JP2002349820A - Waste incinerator discharging no dioxins and the like at starting and stopping time - Google Patents

Waste incinerator discharging no dioxins and the like at starting and stopping time

Info

Publication number
JP2002349820A
JP2002349820A JP2001155573A JP2001155573A JP2002349820A JP 2002349820 A JP2002349820 A JP 2002349820A JP 2001155573 A JP2001155573 A JP 2001155573A JP 2001155573 A JP2001155573 A JP 2001155573A JP 2002349820 A JP2002349820 A JP 2002349820A
Authority
JP
Japan
Prior art keywords
dioxins
starting
waste incinerator
combustion
temperature
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
JP2001155573A
Other languages
Japanese (ja)
Inventor
Seiji Ohara
清司 大原
Keiichi Hayashi
圭一 林
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP2001155573A priority Critical patent/JP2002349820A/en
Publication of JP2002349820A publication Critical patent/JP2002349820A/en
Pending legal-status Critical Current

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  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Incineration Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a waste incinerator discharging no dioxins and the like even at starting and stopping time, although starting and stopping the incinerator always cause the performance of low-temperature combustion to produce a large amount of dioxins and the like due to the fact that the waste incinerator produces a large amount of dioxins and the like at a low temperature. SOLUTION: When a waste incinerator is at a low temperature, the gas containing dioxins and the like is circulated and heated at a high temperature. Thereby, the dioxins and the like are decomposed, and the discharge of the dioxins and the like is prevented even at starting and stopping time.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は起動・停止時にもダイオ
キシン類が出ない廃棄物焼却炉に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste incinerator which does not emit dioxins even when it is started or stopped.

【0002】[0002]

【従来の技術】廃棄物焼却炉では低温のときにダイオキ
シン類を多量に発生する。焼却炉を起動・停止させれば
必ず低温燃焼を行うから焼却炉はダイオキシン類を多量
に発生する。このため、起動・停止を行う焼却炉は敬遠
され、連続運転が可能な連続炉が賞用される。しかし、
焼却炉は必ずしも連続運転が可能な廃棄物の量で運転さ
れる訳ではなく、収集される廃棄物の量が少ないと、起
動・停止を行うことが必要になる。現在の技術ではダイ
オキシン類の発生防止のため、起動・停止を行う焼却炉
は建設できない。
2. Description of the Related Art Waste incinerators generate a large amount of dioxins at low temperatures. Starting and stopping the incinerator always causes low-temperature combustion, so the incinerator generates a large amount of dioxins. Therefore, incinerators that start and stop are avoided, and continuous furnaces that can be operated continuously are awarded. But,
The incinerator is not always operated with the amount of waste that can be operated continuously. If the amount of collected waste is small, it is necessary to start and stop the incinerator. With the current technology, incinerators that start and stop cannot be built to prevent the generation of dioxins.

【0003】[0003]

【発明が解決しようとする課題】本発明は、起動・停止
時にダイオキシン類が出ないため、起動・停止を行うこ
とができる廃棄物焼却炉を提供するものである。
SUMMARY OF THE INVENTION The present invention provides a waste incinerator which can be started and stopped because no dioxins are generated at the time of starting and stopping.

【0004】[0004]

【課題を解決するための手段】もし、起動・停止時に発
生するダイオキシン類を分解することができれば、起動
・停止を行うことができる廃棄物焼却炉は製作可能であ
る。
If the dioxins generated at the time of starting and stopping can be decomposed, a waste incinerator that can be started and stopped can be manufactured.

【0005】これは、起動・停止時に発生するダイオキ
シン類を含むガスを循環させ、高温に加熱することによ
って可能になる。
[0005] This is made possible by circulating a gas containing dioxins generated at the time of starting and stopping and heating the gas to a high temperature.

【0006】[0006]

