace internal pressure control means,
Since the operating conditions are fixed, there is no dust in the hopper,
Even if the hopper lid is opened and the inside of the furnace is open to the atmosphere, it does not cause disturbance to the control of the furnace pressure control means. Further, the hopper lid is opened to put dust into the dust hopper, and after the completion of sealing of the opening due to dust thrown into the dust hopper is detected, the bag filter is switched to the bag filter aeration state, and the furnace pressure is increased. If the control of the furnace internal pressure by the furnace internal pressure control means within the predetermined range is restarted when it has been settled, the overshoot in the furnace internal pressure control means can be avoided, and the bag filter is switched to the bag filter ventilation state. Therefore, even if dust is drawn in at the time of sealing the opening, it can be prevented from being discharged as it is. As a result, it is possible to prevent the damage of the bag filter caused by dew condensation, to discharge the harmful substances, and to control the internal pressure of the furnace in a stable manner. Therefore, it is possible to maintain a good combustion condition in the furnace. Became. [Second Characteristic Configuration and Operation and Effect] The second characteristic configuration of the method for controlling the startup of the dust incinerator according to the present invention is, as described in claim 2, the startup of the dust incinerator according to the first characteristic configuration. When raising, the bag filter inlet temperature is prioritized when the temperature is equal to or higher than the reference temperature, while holding the bag filter in the bag filter aeration state, open the hopper lid to put dust in the dust hopper, A point at which heating by the heating mechanism is started after the induction blower mechanism is operated after the opening of the opening is sealed by dust input to the dust hopper and the furnace internal pressure is maintained within a predetermined range by the furnace internal pressure control means. It is in. Therefore, if the bag filter does not interfere with ventilation and dust removal, that is, if there is no risk of dew condensation on the bag, preheating is not necessary and the bag filter is immediately maintained in the vented state, so there was an exhaust airflow. As a result, it is possible to prevent the discharge of dust and the like, and to put the dust into the dust hopper early. Furthermore, since the induction blower mechanism is operated after the opening is sealed by the input dust,
Since the increase in the amount of induced air can be suppressed, dust and the like can be prevented from being entrained in the combustion exhaust gas, fluctuations in the furnace pressure can also be suppressed, and disturbance to the furnace pressure control means can be reduced. Moreover, since the heating by the heating mechanism is started after the internal pressure of the furnace is maintained within the predetermined range, the combustion conditions in the furnace are stabilized. As a result, when starting up the garbage incinerator, it is possible to prevent the trouble of the bag filter caused by dew condensation,
It is possible to control the pressure inside the furnace in a stable manner without discharging harmful substances, and therefore to maintain the combustion condition in the furnace better, and at the same time protect the bag filter and release harmful substances into the atmosphere. It has become possible to shorten the period during which the furnace is shut down, while at the same time preventing the release of hydrogen. [Third Characteristic Configuration and Operation and Effect] Further, the third characteristic configuration of the method for controlling the startup of the dust incinerator according to the present invention is as described in claim 3, in starting the dust incinerator in the first characteristic configuration. When the bag filter inlet temperature is equal to or higher than the reference temperature, the bag blower is operated in the induced air blowing mechanism while keeping the bag filter in a vented state, and the hopper lid is opened to collect dust in the dust hopper. Is charged to seal the opening by the dust introduced into the dust hopper, and the heating by the heating mechanism is started after the furnace internal pressure is maintained within a predetermined range by the furnace internal pressure control means. Therefore, if the bag filter does not interfere with ventilation and dust removal, that is, if there is no risk of dew condensation on the bag, preheating is not necessary and the bag filter is immediately maintained in the vented state. Even then, it is possible to prevent the discharge of dust and the like, and it is possible to quickly put the dust into the dust hopper. Furthermore, since the induction blower mechanism is operated with the bag filter ventilated, even if the hopper lid is opened and closed, it is possible to avoid an extremely large amount of induced air due to the ventilation resistance of the bag filter. And the like can be prevented from being released into the atmosphere, and rapid fluctuations in the furnace pressure can be avoided, and disturbance to the furnace pressure control means can be reduced. Moreover, since the heating by the heating mechanism is started after the pressure inside the furnace is maintained within the predetermined range, the combustion condition in the furnace is stabilized. As a result, similar to the second characteristic configuration, at the time of starting up the refuse incinerator, it is possible to prevent the bag filter from being damaged by dew condensation, but to prevent harmful substances from being discharged and to control the furnace pressure stably. Therefore, it becomes possible to maintain a better combustion state in the furnace, and at the same time, while protecting the bag filter and preventing the release of harmful substances into the atmosphere,
It became possible to shorten the shutdown period of the furnace.

