JPH116609A - Incinerator - Google Patents
IncineratorInfo
- Publication number
- JPH116609A JPH116609A JP17298797A JP17298797A JPH116609A JP H116609 A JPH116609 A JP H116609A JP 17298797 A JP17298797 A JP 17298797A JP 17298797 A JP17298797 A JP 17298797A JP H116609 A JPH116609 A JP H116609A
- Authority
- JP
- Japan
- Prior art keywords
- combustion chamber
- incinerator
- air
- combustion
- primary
- 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
- 238000002485 combustion reaction Methods 0.000 claims abstract description 279
- 239000002699 waste material Substances 0.000 claims abstract description 43
- 230000002093 peripheral effect Effects 0.000 claims description 13
- 238000007664 blowing Methods 0.000 claims description 11
- 238000005192 partition Methods 0.000 claims description 10
- 239000002184 metal Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 239000000779 smoke Substances 0.000 abstract description 4
- 239000004071 soot Substances 0.000 abstract description 3
- 231100001261 hazardous Toxicity 0.000 abstract 2
- 239000000356 contaminant Substances 0.000 abstract 1
- 230000007613 environmental effect Effects 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 50
- 238000013021 overheating Methods 0.000 description 12
- 239000000428 dust Substances 0.000 description 11
- 238000010586 diagram Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 6
- 239000002956 ash Substances 0.000 description 5
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000002542 deteriorative effect Effects 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000013502 plastic waste Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、廃棄物を焼却する
ために使用され、特に有害成分の外部への放出量を抑え
た焼却炉に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an incinerator used for incinerating wastes, and in particular, to reduce the amount of harmful components discharged to the outside.
【0002】[0002]
【従来の技術】従来、焼却炉における廃棄物の焼却処理
においては、木、紙、プラスチック等の可燃性の高いも
のは廃棄物自身の燃焼によって焼却され、可燃性の低い
廃棄物に関しては廃棄物自身のみの燃焼によっては焼却
が難しいため、重油、ガス等の燃焼装置を併用して焼却
が行われている。一般的には、焼却炉内に投入された廃
棄物を焼却炉側面に配設した重油(灯油、ガス)バーナ
ーによって着火あるいは継続的に焼却するという方法が
採られている。こうした焼却炉は、廃棄物を直接燃焼さ
せる一次燃焼室と、この一次燃焼室で生じた排ガスをバ
ーナーから放射した火炎で再燃焼させる二次燃焼室とで
構成されることが多く、有害成分ができるだけ焼却炉外
に出ないようにしている。また、焼却に必要な空気は、
ファンで強制的に燃焼室内に送込んだり、空気取入れ用
の孔を設けて燃焼に合わせて自然に流入するようにして
いる。2. Description of the Related Art Conventionally, in the incineration of waste in an incinerator, highly flammable materials such as wood, paper and plastic are incinerated by the combustion of the waste itself, and low inflammable waste is treated as waste. Since it is difficult to incinerate only by burning itself, incineration is performed using a combustion device for heavy oil, gas and the like. Generally, a method is adopted in which waste put into an incinerator is ignited or continuously incinerated by a heavy oil (kerosene, gas) burner disposed on the side of the incinerator. Such incinerators often consist of a primary combustion chamber that directly burns waste and a secondary combustion chamber that reburns the exhaust gas generated in this primary combustion chamber with a flame radiated from a burner, and contains harmful components. We try to stay out of the incinerator as much as possible. The air required for incineration is
The fan is forced into the combustion chamber by a fan, or a hole for taking in air is provided so that the air naturally flows in accordance with combustion.
【0003】[0003]
【発明が解決しようとする課題】従来の焼却炉は以上の
ように構成されていたことから、燃焼時の空気量制御が
難しく、空気量が不足して廃棄物が焼却炉内で完全燃焼
されないと大気中にすすや煙あるいは人体に影響を及す
ダイオキシン等の環境を汚染する有害成分を放出してし
まうという課題を有していた。Since the conventional incinerator is configured as described above, it is difficult to control the amount of air at the time of combustion, and the amount of air is insufficient, so that waste is not completely burned in the incinerator. In addition, there has been a problem that harmful components that pollute the environment, such as soot and smoke or dioxin that affects the human body, are released into the atmosphere.
