JPH0313705A - Full automatic incinerating device - Google Patents
Full automatic incinerating deviceInfo
- Publication number
- JPH0313705A JPH0313705A JP1149855A JP14985589A JPH0313705A JP H0313705 A JPH0313705 A JP H0313705A JP 1149855 A JP1149855 A JP 1149855A JP 14985589 A JP14985589 A JP 14985589A JP H0313705 A JPH0313705 A JP H0313705A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- gas
- waste gas
- regulating
- change
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000000428 dust Substances 0.000 claims abstract description 5
- 239000007789 gas Substances 0.000 abstract description 20
- 230000001105 regulatory effect Effects 0.000 abstract description 6
- 238000001816 cooling Methods 0.000 abstract description 5
- 239000002912 waste gas Substances 0.000 abstract 4
- 238000002485 combustion reaction Methods 0.000 description 11
- 238000001035 drying Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000011068 loading method Methods 0.000 description 2
- 239000012716 precipitator Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 240000005979 Hordeum vulgare Species 0.000 description 1
- 235000007340 Hordeum vulgare Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- Chimneys And Flues (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、ごみの投入から焼却を経て灰の始末まで全自
動で行なう焼却炉に係り、特に炉内の温度変化に伴う焼
却室内のガスの体積変化、或いは排ガス温度の調整を自
動的に処理することを可能にした全自動焼却炉に関する
ものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to an incinerator that performs the entire process automatically, from inputting garbage to incineration to disposing of ash. The present invention relates to a fully automatic incinerator that makes it possible to automatically handle changes in the volume of gas or the adjustment of exhaust gas temperature.
[従来の技術]
従来のごみ焼却炉においては、焼却部では補助バーナー
を使用した温度制御方式はなく、また集塵部においては
、集塵器入口温度に間係なく冷却し、浮遊物、塩素等を
捕集したが、燃焼室のガス温度に伴う増減を調整した排
ガス温度をコントロールするものは存在しない。[Conventional technology] In conventional waste incinerators, there is no temperature control method using an auxiliary burner in the incineration section, and the dust collection section is constantly cooled to the dust collector inlet temperature to remove suspended matter and chlorine. However, there is no way to control the exhaust gas temperature by adjusting the fluctuations associated with the gas temperature in the combustion chamber.
[発明が解決しようとする課題]
本発明の課題は、燃焼室の温度変化に基づいて給排気量
を変化させ、効率良く完全燃焼させると同時に、集塵器
の洗浄水量も変化させて排ガス温度を一定にし、ダイオ
キシン等の有害物質を発生させないで処理可能な全自動
焼却装置を提供することにある。[Problems to be Solved by the Invention] An object of the present invention is to vary the supply and exhaust amount based on temperature changes in the combustion chamber to achieve efficient and complete combustion, and at the same time to vary the amount of washing water in the dust collector to reduce the exhaust gas temperature. It is an object of the present invention to provide a fully automatic incinerator that can maintain a constant amount of waste and produce no harmful substances such as dioxins.
[課題を解決するための手段] 本発明の手段、即ち構成は次のとおりである。[Means to solve the problem] The means or structure of the present invention is as follows.
焼却炉の室内温度センサーによって、マイコンの高速演
算による汎用モータ使用のインバーターで排風機の回転
速度を温度変化に合せて変化させガス体積を調整する手
段と集塵器に入るガス温度を一定にするシャワーリング
の水量を調整する手段とから構成される全自動焼却装置
。Using the incinerator's indoor temperature sensor, a microcomputer performs high-speed calculations and an inverter using a general-purpose motor changes the rotational speed of the exhaust fan in accordance with temperature changes, adjusting the gas volume and keeping the gas temperature that enters the precipitator constant. A fully automatic incinerator comprising means for adjusting the amount of water in the shower ring.