【0006】〔第4特徴構成〕また、本発明のゴミ焼却
炉の第4特徴構成は、請求項4に記載の如く、ゴミホッ
パから投入されたゴミによる開口部のシール完了を検出
するゴミシール検出手段と、バグフィルタ入口温度を検
出するバグフィルタ温度検出手段とを設けるとともに、
誘引送風機構の運転に対して優先して、排ガス路切換機
構によって前記バグフィルタをバグフィルタ通気状態に
切換えて、ホッパ蓋体を開いて前記ゴミホッパにゴミを
投入し、前記ゴミシール検出手段からのシール完了検出
に基づき、前記誘引送風機構を運転して、前記送風機構
制御手段による前記誘引送風機構の制御を開始するバグ
フィルタ優先運転モードと、前記排ガス路切換機構によ
って前記バグフィルタをバグフィルタ休止状態に保持し
た状態で、前記誘引送風機構を運転し、前記バグフィル
タ温度検出手段の検出温度が予め設定された基準温度に
達した後に、前記排ガス路切換機構によって前記バグフ
ィルタを前記バグフィルタ通気状態に切換えるととも
に、前記ホッパ蓋体を開いて前記ゴミホッパにゴミを投
入し、前記シール完了検出に基づき、前記送風機構制御
手段による前記誘引送風機構の制御を開始する送風機優
先運転モードとの、二種類の立上げ運転モードを備えた
立上げ運転制御手段を設けて、前記バグフィルタ温度検
出手段の検出温度が前記基準温度未満の場合には、前記
立上げ運転モードを前記送風機優先運転モードに切換え
るようにしてある点にある。 〔第4特徴構成の作用効果〕上記第4特徴構成によれ
ば、バグフィルタ温度検出手段を設けるとともに、ゴミ
焼却炉の立上げ運転制御手段に備える立上げ運転モード
を、バグフィルタ優先運転モードと送風機優先運転モー
ドとの二種類の立上げ運転モードに切換え可能に構成し
てあるので、前記バグフィルタ温度検出手段のバグフィ
ルタ入口温度検出温度が基準温度未満の場合、即ち、燃
焼排ガスの露点未満になるおそれのある場合には、前記
立上げ運転モードを送風機優先運転モードに切換えて、
バグフィルタ休止状態に保持したまま火炉内を昇温しつ
つ火炉内からガスを誘引して、前記バグフィルタ入口温
度の上昇を待ち、前記バグフィルタ入口温度検出温度が
基準温度に達した後に、前記バグフィルタをバグフィル
タ通気状態に切換えるので、前記バグフィルタに結露の
生ずることを回避出来る。また、バグフィルタ通気状態
に切換えた後に、ホッパ蓋体を開いてゴミホッパにゴミ
を投入すれば、投入した中から飛散するゴミが外部へ放
出されることを防止出来る。さらに、投入ゴミによる開
口部のシール完了を検出した後に誘引送風機構の制御を
開始するので、炉外からの外気の吸引を抑制出来、送風
機構制御手段による火炉内圧制御を円滑化することが可
能になる。その結果、前記第1特徴構成と同様に、結露
に誘起されるバグフィルタの障害を防止出来ながら、有
害物質を排出すること無く、しかも、火炉内圧を安定制
御可能な、従って、火炉内の燃焼状態を良好に維持する
ことが可能になり、同時に、バグフィルタの保護と有害
物質の大気中への放出の防止とを共に図りながら、炉の
操業停止期間を短縮することが可能になった。 〔第5特徴構成及び作用効果〕さらに、本発明のゴミ焼
却炉の第5特徴構成は、請求項5に記載の如く、前記第
4特徴構成における運転制御手段を、ゴミ焼却炉の立上
げに際して、バグフィルタ温度検出手段の検出温度が基
準温度以上の場合には、立上げ運転モードをバグフィル
タ優先モードに切換えるように構成することによって、
ゴミホッパからのゴミの投入を直ちに開始出来るように
なる。その結果、前記第2特徴構成と同様に、ゴミ焼却
炉の立上げに際して、結露に誘起されるバグフィルタの
障害を防止出来ながら、有害物質を排出すること無く、
しかも、火炉内圧を安定制御可能になり、同時に、バグ
フィルタの保護と有害物質の大気中への放出の防止とを
共に図りながら、炉の操業停止期間を短縮することが可
能になった。 〔第6特徴構成及び作用効果〕本発明のゴミ焼却炉の第
6特徴構成は、請求項6に記載の如く、前記第4特徴構
成又は前記第5特徴構成における送風機優先運転モード
に於いて、排ガス路切換機構によってバグフィルタをバ
グフィルタ通気状態に切換えると同時に、送風機構制御
手段の制御を火炉内が正常圧力に維持されている場合に
設定される安定運転条件に固定し、ゴミシール検出手段
からのシール完了の検出に基づき、前記送風機構制御手
段による誘引送風機構の制御を開始するように運転制御
手段を構成してある点にあり、このようにすれば、バグ
フィルタをバグフィルタ通気状態に切換える際に、それ
迄に送風機構制御手段によって火炉内が正常圧力に維持
された状態の誘引送風機構の運転条件に固定して前記誘
引送風機構を運転するので、火炉内圧がホッパ蓋体の開
閉に伴って急変しても、前記送風機構制御手段による前
記誘引送風機構の制御に影響を及ぼすことを防止出来
る。そして、ゴミシール検出手段からのシール完了の検
出に基づき、前記送風機構制御手段による誘引送風機構
の制御を開始することによって、所謂オーバーシュート
は回避出来、炉内圧の目標値への収束性の悪化を防止出
来る。その結果、前記第4特徴構成又は前記第5特徴構
成における効果に加え、さらに過渡制御の安定性を向上
出来るようになった。 〔第7特徴構成及び作用効果〕本発明のゴミ焼却炉の第
7特徴構成は、請求項7に記載の如く、前記第4〜第6
特徴構成の何れかにおけるバグフィルタ優先運転モード
に於いて、ゴミシール検出手段からのシール完了の検出
に基づき、送風機構制御手段による誘引送風機構の制御
を開始するように運転制御手段を構成してある点にあ
り、このようにすれば、所謂オーバーシュートは回避出
来、炉内圧の目標値への収束性の悪化を防止出来る。
[Fourth Characteristic Configuration] The fourth characteristic configuration of the dust incinerator according to the present invention is, as described in claim 4, a dust seal detecting means for detecting completion of sealing of an opening by dust introduced from a dust hopper. And a bag filter temperature detecting means for detecting the bag filter inlet temperature,
Priority is given to the operation of the induction blower mechanism, the bag filter is switched to the bag filter ventilation state by the exhaust gas passage switching mechanism, the hopper lid is opened to throw dust into the dust hopper, and the seal from the dust seal detection means is set. A bag filter priority operation mode in which the induction blower mechanism is operated based on completion detection, and control of the induction blower mechanism by the blower mechanism control means is started, and the bag filter is in a bag filter idle state by the exhaust gas passage switching mechanism. In the state of being held at, the induced air blowing mechanism is operated, and after the detection temperature of the bag filter temperature detecting means reaches a preset reference temperature, the bag filter is switched to the bag filter ventilation state by the exhaust gas passage switching mechanism. Switch to, and open the hopper lid to put dust into the dust hopper to complete the seal. Based on the detection, a blower priority operation mode for starting control of the induction blower mechanism by the blower mechanism control means, and a startup operation control means having two types of startup operation modes are provided to detect the bag filter temperature. When the temperature detected by the means is lower than the reference temperature, the startup operation mode is switched to the blower priority operation mode. [Operation and Effect of Fourth Characteristic Configuration] According to the fourth characteristic structure, the bag filter temperature detecting means is provided, and the startup operation mode provided in the startup operation control means of the refuse incinerator is referred to as the bag filter priority operation mode. Since it is configured to be switchable to two types of start-up operation modes including the blower priority operation mode, when the bag filter inlet temperature detection temperature of the bag filter temperature detection means is lower than the reference temperature, that is, less than the dew point of the combustion exhaust gas. If there is a possibility that it will become, switch the startup operation mode to the blower priority operation mode,
While attracting gas from the furnace while raising the temperature in the furnace while keeping the bag filter inactive, waiting for the rise in the bag filter inlet temperature, after the bag filter inlet temperature detection temperature reaches the reference temperature, the Since the bag filter is switched to the bag filter ventilation state, it is possible to avoid the occurrence of dew condensation on the bag filter. If the hopper lid is opened and dust is thrown into the dust hopper after switching to the bag filter ventilation state, it is possible to prevent the dust scattered from being thrown to the outside. Furthermore, since the control of the induction blower mechanism is started after detecting the completion of the sealing of the opening due to the input dust, it is possible to suppress the suction of outside air from outside the furnace, and it is possible to facilitate the control of the furnace pressure by the blower mechanism control means. become. As a result, similar to the first characteristic configuration, it is possible to prevent the bag filter from being hindered by dew condensation, yet to discharge harmful substances, and to stably control the internal pressure of the furnace. It is possible to maintain the condition in good condition, and at the same time, it is possible to shorten the period of shutdown of the furnace while simultaneously protecting the bag filter and preventing the release of harmful substances into the atmosphere. [Fifth Characteristic Configuration and Operation and Effect] Further, according to a fifth characteristic configuration of the refuse incinerator of the present invention, as described in claim 5, the operation control means in the fourth characteristic configuration is used when starting up the dust incinerator. When the temperature detected by the bag filter temperature detecting means is equal to or higher than the reference temperature, the startup operation mode is switched to the bag filter priority mode.
Immediately start to put garbage from the garbage hopper. As a result, similar to the second characteristic configuration, at the time of starting up the refuse incinerator, it is possible to prevent the trouble of the bag filter induced by dew condensation, but without discharging harmful substances,
Moreover, the furnace pressure can be stably controlled, and at the same time, it is possible to shorten the furnace shutdown period while protecting the bag filter and preventing harmful substances from being released into the atmosphere. [Sixth Characteristic Configuration and Action and Effect] The sixth characteristic configuration of the refuse incinerator of the present invention is, as described in claim 6, in the blower priority operation mode according to the fourth characteristic configuration or the fifth characteristic configuration, At the same time that the bag filter is switched to the bag filter ventilation state by the exhaust gas passage switching mechanism, the control of the blower mechanism control means is fixed to the stable operating condition set when the inside of the furnace is maintained at normal pressure, and the dust seal detection means The operation control means is configured to start the control of the induction blower mechanism by the blower mechanism control means on the basis of the detection of the completion of the sealing of the bag filter. When switching, the induction blower mechanism is operated by fixing it to the operating conditions of the induction blower mechanism in which the inside of the furnace has been maintained at the normal pressure by the blower mechanism control means. Runode, even furnace pressure is suddenly changed in accordance with the opening and closing of the hopper lid, can be prevented from affecting the control of the induced draft mechanism by the air blowing mechanism controller. Then, based on the detection of the seal completion from the dust seal detection means, by starting the control of the induction blower mechanism by the blower mechanism control means, so-called overshoot can be avoided, the deterioration of the convergence of the furnace pressure to the target value. It can be prevented. As a result, in addition to the effects of the fourth characteristic configuration or the fifth characteristic configuration, the stability of transient control can be further improved. [Seventh Characteristic Configuration and Operation and Effect] The seventh characteristic configuration of the refuse incinerator of the present invention is the fourth to sixth aspects as described in claim 7.
In the bag filter priority operation mode in any one of the characteristic configurations, the operation control means is configured to start the control of the induced blower mechanism by the blower mechanism control means based on the detection of the seal completion from the dust seal detection means. In this way, so-called overshoot can be avoided, and deterioration of the convergence of the furnace pressure to the target value can be prevented.