【0004】特にプラスチック系廃棄物においては、燃
焼温度が比較的低温(500℃位)であるとダイオキシ
ン等の有害な副生成物が大量に発生して環境に悪影響を
与えてしまうという課題を有する。一方、これを防ぐた
めに炉内に空気を十分に供給し、且つ燃焼ガスの炉内滞
留時間を長くとるようにして燃焼温度を高温(1000
℃以上)とすると、ダイオキシン等の発生は抑えられる
ものの、炉壁や火格子等の過熱・損傷が起りやすくな
り、耐久性に劣ることとなるという課題を有した。Particularly, plastic waste has a problem that if the combustion temperature is relatively low (about 500 ° C.), a large amount of harmful by-products such as dioxin is generated, which adversely affects the environment. . On the other hand, in order to prevent this, sufficient air is supplied into the furnace, and the combustion gas is kept at a high temperature (1000
(° C. or higher), the generation of dioxin and the like can be suppressed, but there has been a problem that overheating and damage to the furnace wall, the grate, and the like are likely to occur, resulting in poor durability.
【0005】本発明は前記課題を解消するためになされ
たもので、燃焼用空気の供給を適切に行って廃棄物を完
全燃焼させることができ、外部にすすや煙あるいは環境
汚染物質を放出しないと共に、炉内が過熱せず耐久性に
優れる焼却炉を提供することを目的とする。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and can appropriately supply combustion air to completely burn waste and does not emit soot, smoke or environmental pollutants to the outside. In addition, an object of the present invention is to provide an incinerator which is excellent in durability without overheating in the furnace.
【0006】[0006]
【課題を解決するための手段】本発明に係る焼却炉は、
廃棄物を燃焼させる一次燃焼室と、当該一次燃焼室に連
通し、一次燃焼室における未燃成分を燃焼させる二次燃
焼室とを有する焼却炉において、前記一次燃焼室の内側
壁に複数の圧搾空気の吹出口が配設されるものである。
このように本発明によれば、一次燃焼室に圧搾空気の吹
出口を配設し、廃棄物の燃焼中に一次燃焼室内に圧搾空
気を吹込むことにより、圧搾空気を吹込んだ部分が局所
的に十分な空気で燃焼することとなり、吹込んだ部分に
おいてガス化した燃焼成分が高温で且つ燃焼速度が速い
状態で完全燃焼して有害な成分を発生させず、焼却炉全
体でこうした有害成分の排出量を抑えられると共に、こ
の圧搾空気の吹込みが局所的で燃焼室全体の空気量に著
しく影響を与えないことにより、廃棄物全体が高温燃焼
することはなく、燃焼室の過熱損傷が起りにくく耐久性
に優れる。The incinerator according to the present invention comprises:
In an incinerator having a primary combustion chamber that burns waste and a secondary combustion chamber that communicates with the primary combustion chamber and burns unburned components in the primary combustion chamber, a plurality of squeezes are applied to an inner wall of the primary combustion chamber. An air outlet is provided.
As described above, according to the present invention, the compressed air outlet is disposed in the primary combustion chamber, and the compressed air is blown into the primary combustion chamber during the combustion of the waste, so that the compressed air is locally blown. In the incinerator as a whole, the gasified combustion components in the blown part are completely burned at a high temperature and at a high burning rate to produce no harmful components. And the compressed air blowing does not significantly affect the air volume in the entire combustion chamber, so that the entire waste does not burn at high temperature, and the overheating damage of the combustion chamber is reduced. It does not easily occur and has excellent durability.
【0007】また、本発明に係る焼却炉は必要に応じ
て、前記複数の吹出口が、相対向する内側壁における各
々の配設位置を互違いにずらして配設されるものであ
る。このように本発明によれば、吹出口を向い合う側壁
において互違いにずらして配設し、吹出した圧搾空気が
互いに干渉しないようにすることにより、干渉で圧搾空
気が空気量十分の領域を広く形成して廃棄物の燃焼を過
度に促進させることがなく、局所的な吹込みを維持しつ
つ吹込み箇所を増やせることとなり、有害成分をより効
果的に減少させられる。Further, in the incinerator according to the present invention, the plurality of outlets are arranged so as to be shifted from each other on the opposing inner walls as necessary. As described above, according to the present invention, the air outlets are disposed so as to be staggered on the opposing side walls so that the compressed air that has been blown out does not interfere with each other. Widely formed without excessively promoting the combustion of waste, it is possible to increase the number of injection points while maintaining local injection, and it is possible to more effectively reduce harmful components.