[実施例、発明の作動]
本発明に係る全自動焼却装置をフローシートにより概要
を説明する。[Example, Operation of the Invention] A fully automatic incinerator according to the present invention will be outlined using a flow sheet.
本発明の全自動焼却装置はごみの投入から灰バンカーの
貯溜までを一切自動で運行するものである。図中1はホ
ッパー、2はスクリーン、3はバイブレータ−14はス
クリューコンベヤーである。外部から投入されたごみは
パルベートホッパー(貯芥室)1に移し入れホッパー上
部にはスクリーン2を設け、バイブレータ−3でゆり落
とし、スクリーンをくぐり抜けたごみはバルブの役目を
するスクリューコンベヤー4によって量的に整えられる
。5は金網製ベルトコンベヤーで炉の上部にある自動投
入機6の上部室に搬入される。自動投入機6は上下二室
あり、上部が一杯になるとビームセンサー7の指令でパ
ルベートとホッパーを含めた搬送路を停止させる。下部
室のビームセンサーの信号でピストン8で下部室に下降
させ、炉内レーザー光線センサー9の指令を受け、乾燥
ゾーン1oに投入される。上部室が空になると搬送経路
に指令して再起動させ満杯にし停止させる。この繰返し
を継続する。11は摺動ロスドルで乾燥ゾーン10に投
入されたごみは摺動ロスドル11によって順次焼却ゾー
ン12に向かって送られ、揺動ロスドル13で焼却され
る。14は再燃焼室で、排ガスは再燃焼室14の焼ブロ
ック15を通過して熱交換器16付煙導16′を経てク
ーリングサイクロン17に導入される。熱交換器16は
二重にしてその外側に送風機」8で外気を送り入れ、内
側を通過する排ガスの温度で温め、熱気として一部を乾
燥空気としてストーカ−の背後から、また一部をロスド
ル下部から燃焼空気として供給する。The fully automatic incinerator of the present invention operates automatically from loading garbage to storing ash in the ash bunker. In the figure, 1 is a hopper, 2 is a screen, 3 is a vibrator, and 14 is a screw conveyor. Garbage thrown in from outside is transferred to a parbate hopper (storage chamber) 1, a screen 2 is installed above the hopper, and a vibrator 3 is used to shake it off.The garbage that has passed through the screen is transferred to a screw conveyor 4 that acts as a valve. It can be arranged quantitatively. 5 is transported by a wire mesh belt conveyor to the upper chamber of an automatic loading machine 6 located at the upper part of the furnace. The automatic feeding machine 6 has two chambers, an upper and a lower chamber, and when the upper chamber is full, the beam sensor 7 commands to stop the conveyance path including the parvate and hopper. In response to a signal from a beam sensor in the lower chamber, the piston 8 lowers it into the lower chamber, and upon receiving a command from an in-furnace laser beam sensor 9, it is introduced into the drying zone 1o. When the upper chamber is empty, it commands the conveyance path to restart, fill up, and then stop. Continue this repetition. Reference numeral 11 denotes a sliding loss dollar.The garbage put into the drying zone 10 is sequentially sent toward the incineration zone 12 by the sliding loss dollar 11, and is incinerated by the swinging loss dollar 13. 14 is a re-combustion chamber, and the exhaust gas passes through the sintering block 15 of the re-combustion chamber 14 and is introduced into the cooling cyclone 17 via a smoke guide 16' with a heat exchanger 16. The heat exchanger 16 is double-layered, and outside air is sent to the outside by a blower 8, heated by the temperature of the exhaust gas passing through the inside, and part of the hot air is used as dry air from behind the stoker, and part of it is sent to the back of the stoker. Supplied as combustion air from the bottom.
クーリングサイクロン17では、排ガスを洗浄、冷却し
浮遊物を落とし、クリーンにして排風機19で外部へ放
出するようにしである。The cooling cyclone 17 cleans and cools the exhaust gas, removes suspended matter, cleans it, and discharges it to the outside using the exhaust fan 19.