【0007】[0007]

【発明の実施の形態】上記本発明の実施の形態の一例に
ついて、以下に、図面を参照しながら説明する。尚、図
面の参照を容易にするために、上記従来例を示す図面に
於ける要素と同一の要素若しくは同等の機能有する要素
には同一の符号を付した。図1は本発明のゴミ焼却炉の
一例を説明するものであり、図2には、本発明の制御方
法による基本的な制御手順の一例をフローチャートとし
て示してあり、図3には、図1に示したゴミ焼却炉の立
上げ手順の一例をフローチャートとして示した。図1に
示すように、図5に示したと同様に構成されたゴミ焼却
炉10に、ゴミシール検出手段23として、火炉1の乾
燥帯A入口側の天井壁にテレビカメラ23Aを取付け、
ゴミホッパ2の開口部2aを監視出来るようにしてあ
る。そして、前記テレビカメラ23Aからの画像を処理
して、前記開口部2aのゴミによるシール完了を検出す
るゴミシール検知手段を設けてある。また、バグフィル
タ4aにはバグフィルタ温度検出手段22として、バグ
フィルタ4a入口に設けた排ガス路切換機構9としての
流路切換ダンパ9Aの入口に吸引式ガス温度計22Aを
設けてあり、前記吸引式ガス温度計22Aによってバグ
フィルタ4a温度を検出するようにしてある。さらに、
炉内圧制御手段として機能する送風機構制御手段21と
してインバータ制御器21Aを備えており、火炉1内か
ら燃焼排ガスを誘引する誘引送風機5Aを制御するよう
に構成してあり、前記誘引送風機5Aを備えた誘引送風
機構5をも制御する運転制御手段20を備え、ゴミ焼却
炉10の運転制御並びに立上げ制御を行うようにしてあ
る。尚、前記送風機構制御手段21は、ストーカ11の
下方から火炉1内に一次燃焼用空気或いは乾燥用空気
(火炉1内で二次燃焼用空気としても機能する。)を供
給する押込送風機構7をも制御するように構成してあ
る。前記運転制御手段20には、前記ゴミシール検知手
段を含み、その検知結果と前記吸引式ガス温度計22A
の検出値とに基づき、前記流路切換ダンパ9Aを操作し
て、燃焼排ガスがバイパス路3aに流通するバグフィル
タ休止状態と、前記燃焼排ガスが前記バグフィルタ4a
に流通するバグフィルタ通気状態とに切換え可能に構成
するとともに、前記インバータ制御器21Aの設定を固
定変更可能に構成してある。この運転制御手段20に
は、バグフィルタ優先運転モードと、送風機優先運転モ
ードとを立上げ運転モードとして備え、前記吸引式ガス
温度計22Aからの検出結果が、基準温度である、燃焼
排ガスの露点に相当する160℃未満では前記送風機優
先運転モードに、前記吸引式ガス温度計22Aからの検
出結果が前記基準温度以上、即ち160℃以上であれば
前記バグフィルタ優先運転モードに、夫々自動的に切り
換えられるように構成してある。
BEST MODE FOR CARRYING OUT THE INVENTION An example of an embodiment of the present invention will be described below with reference to the drawings. In order to facilitate reference to the drawings, the same elements as those in the drawings showing the above-mentioned conventional example or elements having the same functions are designated by the same reference numerals. 1 illustrates an example of the refuse incinerator of the present invention, FIG. 2 shows an example of a basic control procedure according to the control method of the present invention as a flowchart, and FIG. An example of the procedure for starting up the refuse incinerator shown in is shown as a flowchart. As shown in FIG. 1, a television camera 23A is attached to the ceiling wall on the inlet side of the drying zone A of the furnace 1 as the dust seal detecting means 23 in the dust incinerator 10 configured similarly to that shown in FIG.
The opening 2a of the dust hopper 2 can be monitored. A dust sticker detecting means is provided for processing the image from the television camera 23A to detect the completion of sticking of dust in the opening 2a. Further, the bag filter 4a is provided with a suction type gas thermometer 22A as the bag filter temperature detecting means 22 at the inlet of the flow path switching damper 9A as the exhaust gas passage switching mechanism 9 provided at the inlet of the bag filter 4a. The temperature of the bag filter 4a is detected by the gas thermometer 22A. further,
An inverter controller 21A is provided as the blower mechanism control means 21 that functions as a furnace pressure control means, and it is configured to control an induction blower 5A that attracts combustion exhaust gas from the inside of the furnace 1, and is provided with the induction blower 5A. The operation control means 20 for controlling the induction blower mechanism 5 is also provided, and the operation control and the startup control of the refuse incinerator 10 are performed. The blower mechanism control means 21 supplies the forced combustion air or the drying air (which also functions as secondary combustion air in the furnace 1) into the furnace 1 from below the stoker 11. Is also configured to control. The operation control means 20 includes the dust seal detection means, and the detection result and the suction type gas thermometer 22A.
Based on the detected value of the above, the flow path switching damper 9A is operated to stop the bag filter in which the combustion exhaust gas flows into the bypass passage 3a, and the combustion exhaust gas flows into the bag filter 4a.
It is configured such that it can be switched to the ventilation state of a bag filter that circulates in the air conditioner, and the setting of the inverter controller 21A can be fixedly changed. The operation control means 20 is provided with a bag filter priority operation mode and a blower priority operation mode as start-up operation modes, and the detection result from the suction type gas thermometer 22A is a reference temperature. When the temperature is less than 160 ° C., which is lower than 160 ° C., the blower priority operation mode is automatically set, and when the detection result from the suction gas thermometer 22A is the reference temperature or more, that is, 160 ° C. or more, the bag filter priority operation mode is automatically set. It is configured to be switched.