【実施例】図1は、本発明の一実施例である。1は流動
層ガス化炉、2は燃焼溶融炉、3は加熱用バーナ、4は
リジェネレータ、5は再循環用エジェクタ、6は再循環
用送風機、7は押込送風機である。流動層ガス化炉1で
は廃棄物の1部が燃焼する部分燃焼によって廃棄物のガ
ス化が行われるが、その燃焼用空気にはリジェネレータ
4で生じた予熱空気が用いられる。燃焼溶融炉2にも予
熱空気を供給し、これにより発生ガスを燃焼させる。燃
焼溶融炉2を出た燃焼ガスはリジェネレータ4で燃焼用
空気と熱交換する。燃焼溶融炉2には起動・停止時に使
用するバーナ3が設けられている。燃焼用空気は、押込
送風機7によりリジェネレータ4に供給され、高温に予
熱された後、流動層ガス化炉1および燃焼溶融炉2に供
給される。
FIG. 1 shows an embodiment of the present invention. 1 is a fluidized bed gasification furnace, 2 is a combustion melting furnace, 3 is a heating burner, 4 is a regenerator, 5 is a recirculation ejector, 6 is a recirculation blower, and 7 is a push-in blower. In the fluidized bed gasifier 1, waste is gasified by partial combustion in which a part of the waste is burned, and preheated air generated by the regenerator 4 is used as combustion air. Preheated air is also supplied to the combustion melting furnace 2 to burn the generated gas. The combustion gas exiting the combustion melting furnace 2 exchanges heat with combustion air in a regenerator 4. The combustion melting furnace 2 is provided with a burner 3 used for starting and stopping. The combustion air is supplied to the regenerator 4 by the forced air blower 7, preheated to a high temperature, and then supplied to the fluidized bed gasification furnace 1 and the combustion melting furnace 2.

【0007】起動時には、バーナ3に補助燃料を供給し
て燃焼させ、燃焼ガスをリジェネレータ4で空気と蓄熱
式に熱交換して予熱空気を造り、これを流動層ガス化炉
1に供給して加熱し高温にする。十分高温になれば廃棄
物を供給するが、この時流動層ガス化炉1の温度が下が
るのでダイオキシン類が発生する。そこで、発生ガスを
再循環用送風機6またはエジェクタ5により昇圧して流
動層ガス化炉1に循環させる。発生ガスはダストや腐食
成分を含むので、高温になると、これを可動部分の多い
再循環用送風機に通すと汚れたり、腐食したりする。ま
た、耐熱性が要求され高価になる。発生ガスが高温にな
るとき燃焼用空気を駆動媒体とするエジェクタを用いる
と可動部分がないので堅牢・安価にできる。しかし、起
動時には燃焼用空気は完全に消費されず、発生ガス中に
空気が残るのに、流動層に再循環するのにエジェクタを
用いると、駆動用媒体として新たな空気が供給されるか
ら、ダイオキシン類の分解のため多量の燃料が必要とな
る。そこで、起動時低温燃焼が生じるときには再循環用
送風機を用い、循環ガスが高温になった時、エジェクタ
に切替える。これにより、低温燃焼時には余分な空気を
導入せず、高温燃焼になった時にエジェクタを用いて再
循環用送風機を保護する。発生ガスの容積は循環空間よ
り大きいから完全に外部に排出しないようにはできない
ので、余剰の発生ガスは、燃焼溶融炉2においてバーナ
3に補助燃料を供給して燃焼させ、高温に加熱してダイ
オキシンを分解する。流動層ガス化炉1が高温になれば
発生ガスの循環を止める。
At the time of start-up, auxiliary fuel is supplied to the burner 3 and burned, and the combustion gas is heat-exchanged with air by the regenerator 4 in a regenerative manner to produce preheated air, which is supplied to the fluidized bed gasifier 1. To a high temperature. When the temperature becomes sufficiently high, waste is supplied, but at this time, dioxins are generated because the temperature of the fluidized-bed gasification furnace 1 decreases. Therefore, the generated gas is pressurized by the recirculating blower 6 or the ejector 5 and circulated through the fluidized-bed gasification furnace 1. Since the generated gas contains dust and corrosive components, when the gas is heated to a high temperature, it passes through a recirculation blower having many movable parts and becomes dirty or corroded. Moreover, heat resistance is required and it becomes expensive. If an ejector using combustion air as a driving medium is used when the generated gas is at a high temperature, there is no movable part, so that it can be made robust and inexpensive. However, when the combustion air is not completely consumed at the time of startup, and air remains in the generated gas, if an ejector is used to recirculate the fluidized bed, new air is supplied as a driving medium, A large amount of fuel is required for the decomposition of dioxins. Therefore, when low-temperature combustion occurs at startup, a recirculation blower is used, and when the circulating gas becomes high in temperature, switching to an ejector is performed. This prevents extra air from being introduced during low-temperature combustion and protects the recirculation blower using an ejector when high-temperature combustion occurs. Since the volume of the generated gas is larger than the circulation space, it cannot be prevented from being completely exhausted to the outside. Therefore, the surplus generated gas is burned by supplying auxiliary fuel to the burner 3 in the combustion melting furnace 2 and heated to a high temperature. Decomposes dioxin. When the temperature of the fluidized bed gasifier 1 becomes high, the circulation of the generated gas is stopped.