使用した水は、中和剤を混入してpH調整して排水処理
装置へ導入し、そこで沈殿槽20、濾過槽21、曝気槽
22等を経て、SS、B○D、CODなどの規制値をク
リアーして一般外部の排水路に放出する。焼却された灰
は揺動ロスドル13で自動的に灰ビット24に落とされ
、灰量ピストン24′で外部のコンベヤー25に落とさ
れ、灰バンカー26に貯留されトラックなどによる搬出
を待つ。23は補助バーナー27はスプレーノズル、2
8は燃焼室内温度センサー、29はスプレー加圧ポンプ
、30は給水タンク、31は洗浄スプレー、32はpH
調整装置、33は電気集塵器、34はシャワーリング用
温度センサーを示す。The used water is mixed with a neutralizer to adjust its pH and introduced into the wastewater treatment equipment, where it passes through a sedimentation tank 20, a filtration tank 21, an aeration tank 22, etc., and is then adjusted to regulatory values such as SS, B○D, and COD. is cleared and discharged into the general external drainage canal. The incinerated ash is automatically dropped into an ash bit 24 by a swinging loss dollar 13, dropped onto an external conveyor 25 by an ash quantity piston 24', and stored in an ash bunker 26 to wait for removal by a truck or the like. 23 is an auxiliary burner, 27 is a spray nozzle, 2
8 is a combustion chamber temperature sensor, 29 is a spray pressure pump, 30 is a water tank, 31 is a cleaning spray, 32 is a pH
33 is an electric precipitator, and 34 is a shower ring temperature sensor.
焼却室内の燃焼は時間の経過と共に温度が上昇し、最高
の焼却室の温度は800℃となる。The temperature of combustion in the incinerator increases over time, and the maximum temperature in the incinerator is 800°C.
273+20
1rr1’がa、5rriとなる。この変化は時々刻々
と温度に伴って体積も変わる。体積が変わることは立方
米麦りの酸素量も変化するので完全燃焼するためにはこ
の解決が必要となる。273+20 1rr1' becomes a, 5rr. As a result of this change, the volume also changes from moment to moment as the temperature changes. Changing the volume also changes the amount of oxygen in the cubic rice barley, so this solution is necessary for complete combustion.
a、ガス体積の調整
焼却室内の温度センサー1によってマイコンの高速演算
による汎用モーター使用のインバーターで、送風機2、
排風機3の回転速度を温度変化に合せてアンバランスが
生じない様調整する。a. Adjustment of gas volume An inverter using a general-purpose motor uses high-speed calculations from a microcomputer using a temperature sensor 1 inside the incineration chamber, and a blower 2.
The rotational speed of the exhaust fan 3 is adjusted in accordance with temperature changes so as not to cause imbalance.
b、シャワーリングの水量の調整
クーリングサイクロン4に入るガス温度を温度センサー
5で計ってシャワーリングの加圧ポンプ6の回転によっ
て水量を調整して排気ガスの温度を一定にする。この方
法はaと同様である。b. Adjustment of the amount of water in the shower ring The temperature of the gas entering the cooling cyclone 4 is measured by a temperature sensor 5, and the amount of water is adjusted by rotating the pressure pump 6 of the shower ring to keep the temperature of the exhaust gas constant. This method is similar to a.
[発明の効果コ
本発明によれば、全自動焼却装置において、炉内の温度
変化に伴う燃焼室内のガスの体積変化、排ガス温度の調
整を万全に行うことができ全自動焼却装置としての性能
は著しく向上する。[Effects of the Invention] According to the present invention, in a fully automatic incinerator, changes in the volume of gas in the combustion chamber due to temperature changes in the furnace and adjustment of exhaust gas temperature can be perfectly performed, and the performance as a fully automatic incinerator is improved. is significantly improved.