【0008】上述のゴミ焼却炉の基本的な立上げ制御の
一例の基本手順を図2に示したフローチャートに沿って
説明すると、ゴミ焼却炉10の立上げに際しては、予め
ゴミホッパ2のホッパ蓋体2bを閉じておき、さらに、
流路切換ダンパ9Aを排ガスがバイパス路3aに流通す
るように切換えて、バグフィルタ4aをバグフィルタ休
止状態に保持しておいて、誘引送風機構5の誘引送風機
5Aを起動する。その後、火炉1の炉内圧力を検出する
炉内圧検出手段24としての水マノメータ式の微差圧計
24Aからの検出火炉内圧に応じて前記インバータ制御
器21Aによって前記誘引送風機5AをPID制御し
て、火炉1の内圧を設定圧力範囲内に維持する。その
後、加熱機構8であるガスバーナ8Aに点火して、前記
バグフィルタ4aの入口温度として、前記流路切換ダン
パ9Aの入口温度を計測する吸引式ガス温度計22Aか
らの検出結果によって、前記流路切換ダンパ9A入口の
温度を監視する。前記入口温度が160℃に達するのを
待って、前記誘引送風機5Aの運転制御手段20による
PID制御の制御条件を固定しておいて、前記ホッパ蓋
体2bを開き、前記ホッパ2にゴミを投入し、ゴミシー
ル検出手段23として火炉1の乾燥帯A入口側天井壁に
備える、テレビカメラ23Aからの画像から検知するゴ
ミシール検知手段からの前記ゴミホッパ2開口部2aの
ゴミによるシール完了の検知の後に、前記流路切換ダン
パ9Aを排ガスが前記バグフィルタ4aに流通するよう
に切換えて、前記バグフィルタ4aをバグフィルタ通気
状態に保持し、引き続きゴミを前記ゴミホッパ2に投入
し、前記ガスバーナ8Aによって投入したゴミに点火し
て、押込送風機構7を構成する押込送風機7Aを起動し
て、火炉内でのゴミの焼却を開始する。以上に示したよ
うなゴミ焼却炉の立上げ運転制御によって、ゴミ焼却炉
の立上げの際に、バグフィルタに於けるバグへの結露を
回避しつつ、従来のように排ガスをバグフィルタをバイ
パスしてそのまま大気中に放出させることがない。しか
も、ホッパを大気開放する際に、一旦誘引送風機の制御
条件を固定するので、前記誘引送風機の運転制御手段の
所謂オーバーシュートを回避でき、火炉の内圧を急速に
設定範囲内に収束させることが出来る。上述の制御は、
ゴミ焼却炉のシャットダウン後の立上げに際する運転制
御に限らず、ゴミ切れ後の回復運転開始、火炉内の異常
な温度低下後の回復運転開始等にも有効であり、ゴミ焼
却炉の安定運転制御手段としての制御手段に有効に活用
出来るものであり、これら回復運転開始もゴミ焼却炉の
立上げとして包含するものである。また、ゴミ焼却炉の
操業中に、何らかの事情でバグフィルタ入口温度が低下
した場合にも、上記のバグフィルタの状態変更の制御は
動作可能であり、こうした操業中にバグフィルタのバグ
への結露が発生することも予防でき、且つ、有害物質を
大気中に排出することを防止出来るので、ゴミ焼却炉の
安定制御にも有効である。
The basic procedure of an example of the basic start-up control of the dust incinerator described above will be described with reference to the flowchart shown in FIG. 2. When the dust incinerator 10 is started up, the hopper lid of the dust hopper 2 is previously set. Keep 2b closed, and then
The flow path switching damper 9A is switched so that the exhaust gas circulates in the bypass passage 3a, the bag filter 4a is held in the bag filter resting state, and the induction blower 5A of the induction blower mechanism 5 is activated. Then, PID control of the induction blower 5A by the inverter controller 21A according to the detected furnace internal pressure from the water manometer-type fine differential pressure gauge 24A as the furnace internal pressure detection means 24 for detecting the furnace internal pressure of the furnace 1, The internal pressure of the furnace 1 is maintained within the set pressure range. Then, the gas burner 8A which is the heating mechanism 8 is ignited, and the flow path is detected by the suction gas thermometer 22A that measures the inlet temperature of the flow path switching damper 9A as the inlet temperature of the bag filter 4a. The temperature at the inlet of the switching damper 9A is monitored. After waiting for the inlet temperature to reach 160 ° C., the control condition of the PID control by the operation control means 20 of the induction blower 5A is fixed, the hopper lid 2b is opened, and dust is put into the hopper 2. Then, after the completion of the seal due to the dust in the dust hopper 2 opening 2a from the dust seal detection unit that is provided on the ceiling wall of the inlet side of the furnace 1 as the dust seal detection unit 23 and that is detected from the image from the television camera 23A, The flow path switching damper 9A is switched so that the exhaust gas flows to the bag filter 4a, the bag filter 4a is maintained in a bag filter aeration state, and then the dust is thrown into the dust hopper 2 and thrown by the gas burner 8A. The dust is ignited and the forced air blower 7A constituting the forced air blow mechanism 7 is started to start the incineration of the dust in the furnace. . By controlling the startup operation of the refuse incinerator as shown above, when starting up the refuse incinerator, bypassing the exhaust gas through the bag filter while avoiding dew condensation on the bug in the bag filter And it is not released into the atmosphere as it is. Moreover, when opening the hopper to the atmosphere, the control condition of the induction blower is once fixed, so that so-called overshoot of the operation control means of the induction blower can be avoided, and the internal pressure of the furnace can be rapidly converged within the set range. I can. The above control is
It is effective not only for operation control when starting up the garbage incinerator after shutdown, but also for starting recovery operation after exhaustion of dust, starting recovery operation after abnormal temperature drop in the furnace, etc. It can be effectively utilized as the control means as the operation control means, and the start of the recovery operation is also included in the startup of the refuse incinerator. Even if the bag filter inlet temperature drops for some reason during the operation of the refuse incinerator, the above-mentioned control for changing the state of the bag filter can be operated, and the dew condensation of the bug filter on the bug occurs during such operation. It is also effective for stable control of the refuse incinerator since it can be prevented from being generated and the harmful substances can be prevented from being discharged into the atmosphere.