【0008】また、本発明に係る焼却炉は必要に応じ
て、前記複数の吹出口が、内側壁上下方向へ複数段配設
されるものである。このように本発明によれば、吹出口
を上下に複数段に亘って配設し、燃焼室上部と下部で圧
搾空気の吹出状態を異ならせることができることによ
り、燃焼室下部の廃棄物と燃焼室上部に上昇した排ガス
及び未燃ガスとの燃焼状態をそれぞれ最適な状態に調整
できることとなり、完全燃焼による有害成分の低減と同
時に燃焼室の底面及び側壁の過熱防止が図れる。Further, in the incinerator according to the present invention, the plurality of outlets are arranged in a plurality of stages in the vertical direction of the inner wall as required. As described above, according to the present invention, the outlets are disposed in a plurality of stages vertically and the compressed air blowing state can be different between the upper and lower portions of the combustion chamber. The combustion state of the exhaust gas and the unburned gas that have risen to the upper part of the chamber can be adjusted to optimal states, respectively, so that harmful components due to complete combustion can be reduced and overheating of the bottom and side walls of the combustion chamber can be prevented.
【0009】また、本発明に係る焼却炉は必要に応じ
て、前記複数の吹出口が、燃焼開始時にはより下段にな
るほどより多くの空気を吹出し、定常燃焼状態にはより
上段になるほどより多くの空気を吹出すものである。こ
のように本発明によれば、圧搾空気の吹出量を燃焼開始
時には燃焼室上部側に比べ下部側をより多くし、定常燃
焼状態には逆に燃焼室上部側をより多くすることによ
り、廃棄物全体を確実に着火させた後は適度な空気を供
給して燃焼温度が高温になりすぎないようにすると共
に、排ガス中に含まれる未燃ガスや飛塵には十分な空気
を吹込んで高い燃焼温度で完全燃焼させることができ、
着火性を悪化させることなく有害成分の流出量低減と燃
焼室の過熱防止とが一連の焼却プロセスで確実に両立で
きる。Further, in the incinerator according to the present invention, if necessary, the plurality of outlets blows out more air at a lower stage at the start of combustion and more at an upper stage in a steady combustion state. It blows air. As described above, according to the present invention, the amount of compressed air to be blown out is increased at the start of combustion in the lower portion of the combustion chamber as compared with the upper portion, and in the steady combustion state, the amount of compressed air is increased in the upper portion of the combustion chamber. After the entire object is ignited, a suitable amount of air is supplied to prevent the combustion temperature from becoming too high, and sufficient air is blown into the unburned gas and dust contained in the exhaust gas. Complete combustion at the combustion temperature,
The reduction of the amount of harmful components and the prevention of overheating of the combustion chamber can be reliably achieved by a series of incineration processes without deteriorating the ignitability.
【0010】また、本発明に係る焼却炉は必要に応じ
て、多数の孔が穿設された金属穿孔体又はメッシュ状の
金属編目体からなる周側壁を有する略筒状体で形成さ
れ、当該筒状体内部を二次燃焼室に連通させ、前記一次
燃焼室内に突出して配設される副燃焼筒を備えるもので
ある。このように本発明によれば、一次燃焼室と二次燃
焼室の間に副燃焼筒を配設し、副燃焼筒の周側壁の孔に
排ガス及び未燃成分を通過させることにより、孔の通過
抵抗で排ガスの流速を低下させることとなり、二次燃焼
室内で排ガス及び未燃成分の滞留時間を長くでき、燃焼
を確実に進行させられることに加え、一次燃焼室内の熱
で赤熱した副燃焼筒への排ガス及び未燃成分の接触で未
燃成分の燃焼を促進させられることとなり、放出される
排ガス中から有害成分をより一層低減できる。Further, the incinerator according to the present invention is formed of a substantially cylindrical body having a peripheral side wall made of a metal perforated body having a large number of holes or a mesh-shaped metal stitch body, if necessary. The inside of the cylindrical body is communicated with a secondary combustion chamber, and a sub-combustion cylinder is provided to protrude into the primary combustion chamber. As described above, according to the present invention, the sub-combustion cylinder is disposed between the primary combustion chamber and the secondary combustion chamber, and the exhaust gas and the unburned components are passed through the holes on the peripheral side wall of the sub-combustion cylinder. The flow resistance of the exhaust gas is reduced by the passage resistance, so that the residence time of the exhaust gas and unburned components in the secondary combustion chamber can be extended, combustion can proceed reliably, and the sub-combustion glowed by the heat in the primary combustion chamber Combustion of the unburned components can be promoted by contact of the exhaust gas and the unburned components with the cylinder, and harmful components can be further reduced from the discharged exhaust gas.