第1図は本発明に係る全自動焼却装置のフロシート、第
2図は縦断正面図である。
■・・・パルベートホッパー 6・・・自動投入機7・
・・ビームセンサー 9・・・レーザー光線センサ10
・・・乾燥ゾーン 11・・・摺動ロスドル・焼却ゾー
ン 13・・・揺動ロスドル 14 ・再燃焼室 16
・・・熱交換器 17・・・クーリングサイクロン 1
8・・送風機 19・・・排風機 25・・・反出コン
ベヤー 26・・・灰バンカー 28・・・燃焼室温度
センサーFIG. 1 is a flow sheet of a fully automatic incinerator according to the present invention, and FIG. 2 is a longitudinal sectional front view. ■...Parbate hopper 6...Automatic feeding machine 7.
... Beam sensor 9 ... Laser beam sensor 10
... Drying zone 11 ... Sliding loss dollar / Incineration zone 13 ... Swinging loss dollar 14 - Reburning chamber 16
... Heat exchanger 17 ... Cooling cyclone 1
8...Blower 19...Exhaust fan 25...Blowout conveyor 26...Ash bunker 28...Combustion chamber temperature sensor
Claims (1)
算による汎用モータ使用のインバーターで排風機の回転
速度を温度変化に合せて変化させガス体積を調整する手
段と、集塵器に入るガス温度を一定にするシャワーリン
グの水量を調整する手段とから構成される全自動焼却装
置。The indoor temperature sensor of the incinerator is used to adjust the gas volume by changing the rotation speed of the exhaust fan in accordance with temperature changes using an inverter using a general-purpose motor based on high-speed calculations by a microcomputer, and the temperature of the gas entering the dust collector is kept constant. and means for adjusting the amount of water in the shower ring.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1149855A JPH0313705A (en) | 1989-06-13 | 1989-06-13 | Full automatic incinerating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1149855A JPH0313705A (en) | 1989-06-13 | 1989-06-13 | Full automatic incinerating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0313705A true JPH0313705A (en) | 1991-01-22 |
Family
ID=15484122
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1149855A Pending JPH0313705A (en) | 1989-06-13 | 1989-06-13 | Full automatic incinerating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0313705A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06101825A (en) * | 1992-09-19 | 1994-04-12 | Japan Akuatetsuku:Kk | Incinerator |
JPH07110121A (en) * | 1993-10-14 | 1995-04-25 | Maejima Kogyosho:Kk | Incinerator having double structure |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54107167A (en) * | 1978-02-10 | 1979-08-22 | Toshiba Corp | Combustion control for incinerator |
JPS62213609A (en) * | 1986-03-13 | 1987-09-19 | Inshinaa Kogyo Kk | Full automatic massive refuse incinerator |
JPS62213608A (en) * | 1986-03-14 | 1987-09-19 | Inshinaa Kogyo Kk | Automatic dumper of large refuse incinerator |
JPS63273717A (en) * | 1987-04-30 | 1988-11-10 | Kurimoto Iron Works Ltd | Incinerating system for large-size refuse |
-
1989
- 1989-06-13 JP JP1149855A patent/JPH0313705A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54107167A (en) * | 1978-02-10 | 1979-08-22 | Toshiba Corp | Combustion control for incinerator |
JPS62213609A (en) * | 1986-03-13 | 1987-09-19 | Inshinaa Kogyo Kk | Full automatic massive refuse incinerator |
JPS62213608A (en) * | 1986-03-14 | 1987-09-19 | Inshinaa Kogyo Kk | Automatic dumper of large refuse incinerator |
JPS63273717A (en) * | 1987-04-30 | 1988-11-10 | Kurimoto Iron Works Ltd | Incinerating system for large-size refuse |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06101825A (en) * | 1992-09-19 | 1994-04-12 | Japan Akuatetsuku:Kk | Incinerator |
JPH07110121A (en) * | 1993-10-14 | 1995-04-25 | Maejima Kogyosho:Kk | Incinerator having double structure |
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