【0009】尚、上記回復運転開始においては、上述の
立上げ運転制御手順をさらに発展させた、図3及び図4
に示す運転制御手順が一層有効である。これは、前述の
ゴミ焼却炉に於ける運転制御手段に備える立上げ運転モ
ードの、バグフィルタ優先運転モードと、送風機優先運
転モードとを切り換えて活用するものである。即ち、ゴ
ミ焼却炉の立上げに際して、誘引送風機5Aの運転開始
に先立ち、バグフィルタ4aの入口温度を基準温度(上
記例では160℃)と比較し、その比較結果により事後
の運転制御手順を決定するのである。前記バグフィルタ
入口温度、即ち流路切換ダンパ9Aの入口温度が基準温
度以上の場合には、図3に示すように、運転制御手段2
0の立上げ運転モードをバグフィルタ優先運転モードに
切換える。このモードに於いては、先ず流路切換ダンパ
9Aを排ガス流路が前記バグフィルタ4aに連通するよ
うに切換えて、前記バグフィルタ4aをバグフィルタ通
気状態に保持し、上記と同様の手順でゴミをゴミホッパ
2に投入して、ホッパ開口部2aのゴミによるシールを
検知した後に、前記誘引送風機5Aを起動して、火炉内
圧力が所定圧力範囲内に静定するのを待つのである。そ
の後、ガスバーナ8Aに点火して、ゴミホッパ2に投入
され、火炉1の乾燥帯Aで乾燥され、燃焼帯Bに送り込
まれた燃焼帯ストーカ11a上のゴミに点火し、押込送
風機7Aを起動してゴミ焼却炉の操業を開始する。前記
バグフィルタ入口温度が基準温度未満の場合には、運転
制御手段20の立上げ運転モードを図4に示す送風機優
先運転モードに切換える。このモードに於いては、先に
説明したと同様に、前記誘引送風機5Aを起動し、火炉
1内圧力が所定圧力範囲内に静定するのを待って、前記
ガスバーナ8Aに点火し、バグフィルタ入口温度、即ち
流路切換ダンパ9Aの入口温度が基準温度に達するのを
待つ。その後、ゴミを投入し、火炉1内圧力が所定圧力
範囲内に静定するのを待って、前記ガスバーナ8Aによ
って、前記燃焼帯ストーカ11a上のゴミに点火し、前
記押込送風機7Aを起動してゴミ焼却炉の操業を開始す
る。以上のように、誘引送風機構の起動に先立ってバグ
フィルタ入口温度を検査するので、ゴミ焼却炉の以前の
状態如何に拘わらず、立上げ時の状態に応じた立上げ制
御を実施することが可能となる。
At the start of the recovery operation, the above-described startup operation control procedure is further developed, as shown in FIGS.
The operation control procedure shown in is more effective. This is to switch between the bag filter priority operation mode and the blower priority operation mode of the startup operation mode provided in the operation control means in the above-mentioned refuse incinerator. That is, when starting up the refuse incinerator, the inlet temperature of the bag filter 4a is compared with the reference temperature (160 ° C. in the above example) prior to the start of operation of the induction blower 5A, and the subsequent operation control procedure is determined based on the comparison result. To do. When the bag filter inlet temperature, that is, the inlet temperature of the flow path switching damper 9A is equal to or higher than the reference temperature, as shown in FIG.
Switch the startup operation mode of 0 to the bag filter priority operation mode. In this mode, first, the flow path switching damper 9A is switched so that the exhaust gas flow path communicates with the bag filter 4a, the bag filter 4a is kept in the bag filter aeration state, and dust is collected by the same procedure as described above. Is put into the dust hopper 2, and after the seal of dust in the hopper opening 2a is detected, the induction blower 5A is activated to wait until the pressure inside the furnace is stabilized within a predetermined pressure range. Then, the gas burner 8A is ignited, thrown into the dust hopper 2, dried in the drying zone A of the furnace 1, and ignited on the dust on the combustion zone stoker 11a sent to the combustion zone B to start the forced draft blower 7A. Commenced operation of garbage incinerator. When the bag filter inlet temperature is lower than the reference temperature, the start-up operation mode of the operation control means 20 is switched to the blower priority operation mode shown in FIG. In this mode, in the same manner as described above, the induction blower 5A is started, and after waiting for the pressure inside the furnace 1 to settle within the predetermined pressure range, the gas burner 8A is ignited and the bag filter Wait until the inlet temperature, that is, the inlet temperature of the flow path switching damper 9A reaches the reference temperature. After that, dust is thrown in, and after waiting for the pressure inside the furnace 1 to settle within a predetermined pressure range, the gas burner 8A ignites the dust on the combustion zone stoker 11a to activate the forced draft blower 7A. Commenced operation of garbage incinerator. As described above, since the bag filter inlet temperature is inspected prior to the activation of the induced draft mechanism, it is possible to perform the startup control according to the startup state regardless of the previous state of the refuse incinerator. It will be possible.