【0011】また、本発明に係る焼却炉は必要に応じ
て、前記二次燃焼室が、略円筒状に形成されて前記一次
燃焼室上側に配設されると共に、前記二次燃焼室の略中
心に配設されて周側壁に多数の孔が形成される略筒状体
からなる補助燃焼筒と、当該補助燃焼筒の一次燃焼室寄
りの端部に連設されて二次燃焼室を横に仕切る略円板で
多数の孔を形成されてなる隔壁板と、二次燃焼室内部に
おいて補助燃焼筒の略円断面の接線方向に火炎を放射す
る二次バーナーとを備えてなるものである。このように
本発明によれば、二次燃焼室内にそれぞれ多数の孔を形
成された補助燃焼筒及び隔壁板を配設し、二次燃焼室に
入った排ガス及び未燃成分を隔壁で規制して補助燃焼筒
内に入れ、周側壁の多数の孔を経て二次燃焼室内に噴出
する排ガス及び未燃成分に二次バーナーによる火炎放射
で補助燃焼筒周りの回転運動を生じさせながら燃焼させ
ることにより、未燃成分が排ガスと共に撹拌されながら
再燃焼することとなり、未燃成分が完全に燃焼して有害
成分の外部への放出量を著しく抑えられる。In the incinerator according to the present invention, if necessary, the secondary combustion chamber is formed in a substantially cylindrical shape and disposed above the primary combustion chamber. An auxiliary combustion cylinder, which is disposed at the center and is formed of a substantially cylindrical body having a large number of holes formed in a peripheral side wall, and an auxiliary combustion cylinder, which is connected to an end of the auxiliary combustion cylinder near the primary combustion chamber, extends through the secondary combustion chamber. And a secondary burner that radiates a flame in a tangential direction of a substantially circular cross section of the auxiliary combustion cylinder in the secondary combustion chamber. . As described above, according to the present invention, the auxiliary combustion cylinder and the partition plate each having a large number of holes are disposed in the secondary combustion chamber, and the exhaust gas and the unburned components entering the secondary combustion chamber are regulated by the partition. Into the secondary combustion chamber through a large number of holes in the peripheral side wall, and burn the exhaust gas and unburned components ejected into the secondary combustion chamber while generating rotational motion around the auxiliary combustion cylinder by flame radiation from the secondary burner. As a result, the unburned components are re-burned while being agitated together with the exhaust gas, and the unburned components are completely burned and the amount of harmful components released to the outside can be significantly suppressed.
【0012】また、本発明に係る焼却炉は必要に応じ
て、周側壁に多数の孔が穿設される略円筒体に形成さ
れ、筒体内部を前記一次燃焼室上部に連通させ、前記二
次燃焼室内に配設される補助燃焼筒を備え、前記一次燃
焼室における未燃成分を補助燃焼筒の孔から二次燃焼室
内に噴出させると共に、前記一次燃焼室の廃棄物燃焼領
域において生じる熱を二次燃焼室にそのまま導入して前
記未燃成分を燃焼させるものである。このように本発明
によれば、二次燃焼室内に一次燃焼室から熱を導入し、
未燃成分を燃焼させることにより、二次燃焼室において
バーナー等の助燃手段が不要となり、コストダウンが図
れる。Further, the incinerator according to the present invention is formed, if necessary, in a substantially cylindrical body having a large number of holes formed in the peripheral side wall, and the inside of the cylindrical body communicates with the upper part of the primary combustion chamber. An auxiliary combustion cylinder disposed in the secondary combustion chamber, wherein unburned components in the primary combustion chamber are ejected from a hole of the auxiliary combustion cylinder into the secondary combustion chamber, and heat generated in a waste combustion area of the primary combustion chamber. Is introduced into the secondary combustion chamber as it is to burn the unburned components. Thus, according to the present invention, heat is introduced from the primary combustion chamber into the secondary combustion chamber,
By burning the unburned components, auxiliary combustion means such as a burner is not required in the secondary combustion chamber, and the cost can be reduced.