【0008】停止時には、各部が高温のまま廃棄物の供
給を止める。すると発生ガスの量および発熱量が低下す
るから、各部の温度は下がり、発生ガス中にダイオキシ
ン類が生じる。そこでバーナ3により発生ガスを加熱し
ダイオキシン類を分解する。発生ガスが生じなくなると
バーナ3の燃焼を止める。
At the time of stoppage, the supply of the waste is stopped while each part is kept at a high temperature. Then, since the amount of generated gas and the calorific value decrease, the temperature of each part decreases, and dioxins are generated in the generated gas. Then, the generated gas is heated by the burner 3 to decompose dioxins. When no generated gas is generated, the combustion of the burner 3 is stopped.

【0009】燃焼溶融炉2から排出される燃焼ガスは、
起動・停止時にもバーナ3により高温に保たれるのでダ
イオキシン類は分解され外部に排出されることはなく、
高温の燃焼ガスの持つ熱量はリジェネレータ4にて回収
されるので、補助燃料の使用量は必要最小限で済む。
The combustion gas discharged from the combustion melting furnace 2 is
The dioxins are not decomposed and discharged to the outside because they are kept at a high temperature by the burner 3 even when starting and stopping.
Since the amount of heat of the high-temperature combustion gas is recovered by the regenerator 4, the amount of auxiliary fuel used can be minimized.

【0010】[0010]

【発明の効果】本発明によれば、廃棄物焼却炉で起動・
停止時に低温のために発生するダイオキシン類は発生ガ
スを循環・加熱することにより分解され、それに要する
補助燃料は必要最小限で済む。
According to the present invention, starting up in a waste incinerator
Dioxins generated due to low temperature during shutdown are decomposed by circulating and heating the generated gas, and the auxiliary fuel required for it is minimized.

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

【図1】 本発明の一実施例である。FIG. 1 is an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1:流動層ガス化炉、2:燃焼溶融炉、3:加熱用バー
ナ、4:リジェネレータ(空気余熱器)、5:再循環用
エジェクタ、、6:再循環用送風機、7:押込送風機
1: fluidized bed gasification furnace, 2: combustion melting furnace, 3: heating burner, 4: regenerator (air preheater), 5: recirculation ejector, 6: recirculation blower, 7: push-in blower

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23G 5/14 F23C 11/02 301 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) F23G 5/14 F23C 11/02 301

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】起動・停止時に発生ガスを循環加熱するこ
とによりダイオキシン類が出ないことを特長とする廃棄
物焼却炉
1. A waste incinerator characterized in that dioxins are not produced by circulating and heating generated gas at the time of starting and stopping.
JP2001155573A 2001-05-24 2001-05-24 Waste incinerator discharging no dioxins and the like at starting and stopping time Pending JP2002349820A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001155573A JP2002349820A (en) 2001-05-24 2001-05-24 Waste incinerator discharging no dioxins and the like at starting and stopping time

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001155573A JP2002349820A (en) 2001-05-24 2001-05-24 Waste incinerator discharging no dioxins and the like at starting and stopping time

Publications (1)

Publication Number Publication Date
JP2002349820A true JP2002349820A (en) 2002-12-04

Family

ID=18999735

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001155573A Pending JP2002349820A (en) 2001-05-24 2001-05-24 Waste incinerator discharging no dioxins and the like at starting and stopping time

Country Status (1)

Country Link
JP (1) JP2002349820A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103836632A (en) * 2012-11-27 2014-06-04 浙江久而久化学有限公司 Waste adhesive incineration disposal device
CN107120664A (en) * 2017-05-04 2017-09-01 江西德运实业有限责任公司 The flue system and internal heat processing method of glue refuse destructor furnace
CN112432183A (en) * 2020-10-23 2021-03-02 清华大学 Waste incineration coupling boiler system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103836632A (en) * 2012-11-27 2014-06-04 浙江久而久化学有限公司 Waste adhesive incineration disposal device
CN107120664A (en) * 2017-05-04 2017-09-01 江西德运实业有限责任公司 The flue system and internal heat processing method of glue refuse destructor furnace
CN112432183A (en) * 2020-10-23 2021-03-02 清华大学 Waste incineration coupling boiler system

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