【0010】次に、本発明の他の実施の形態について説
明する。 〈1〉上記実施の形態に於いては、バグフィルタ入口温
度が基準温度以上の場合に、バグフィルタをバグフィル
タ通気状態に保持しておいて、ホッパにゴミを投入し、
ホッパ開口部のゴミによるシールが完了した後に、誘引
送風機構を起動する例を示したが、前記ゴミ投入に先立
って誘引送風機構を起動し、その後にゴミを投入するよ
うにしてもよく、殊に、既にゴミホッパ内にゴミが存在
して、前記ホッパ開口部がゴミによってシールされてい
る場合には、ホッパ蓋体2bを開いても火炉内圧に対す
る影響は殆どなく、また、バグフィルタがバグフィルタ
通気状態に保持されているので、バグの通気抵抗の寄与
によって、ゴミ投入に伴って火炉内圧が急激に上昇する
ことがないからである。 〈2〉上記実施の形態に於いては、送風機優先運転モー
ドに於いて、バグフィルタをバグフィルタ通気状態に切
換えると同時に、誘引送風機構の制御を固定する例を示
したが、上記制御は、固定することなく、制御機構の時
定数の一時的変更を行って、ゴミ投入に際する火炉内圧
の急変に対する応答を遅らせるように構成してあっても
よく、また、ホッパ蓋体の開閉情報を予め与えることに
よって、誘引制御機構の制御定数を一時的に変更するよ
うにしてあってもよい。例えば、PID制御において、
I制御定数を一時的に大きくし、且つ、D制御定数を一
時的に小さくすることも有効である。尚、上例に於い
て、I制御定数或いはD制御定数の何れか一方を変化さ
せるだけでもよい。 〈3〉上記実施の形態に於いては、排ガス路切換機構9
として、燃焼排ガスをバグフィルタに通じる経路と、バ
グフィルタに対するバイパスを通じる経路とに切換える
流路切換ダンパ9Aとして説明したが、前記排ガス路切
換機構9は、前記流路切換ダンパ9Aに限られるもので
はなく、バグフィルタのバグの通気抵抗を利用して、バ
イパス路への分岐のみを開閉するダンパ機構であっても
よい。勿論、他の流路切換機構も使用可能である。 〈4〉図1には、煙道3にバグフィルタ4aと洗煙装置
4bとで構成する排ガス処理装置4を設ける例を示し、
前記バグフィルタ4aに対するバイパス路3aを、前記
排ガス処理装置4に対するバイパスとして設けた例を示
したが、前記バイパス路3aは、前記バグフィルタ4a
のみに対するバイパスを形成するように設けてあっても
よい。 〈5〉上記実施の形態に於いては、バグフィルタ温度検
出手段としてその入口に備える排ガス路切換機構の入口
に吸引式温度計を設ける例を示したが、前記バグフィル
タ温度検出手段は、他の位置に設けた他の温度検出手段
であってもよく、前記入口近傍の煙道に設けた熱電対温
度計であってもよく、また、サーミスタ温度計であって
もよく、その設ける位置に応じて、任意の温度検出手段
を用いることが出来る。要するに、バグフィルタ入口燃
焼排ガス温度に相当するガス温度を検出出来るものであ
ればよい。 〈6〉上記実施の形態に於いては、ゴミシール検出手段
として、乾燥帯上方の天井壁に備えるテレビカメラを用
いる例を示したが、他の手段も使用可能であり、例え
ば、音波式距離計を用いて、ゴミホッパ開口部のゴミ表
面迄の距離を検出するようにしてもよく、検出距離がゴ
ミホッパ底部迄の距離であったり、引退位置にあるプッ
シャの押出面迄の距離であったりすれば、ゴミシールが
完了していないと判断できる。また、前記ゴミホッパ開
口部を横断する光路を有する光検知装置であってもよ
く、光路の遮断によってゴミシールの完了を検出するよ
うにしてあってもよい。 〈7〉上記実施の形態に於いては、炉内圧検出手段とし
て、水マノメータ式の微差圧計を用いる例を示したが、
他の形式の微差圧計を用いてもよく、また、他の微圧計
であってもよい。要するに、火炉内の圧力を絶対圧で1
00Paレベルで検出可能な火炉内の圧力検出手段であ
ればよい。尚、検出結果が運転制御手段に自動的に検知
可能なものが好ましい。
Next, another embodiment of the present invention will be described. <1> In the above embodiment, when the bag filter inlet temperature is equal to or higher than the reference temperature, the bag filter is kept in the bag filter ventilation state, and dust is put into the hopper,
Although the example of activating the induced air blowing mechanism after the sealing of the hopper opening with dust is completed, the induced air blowing mechanism may be activated prior to the introduction of the dust, and the dust may be introduced after that. When dust is already present in the dust hopper and the hopper opening is sealed with dust, opening the hopper lid 2b has almost no effect on the furnace pressure, and the bag filter is a bag filter. This is because the ventilating state is maintained, so that the contribution of the ventilation resistance of the bag does not cause a rapid increase in the furnace internal pressure due to the introduction of dust. <2> In the above embodiment, an example is shown in which, in the blower priority operation mode, the bag filter is switched to the bag filter ventilation state, and at the same time, the control of the induced blower mechanism is fixed. Instead of fixing the time constant, the time constant of the control mechanism may be temporarily changed to delay the response to a sudden change in the furnace pressure when dust is thrown in. The control constant of the attraction control mechanism may be temporarily changed by giving it in advance. For example, in PID control,
It is also effective to temporarily increase the I control constant and temporarily decrease the D control constant. In the above example, only one of the I control constant and the D control constant may be changed. <3> In the above embodiment, the exhaust gas passage switching mechanism 9
As described above, the flow path switching damper 9A that switches the path through which the combustion exhaust gas is passed to the bag filter and the path through which the bag filter is bypassed has been described, but the exhaust gas path switching mechanism 9 is limited to the flow path switching damper 9A. Instead, a damper mechanism may be used that opens and closes only the branch to the bypass path by utilizing the ventilation resistance of the bag of the bag filter. Of course, other flow path switching mechanisms can be used. <4> FIG. 1 shows an example in which an exhaust gas treatment device 4 including a bag filter 4a and a smoke washing device 4b is provided in the flue 3,
An example in which the bypass passage 3a for the bag filter 4a is provided as a bypass for the exhaust gas treatment device 4 has been shown. However, the bypass passage 3a is provided for the bag filter 4a.
It may also be provided so as to form a bypass for only. <5> In the above embodiment, an example is shown in which the suction filter thermometer is provided at the inlet of the exhaust gas passage switching mechanism provided at the inlet of the bag filter temperature detecting means. Other temperature detecting means may be provided at the position, a thermocouple thermometer provided at the flue near the inlet, or a thermistor thermometer may be provided. Any temperature detecting means can be used accordingly. In short, it is only necessary to be able to detect the gas temperature corresponding to the combustion exhaust gas temperature at the bag filter inlet. <6> In the above embodiment, an example in which the television camera provided on the ceiling wall above the dry zone is used as the dust seal detecting means, but other means can also be used, for example, a sonic distance meter. May be used to detect the distance of the dust hopper opening to the dust surface.If the detection distance is the distance to the bottom of the dust hopper or the pusher pushing surface in the retracted position, , It can be judged that the dust seal is not completed. Further, it may be a light detection device having an optical path that crosses the dust hopper opening, and the completion of the dust seal may be detected by blocking the optical path. <7> In the above embodiment, an example in which a water manometer-type fine differential pressure gauge is used as the furnace pressure detection means has been shown.
Other types of micro differential pressure gauges may be used, or other micro pressure gauges may be used. In short, the pressure inside the furnace is 1 absolute pressure
Any pressure detecting means in the furnace capable of detecting at the 00 Pa level may be used. It is preferable that the operation control means can automatically detect the detection result.

【0011】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
In the claims, reference numerals are provided for convenience of comparison with the drawings, but the present invention is not limited to the configuration shown in the attached drawings.

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

【図1】本発明に関わるゴミ焼却炉の説明図FIG. 1 is an explanatory view of a refuse incinerator according to the present invention.

【図2】本発明のゴミ焼却炉の制御方法の一例を説明す
る制御手順の流れ図
FIG. 2 is a flow chart of a control procedure for explaining an example of a control method of the refuse incinerator of the present invention.

【図3】本発明のゴミ焼却炉の制御方法の他の制御手順
の流れ図
FIG. 3 is a flowchart of another control procedure of the method for controlling the refuse incinerator of the present invention.

【図4】本発明のゴミ焼却炉の制御方法の他の制御手順
の流れ図
FIG. 4 is a flowchart of another control procedure of the method for controlling the refuse incinerator of the present invention.

【図5】従来のゴミ焼却炉の説明図FIG. 5 is an explanatory diagram of a conventional refuse incinerator.

【図6】従来のゴミ焼却炉の制御方法に関わる制御手順
の流れ図
FIG. 6 is a flowchart of a control procedure related to a conventional method for controlling a refuse incinerator.

【符号の説明】[Explanation of symbols]

1 火炉 2 ゴミホッパ 2a ゴミホッパの火炉への開口部 2b ホッパ蓋体 3 煙道 3a バイパス路 4a バグフィルタ 5 誘引送風機構 8 加熱機構 9 廃ガス路切換機構 20 運転制御手段 21 送風機構制御手段 22 バグフィルタ温度検出手段 23 ゴミシール検出手段 1 Furnace 2 Dust Hopper 2a Opening of Dust Hopper to Furnace 2b Hopper Lid 3 Flume 3a Bypass 4a Bag Filter 5 Induced Blower 8 Heating Mechanism 9 Waste Gas Route Switching 20 Operation Control 21 Blower Control 22 Bug Filter Temperature detecting means 23 Dust seal detecting means

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 F23J 15/00 ZAB F23J 15/00 ZABZ ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location F23J 15/00 ZAB F23J 15/00 ZABZ