【0013】[0013]
(本発明の第1の実施の形態)以下、本発明の第1の実
施の形態に係る焼却炉を図1〜図8に基づいて説明す
る。本実施の形態の焼却炉は、主に木及び可燃性プラス
チックで構成される廃棄物、例えばパチンコ台等の焼却
に用いる例を示す。この図1は本実施の形態に係る焼却
炉の正面図、図2は本実施の形態に係る焼却炉の平面
図、図3は本実施の形態に係る焼却炉の側面図、図4は
本実施の形態に係る焼却炉の要部概略構成図、図5は本
実施の形態に係る焼却炉の圧搾空気吹出状態説明図、図
6は本実施の形態に係る焼却炉の二次燃焼室の概略構成
説明図、図7は本実施の形態に係る焼却炉の燃焼状態説
明図、図8は本実施の形態に係る焼却炉の一次燃焼室の
焼却プロセス説明図を示す。(First Embodiment of the Present Invention) Hereinafter, an incinerator according to a first embodiment of the present invention will be described with reference to FIGS. The incinerator according to the present embodiment is used for incineration of waste mainly composed of wood and combustible plastics, for example, pachinko machines and the like. 1 is a front view of the incinerator according to the embodiment, FIG. 2 is a plan view of the incinerator according to the embodiment, FIG. 3 is a side view of the incinerator according to the embodiment, and FIG. FIG. 5 is a schematic diagram of a main part of the incinerator according to the embodiment, FIG. 5 is an explanatory view of a compressed air blowing state of the incinerator according to the embodiment, and FIG. 6 is a view of a secondary combustion chamber of the incinerator according to the embodiment. FIG. 7 is an explanatory diagram of a schematic configuration, FIG. 7 is an explanatory diagram of a combustion state of an incinerator according to the present embodiment, and FIG. 8 is an explanatory diagram of an incineration process of a primary combustion chamber of the incinerator according to the present embodiment.
【0014】前記各図に示すように本実施の形態に係る
焼却炉1は、中空の矩形箱状に形成され、その上面に廃
棄物投入口11aが設けられた一次燃焼室11と、この
一次燃焼室11上部に配設され、一次燃焼室11と連通
する二次燃焼室12と、前記一次燃焼室11及び二次燃
焼室12の側方に配設され、二次燃焼室12に連通する
公知のサイクロン13と、このサイクロン13に連通し
て配設される中空円筒状の公知の煙突14とを備える構
成である。As shown in the figures, an incinerator 1 according to the present embodiment is formed in a hollow rectangular box shape, and has a primary combustion chamber 11 provided with a waste inlet 11a on the upper surface thereof, A secondary combustion chamber 12 disposed above the combustion chamber 11 and communicating with the primary combustion chamber 11; and a secondary combustion chamber 12 disposed on the side of the primary combustion chamber 11 and the secondary combustion chamber 12 and communicating with the secondary combustion chamber 12. The configuration includes a known cyclone 13 and a known chimney 14 in the form of a hollow cylinder disposed in communication with the cyclone 13.
【0015】前記一次燃焼室11は、中空の略矩形箱体
で形成され、廃棄物50が載置される底面には火格子1
1bが固定されて配設されると共に、各側壁及び上面の
廃棄物投入口11aを塞ぐ扉11cを鋼板製の二重構造
に形成され、これらの二重構造の中間部へ過熱焼損を防
ぐために水11dを注入されてなる構成である。廃棄物
投入口11aを塞ぐ扉11cは上方に開閉自在に配設さ
れ、別途設けられるチェーンブロック(図示を省略)で
開閉する仕組みである。また、この一次燃焼室11の長
手方向に平行な二つの側壁には、それぞれ複数の空気吹
出口11eが長手方向に所定間隔で且つ上下に複数段に
わたって配設される。これら各空気吹出口11eは、向
い合う両側壁での配設位置を互違いにずらして互いに正
面に向き合わないように配設される。そして、これら各
空気吹出口11eには複数の段ごとに送風管(図示を省
略)がそれぞれ連通して配設され、この各段の送風管が
圧搾空気の供給量を調節する制御バルブ(図示を省略)
を介して、圧搾空気を供給する空気コンプレッサ(図示
を省略)に連結されている。さらに、この一次燃焼室1
1の長手方向一端側の側壁には一次バーナー11fが火
炎放射口を水平に向けて配設される。The primary combustion chamber 11 is formed of a hollow, substantially rectangular box, and a grate 1 is provided on the bottom surface on which the waste 50 is placed.
1b is fixedly disposed, and a door 11c for closing the waste inlet 11a on each side wall and the upper surface is formed in a double structure made of a steel plate. In order to prevent overheating and burning in an intermediate portion of these double structures. This is a configuration in which water 11d is injected. A door 11c that closes the waste input port 11a is arranged to be openable and closable upward, and is configured to be opened and closed by a separately provided chain block (not shown). In addition, a plurality of air outlets 11e are provided at predetermined intervals in the longitudinal direction and vertically over a plurality of stages on two side walls parallel to the longitudinal direction of the primary combustion chamber 11. These air outlets 11e are arranged so that the arrangement positions on the opposite side walls are alternately shifted so that they do not face each other. Air blow pipes (not shown) are arranged in communication with each of the air outlets 11e for each of a plurality of stages, and the air blow pipes of each stage are provided with control valves (not shown) for adjusting the supply amount of compressed air. Omitted)
Through an air compressor (not shown) for supplying compressed air. Further, the primary combustion chamber 1
A primary burner 11f is disposed on a side wall on one end side in the longitudinal direction with the flame emission port facing horizontally.