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 火炉(1)を外部に対してシール可能な
ホッパ蓋体(2b)を設けるとともに、下端部に前記火
炉(1)への開口部(2a)を設けて構成された、前記
火炉(1)への投入ゴミを受け入れるゴミホッパ(2)
と、 前記火炉(1)を加熱する加熱機構(8)と、 前記火炉(1)からの燃焼排ガスを流通させて浄化する
バグフィルタ通気状態と、前記燃焼排ガスをバイパスさ
せるバグフィルタ休止状態とに切換可能なバグフィルタ
(4a)と、 前記バグフィルタ(4a)の下流側から前記燃焼排ガス
を誘引する誘引送風機構(5)と、 前記誘引送風機構(5)を制御して前記火炉(1)内の
圧力を調節する炉内圧制御手段を備えてあるゴミ焼却炉
において、 前記ホッパ蓋体(2b)を閉じ、且つ、前記バグフィル
タ(4a)を前記バグフィルタ休止状態に保持した状態
で、前記誘引送風機構(5)を運転し、 前記炉内圧制御手段により火炉内圧が所定範囲内に保持
され、且つ、前記加熱機構(8)による前記バグフィル
タ(4a)入口温度が予め定められた基準温度に達した
後に、前記炉内圧制御手段による前記誘引送風機構
(5)に対する運転条件を固定するとともに、前記ホッ
パ蓋体(2b)を開いて前記ゴミホッパ(2)にゴミを
投入し、 前記ゴミホッパ(2)への投入ゴミによる前記開口部
(2a)のシール完了を検出した後に前記バグフィルタ
(4a)を前記バグフィルタ通気状態に切換えて、 前記炉内圧制御手段による火炉内圧の前記所定範囲内へ
の制御を再開するゴミ焼却炉の立上げ制御方法。
1. A hopper lid (2b) capable of sealing the furnace (1) from the outside, and an opening (2a) to the furnace (1) at the lower end thereof. Garbage hopper (2) that receives the garbage thrown into the furnace (1)
A heating mechanism (8) for heating the furnace (1), a bag filter ventilation state for circulating and purifying combustion exhaust gas from the furnace (1), and a bag filter idle state for bypassing the combustion exhaust gas. A switchable bag filter (4a), an induced blower mechanism (5) for attracting the combustion exhaust gas from the downstream side of the bag filter (4a), and the induced blower mechanism (5) to control the furnace (1) In a refuse incinerator equipped with a furnace pressure control means for adjusting the internal pressure, the hopper lid (2b) is closed and the bag filter (4a) is held in the bag filter resting state, The induction blower mechanism (5) is operated, the furnace pressure is kept within a predetermined range by the furnace pressure control means, and the inlet temperature of the bag filter (4a) by the heating mechanism (8) is predetermined. After reaching the predetermined reference temperature, the operating conditions for the induction blower mechanism (5) by the furnace pressure control means are fixed, and the hopper lid (2b) is opened to put dust into the dust hopper (2). The bag filter (4a) is switched to the bag filter aeration state after detecting the completion of sealing of the opening (2a) by the dust introduced into the dust hopper (2), and the furnace pressure inside the furnace is controlled by the furnace pressure control means. A startup control method for a refuse incinerator that restarts control within a predetermined range.
【請求項2】 ゴミ焼却炉の立ち上げに際して、前記バ
グフィルタ(4a)入口温度が前記基準温度以上の場合
に優先して、前記バグフィルタ(4a)を前記バグフィ
ルタ通気状態に保持した状態で、前記ホッパ蓋体(2
b)を開いて前記ゴミホッパ(2)にゴミを投入し、 前記ゴミホッパ(2)への投入ゴミによる前記開口部
(2a)のシールを行った後に前記誘引送風機構(5)
を運転し、 前記炉内圧制御手段により火炉内圧が所定範囲内に保持
された後に、前記加熱機構(8)による加熱を開始する
請求項1記載のゴミ焼却炉の立上げ制御方法。
2. When starting up the refuse incinerator, the bag filter (4a) is kept in the bag filter aeration state prior to the case where the inlet temperature of the bag filter (4a) is equal to or higher than the reference temperature. , The hopper lid (2
b) is opened, dust is thrown into the dust hopper (2), the opening (2a) is sealed by the dust thrown into the dust hopper (2), and then the draft blower mechanism (5).
2. The start-up control method for a refuse incinerator according to claim 1, wherein after the internal pressure of the furnace is maintained within a predetermined range by the internal pressure control means, heating by the heating mechanism (8) is started.
【請求項3】 ゴミ焼却炉の立ち上げに際して、前記バ
グフィルタ(4a)入口温度が前記基準温度以上の場合
に優先して、前記バグフィルタ(4a)を前記バグフィ
ルタ通気状態に保持した状態で前記誘引送風機構(5)
を運転し、 前記ホッパ蓋体(2b)を開いて前記ゴミホッパ(2)
にゴミを投入して前記ゴミホッパ(2)への投入ゴミに
よる前記開口部(2a)のシールを行い、 前記炉内圧制御手段により火炉内圧が所定範囲内に保持
された後に、前記加熱機構(8)による加熱を開始する
請求項1記載のゴミ焼却炉の立上げ制御方法。
3. When starting up the refuse incinerator, the bag filter (4a) is kept in the bag filter aeration state prior to the case where the inlet temperature of the bag filter (4a) is equal to or higher than the reference temperature. The induction blower mechanism (5)
The waste hopper (2) by opening the hopper lid (2b).
The opening (2a) is sealed by introducing dust into the dust hopper (2) and the furnace internal pressure is kept within a predetermined range by the furnace internal pressure control means, and then the heating mechanism (8 ) The method for controlling startup of the refuse incinerator according to claim 1, wherein heating by (1) is started.
【請求項4】 下端部に火炉(1)に開口する開口部
(2a)を備えるとともに、前記火炉(1)を外気に対
してシール可能なホッパ蓋体(2b)を設けて構成され
た、前記火炉(1)への投入ゴミを受け入れるゴミホッ
パ(2)と、 前記火炉(1)からの燃焼排ガスの排出経路としての煙
道(3)に、バグフィルタ(4a)と、前記バグフィル
タ(4a)の下流側から前記燃焼排ガスを誘引する誘引
送風機構(5)とを設け、 前記火炉(1)内の圧力を所定範囲内に保つべく前記誘
引送風機構(5)を制御可能な送風機構制御手段(2
1)を備え、 前記煙道(3)には、前記バグフィルタ(4a)に対す
るバイパス路(3a)を備えるとともに、前記燃焼排ガ
スを前記バグフィルタ(4a)に流通させるバグフィル
タ通気状態と、前記燃焼排ガスを前記バイパス路(3
a)を経て排出させるバグフィルタ休止状態とに切換え
可能な排ガス路切換機構(9)を配置してあるゴミ焼却
炉であって、 前記ゴミホッパ(2)から投入されたゴミによる前記開
口部(2a)のシール完了を検出するゴミシール検出手
段(23)と、前記バグフィルタ(4a)入口温度を検
出するバグフィルタ温度検出手段(22)とを設けると
ともに、 前記誘引送風機構(5)の運転に対して優先して、前記
排ガス路切換機構(9)によって前記バグフィルタ(4
a)を前記バグフィルタ通気状態に切換えて、前記ホッ
パ蓋体(2b)を開いて前記ゴミホッパ(2)にゴミを
投入し、前記ゴミシール検出手段(23)からのシール
完了検出に基づき、前記誘引送風機構(5)を運転し
て、前記送風機構制御手段(21)による前記誘引送風
機構(5)の制御を開始するバグフィルタ優先運転モー
ドと、 前記排ガス路切換機構(9)によって前記バグフィルタ
(4a)を前記バグフィルタ休止状態に保持した状態
で、前記誘引送風機構(5)を運転し、前記バグフィル
タ温度検出手段(22)の検出温度が予め設定された基
準温度に達した後に、前記排ガス路切換機構(9)によ
って前記バグフィルタ(4a)を前記バグフィルタ通気
状態に切換えるとともに、前記ホッパ蓋体(2b)を開
いて前記ゴミホッパ(2)にゴミを投入し、前記シール
完了検出に基づき、前記送風機構制御手段(21)によ
る前記誘引送風機構(5)の制御を開始する送風機優先
運転モードとの、二種類の立上げ運転モードを備えた立
上げ運転制御手段(20)を設けて、 前記バグフィルタ温度検出手段(22)の検出温度が前
記基準温度未満の場合には、前記立上げ運転モードを前
記送風機優先運転モードに切換えるようにしてあるゴミ
焼却炉。
4. A hopper lid (2b) is provided at the lower end of the furnace (1) for opening to the furnace (1) and capable of sealing the furnace (1) against the outside air. A bag hopper (2) for receiving the dust input to the furnace (1) and a flue (3) as a discharge path of combustion exhaust gas from the furnace (1) are provided with a bag filter (4a) and the bag filter (4a). ), An induction blower mechanism (5) for inducing the combustion exhaust gas from a downstream side of the induction blower mechanism, and a blower mechanism control capable of controlling the induced blower mechanism (5) to keep the pressure in the furnace (1) within a predetermined range. Means (2
1), the flue (3) is provided with a bypass passage (3a) for the bag filter (4a), and the combustion exhaust gas is circulated through the bag filter (4a). The combustion exhaust gas is passed through the bypass passage (3
A waste incinerator in which an exhaust gas passage switching mechanism (9) capable of switching to a bag filter idle state for discharging via a) is disposed, wherein the opening (2a) is formed by the dust introduced from the dust hopper (2). ), A dust seal detecting means (23) for detecting the completion of sealing, and a bag filter temperature detecting means (22) for detecting the inlet temperature of the bag filter (4a) are provided, and for the operation of the induction blower mechanism (5). Priority is given to the bag filter (4) by the exhaust gas passage switching mechanism (9).
a) is switched to the bag filter ventilation state, the hopper lid (2b) is opened, dust is put into the dust hopper (2), and the attraction is detected based on the detection of the seal completion from the dust seal detection means (23). A bag filter priority operation mode in which the blower mechanism (5) is operated to start control of the induced blower mechanism (5) by the blower mechanism control means (21), and the bag filter is changed by the exhaust gas passage switching mechanism (9). In the state where (4a) is held in the bag filter resting state, the induction blower mechanism (5) is operated, and after the detected temperature of the bag filter temperature detecting means (22) reaches a preset reference temperature, The bag filter (4a) is switched to the bag filter aeration state by the exhaust gas passage switching mechanism (9), and the hopper lid (2b) is opened to remove the dust hopper. A duster is put into the lid (2), and based on the detection of the completion of the sealing, a blower priority operation mode in which control of the induced blower mechanism (5) by the blower mechanism control means (21) is started, and two types of standing modes are set. A startup operation control means (20) having a startup operation mode is provided, and when the temperature detected by the bag filter temperature detection means (22) is lower than the reference temperature, the startup operation mode is set to the blower priority operation. Garbage incinerator that can be switched to mode.
【請求項5】 ゴミ焼却炉の立ち上げに際して、前記バ
グフィルタ温度検出手段(22)の検出温度が前記基準
温度以上の場合には、前記立上げ運転モードを前記バグ
フィルタ優先運転モードに切換えるように前記運転制御
手段(20)を構成してある請求項4記載のゴミ焼却
炉。
5. When starting up the refuse incinerator, if the temperature detected by the bag filter temperature detecting means (22) is equal to or higher than the reference temperature, the start-up operation mode is switched to the bag filter priority operation mode. The refuse incinerator according to claim 4, wherein the operation control means (20) is provided in the.
【請求項6】 前記送風機優先運転モードに於いて、前
記排ガス路切換機構(9)によって前記バグフィルタ
(4a)を前記バグフィルタ通気状態に切換えると同時
に、前記送風機構制御手段(21)の制御を前記火炉
(1)内が正常圧力に維持されている場合に設定される
安定運転条件に固定し、前記ゴミシール検出手段(2
3)からのシール完了の検出に基づき、前記送風機構制
御手段(21)による前記誘引送風機構(5)の制御を
開始するように前記運転制御手段(20)を構成してあ
る請求項4又は5に記載のゴミ焼却炉。
6. In the blower priority operation mode, the exhaust gas passage switching mechanism (9) switches the bag filter (4a) to the bag filter ventilation state, and at the same time, controls the blower mechanism control means (21). Is fixed to a stable operating condition set when the inside of the furnace (1) is maintained at a normal pressure, and the dust seal detection means (2
The operation control means (20) is configured so as to start the control of the induced blower mechanism (5) by the blower mechanism control means (21) based on the detection of the seal completion from 3). The waste incinerator described in 5.
【請求項7】 前記バグフィルタ優先運転モードに於い
て、前記ゴミシール検出手段(23)からのシール完了
の検出に基づき、前記送風機構制御手段(21)による
前記誘引送風機構(5)の制御を開始するように前記運
転制御手段(20)を構成してある請求項4〜6の何れ
かに記載のゴミ焼却炉。
7. In the bag filter priority operation mode, the blower mechanism control means (21) controls the induced blower mechanism (5) based on the detection of the seal completion from the dust seal detector (23). The refuse incinerator according to any one of claims 4 to 6, wherein the operation control means (20) is configured to start.
JP12690096A 1996-05-22 1996-05-22 Starting control method of garbage incinerator and garbage incinerator Pending JPH09310832A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12690096A JPH09310832A (en) 1996-05-22 1996-05-22 Starting control method of garbage incinerator and garbage incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12690096A JPH09310832A (en) 1996-05-22 1996-05-22 Starting control method of garbage incinerator and garbage incinerator