【0016】前記二次燃焼室12は、鋼板製の二重構造
の略円筒体で形成され、一次燃焼室11の上面の一部か
ら上方に突出して配設され、下部を一次燃焼室11内に
連通させてなる構成である。前記一次燃焼室11同様、
二次燃焼室12の二重構造の中間部には水が注入され
る。二次燃焼室12内には、メッシュ状に孔を多数穿設
された円筒体で形成される補助燃焼筒12a及びこの補
助燃焼筒12aを支持する円板でメッシュ状に孔を多数
穿設されてなる隔壁板12bが配設される。さらに、二
基の二次バーナー12cが火炎放射口を水平に二次燃焼
室12内に向け、且つ放射方向を二次燃焼室12中心か
らずらして補助燃焼筒12aの接線方向とするようにし
て二次燃焼室12側壁に配設される。一方、この二次燃
焼室12の一次燃焼室11と連通する入口には、メッシ
ュ状に孔が多数穿設された周側壁を有する略筒状の副燃
焼筒15が一次燃焼室11内に突出して配設される。The secondary combustion chamber 12 is formed of a substantially cylindrical body having a double structure made of a steel plate, is disposed so as to protrude upward from a part of the upper surface of the primary combustion chamber 11, and has a lower portion in the primary combustion chamber 11. It is the structure made to communicate with. Like the primary combustion chamber 11,
Water is injected into the middle part of the secondary structure of the secondary combustion chamber 12. In the secondary combustion chamber 12, an auxiliary combustion tube 12a formed of a cylindrical body having a large number of holes formed in a mesh shape and a large number of holes formed in a mesh shape with a disk supporting the auxiliary combustion tube 12a. Is provided. Further, the two secondary burners 12c direct the flame emission port horizontally into the secondary combustion chamber 12, and the emission direction is shifted from the center of the secondary combustion chamber 12 so as to be tangential to the auxiliary combustion cylinder 12a. It is arranged on the side wall of the secondary combustion chamber 12. On the other hand, at the inlet communicating with the primary combustion chamber 11 of the secondary combustion chamber 12, a substantially cylindrical sub-combustion cylinder 15 having a peripheral side wall with a large number of holes formed in a mesh shape protrudes into the primary combustion chamber 11. Is arranged.
【0017】次に、前記構成に基づく焼却炉における焼
却動作について説明する。図8に示すように、一次燃焼
室11での焼却プロセスは、まず、廃棄物50を廃棄物
投入口11aより一次燃焼室11内に投入し(ステップ
1)、扉11cを閉鎖した後、一次バーナー11fの火
炎放射口から火炎を放射し、廃棄物50に着火する(ス
テップ2)。また、空気コンプレッサを作動させて空気
吹出口11eから一次燃焼室11内に圧搾空気を供給す
る。圧搾空気の供給に際しては、制御バルブの調整によ
り、燃焼開始時には複数段の空気吹出口11eがより下
段になるほど吹出させる空気量を多くし、廃棄物50全
体が確実に着火できるようにする(ステップ3)。Next, the incineration operation in the incinerator based on the above configuration will be described. As shown in FIG. 8, in the incineration process in the primary combustion chamber 11, first, waste 50 is put into the primary combustion chamber 11 from the waste input port 11a (step 1), the door 11c is closed, and the primary The flame is radiated from the flame radiating port of the burner 11f to ignite the waste 50 (step 2). Further, the air compressor is operated to supply compressed air into the primary combustion chamber 11 from the air outlet 11e. When the compressed air is supplied, by adjusting the control valve, the amount of air to be blown out is increased as the plurality of air outlets 11e become lower at the start of combustion so that the entire waste 50 can be ignited reliably (step). 3).
【0018】燃焼室内の炎色・炎温度、あるいは燃焼室
から排出される煙の量・成分等の変化を各種のセンサ
(図示を省略)によって検知し、このセンサからの検知
信号により制御部(図示を省略)で廃棄物50全体が火
炎を発する定常燃焼状態に移行したことを判断したら
(ステップ4)、前記と逆に空気吹出口11eがより上
段になるほど吹出させる空気量を多くし(ステップ
5)、燃焼する廃棄物50に適度な空気を供給して継続
的に燃焼させながら、燃焼により上昇してくる排ガス中
に含まれる未燃ガスや飛塵に十分な空気を吹込んで再燃
焼させ、これらの二次燃焼室12への流出量を減らす。Changes in the flame color / flame temperature in the combustion chamber, or the amount and components of smoke discharged from the combustion chamber are detected by various sensors (not shown), and a control unit ( If it is determined that the entire waste 50 has shifted to a steady combustion state in which a flame is generated (not shown) (step 4), conversely, the air amount to be blown out is increased as the air outlet 11e becomes higher (step 4). 5), while supplying appropriate air to the burning waste 50 and continuously burning it, sufficient air is blown into the unburned gas and flying dust contained in the exhaust gas rising by the combustion to reburn. Thus, the amount of these flowing out to the secondary combustion chamber 12 is reduced.
【0019】圧搾空気を複数の空気吹出口11eから局
所的に吹出すため、燃焼室内全体が一律な空気供給状態
とはならず、上層の未燃ガスや飛塵に十分な空気を吹込
んで高温で再燃焼させ、ダイオキシン等の有害な副生成
物の発生・流出を防ぐことを可能にしながら、下層では
供給空気量を抑えることができ、過剰な空気量で高燃焼
速度・高燃焼温度となるのを防いで、燃焼室の過熱によ
る損傷を確実に防止できる。なお、本実施の形態では、
制御部で燃焼開始状態から定常燃焼状態への移行を判断
して各段の空気吹出口の空気吹出量を変化させる構成と
しているが、この他、廃棄物の量、質の違いや燃焼室内
の燃焼状態に基づいて制御部から各空気吹出口の空気吹
出量の調整を行って燃焼を継続的に制御することもでき
る。Since the compressed air is locally blown out from the plurality of air outlets 11e, the entire combustion chamber does not have a uniform air supply state. In the lower layer, the amount of supplied air can be suppressed, and the excess air volume results in high combustion speed and high combustion temperature, while preventing the generation and outflow of harmful by-products such as dioxin Thus, damage due to overheating of the combustion chamber can be reliably prevented. In the present embodiment,
The control unit determines the transition from the combustion start state to the steady combustion state and changes the amount of air blown out from the air outlet at each stage. The control unit can adjust the amount of air blown out from each air blow-out port based on the combustion state to continuously control the combustion.
【0020】こうした一次燃焼室11内の燃焼により、
廃棄物50は残灰を残して排ガス(ガス化あるいは蒸気
化した未燃成分を含む)及び燃残りの飛塵となり、二次
燃焼室12に送込まれる。排ガス及び飛塵は、一次燃焼
室11から二次燃焼室12へ向う途中の副燃焼筒15の
各孔を通過することで流速を低下させ、滞留時間を十分
とって二次燃焼室12内で燃焼が確実に進行するように
なる。また、副燃焼筒15の各孔を通過する際、一次燃
焼室11内の熱で赤熱した副燃焼筒15に接触して一部
燃焼し、未燃分が減少する。Due to the combustion in the primary combustion chamber 11,
The waste 50 leaves residual ash and becomes exhaust gas (including unburned gasified or vaporized components) and unburned dust, and is sent to the secondary combustion chamber 12. The exhaust gas and flying dust decrease the flow velocity by passing through each hole of the sub-combustion cylinder 15 on the way from the primary combustion chamber 11 to the secondary combustion chamber 12, and take a sufficient residence time to cause a sufficient residence time in the secondary combustion chamber 12. Combustion proceeds reliably. Further, when passing through the holes of the sub-combustion cylinder 15, the sub-combustion cylinder 15, which is heated by the heat in the primary combustion chamber 11, is partially burned by contact with the sub-combustion cylinder 15, and the unburned portion decreases.
【0021】二次燃焼室12に入った排ガス及び飛塵
は、隔壁板12bに規制されて補助燃焼筒12a内に入
り、周壁の側部に配設された多数の孔を経て二次燃焼室
12内に噴出する。これら排ガス及び飛塵は二次燃焼室
12内における二次バーナー12cによる火炎放射を受
けて、撹拌と共に再燃焼が行われ、未燃分が完全に燃焼
する。完全燃焼により生じた排ガス及び飛灰は二次燃焼
室12から排出されてサイクロン13に送込まれ、サイ
クロン13内で排ガスと灰が分離される。灰はサイクロ
ン13の底に落下して溜り、後でまとめて排出される。
排ガスはサイクロン13の中央の筒体から出て、煙突1
4を介して外部に放出される。Exhaust gas and flying dust entering the secondary combustion chamber 12 are regulated by the partition plate 12b, enter the auxiliary combustion cylinder 12a, and pass through a large number of holes provided on the side of the peripheral wall to form the secondary combustion chamber. It spouts into 12. The exhaust gas and the flying dust receive the flame emission from the secondary burner 12c in the secondary combustion chamber 12, and are re-burned together with the stirring, so that the unburned components are completely burned. Exhaust gas and fly ash generated by complete combustion are discharged from the secondary combustion chamber 12 and sent to the cyclone 13 where the exhaust gas and ash are separated. The ash falls and accumulates on the bottom of the cyclone 13 and is collectively discharged later.