Publications (1)

Publication Number Publication Date
JPH09310832A true JPH09310832A (en) 1997-12-02

Family

ID=14946670

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12690096A Pending JPH09310832A (en) 1996-05-22 1996-05-22 Starting control method of garbage incinerator and garbage incinerator

Country Status (1)

Country Link
JP (1) JPH09310832A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006207865A (en) * 2005-01-25 2006-08-10 Oyamada Engineering Kk Solid fuel combustion device
JP2008089269A (en) * 2006-10-04 2008-04-17 Taisei Denki Seisakusho:Kk Low pollution incineration controller
JP2015075325A (en) * 2014-07-10 2015-04-20 株式会社神鋼環境ソリューション Waste treatment facilities and thermal insulation method of duct collector in waste treatment facilities

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006207865A (en) * 2005-01-25 2006-08-10 Oyamada Engineering Kk Solid fuel combustion device
JP2008089269A (en) * 2006-10-04 2008-04-17 Taisei Denki Seisakusho:Kk Low pollution incineration controller
JP4586789B2 (en) * 2006-10-04 2010-11-24 株式会社 大成電機製作所 Low pollution incineration control device
JP2015075325A (en) * 2014-07-10 2015-04-20 株式会社神鋼環境ソリューション Waste treatment facilities and thermal insulation method of duct collector in waste treatment facilities

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