Exhaust gas exits the central cylinder of cyclone 13 and goes into chimney 1
4 to the outside.
【0022】このように、本実施の形態に係る焼却炉で
は、空気吹出口11eを一次燃焼室11の向い合う側壁
において水平方向に互違いにずらしながら上下に複数段
に亘って配設し、圧搾空気の吹出量を燃焼状態に応じて
上下方向各段でそれぞれ調整可能とすることにより、廃
棄物50全体を確実に着火させた後は適度な空気を供給
して廃棄物50自体の燃焼温度が高温になりすぎないよ
うにすると共に、排ガス中に含まれる未燃ガスや飛塵に
は上段の各空気吹出口11eから局所的に十分な空気を
吹込んで高い燃焼温度で完全燃焼させることができ、有
害成分をより効果的に減少させて後段への流出量を減ら
せる上、この圧搾空気の吹込みが局所的で一次燃焼室1
1全体の空気量に著しく影響を与えないことにより、一
次燃焼室11の火格子11b等の過熱損傷が起りにくく
耐久性に優れる。また、二次燃焼室12内に補助燃焼筒
12a及び隔壁板12bを配設すると共に一次燃焼室1
1と二次燃焼室12の間に副燃焼筒15を配設し、これ
らで排ガス及び未燃成分の流れを制御することにより、
二次燃焼室12内での排ガス及び未燃成分の滞留時間を
長くした上で、排ガス及び未燃成分が二次燃焼室12内
で撹拌されながら再燃焼することとなり、排ガス中の未
燃成分が完全に燃焼して有害成分の外部への放出量を著
しく抑えられる。As described above, in the incinerator according to the present embodiment, the air outlets 11e are disposed in a plurality of stages vertically while shifting the air outlets 11e alternately in the horizontal direction on the opposite side wall of the primary combustion chamber 11. By making it possible to adjust the amount of compressed air to be blown up and down at each stage in accordance with the combustion state, after the entire waste 50 is securely ignited, an appropriate amount of air is supplied to the combustion temperature of the waste 50 itself. Not to become too high temperature, and it is also possible to blow sufficient air locally from the upper air outlets 11e to unburned gas and dust contained in the exhaust gas to completely burn at high combustion temperature. In addition to reducing the harmful components more effectively and reducing the amount of effluent flowing to the subsequent stage, the compressed air is locally blown and the primary combustion chamber 1
By not significantly affecting the air amount of the whole 1, overheating damage to the grate 11 b of the primary combustion chamber 11 and the like hardly occur, and the durability is excellent. In addition, an auxiliary combustion cylinder 12a and a partition plate 12b are provided in the secondary combustion chamber 12 and the primary combustion chamber 1
By arranging the sub-combustion cylinder 15 between the primary combustion chamber 12 and the secondary combustion chamber 12 and controlling the flow of the exhaust gas and the unburned components with these,
After prolonging the residence time of the exhaust gas and unburned components in the secondary combustion chamber 12, the exhaust gas and unburned components re-combust while being stirred in the secondary combustion chamber 12, and the unburned components in the exhaust gas Completely burns, and the amount of harmful components released to the outside can be significantly suppressed.
【0023】(本発明の第2の実施の形態)本発明の第
2の実施の形態に係る焼却炉を図9に基づいて説明す
る。この図9は本実施の形態に係る焼却炉の要部概略構
成図を示す。前記図9に示すように本実施の形態に係る
焼却炉2は、前記第1の実施形態と同様に、一次燃焼室
21と、二次燃焼室22と、サイクロン及び煙突(図示
を省略)とを備え、異なる点として一次燃焼室21と二
次燃焼室22が近接し、一次燃焼室21内の熱が二次燃
焼室22にそのまま達するようにして二次バーナーを省
いた構成を有するものである。(Second Embodiment of the Present Invention) An incinerator according to a second embodiment of the present invention will be described with reference to FIG. FIG. 9 shows a schematic configuration diagram of main parts of an incinerator according to the present embodiment. As shown in FIG. 9, the incinerator 2 according to the present embodiment includes a primary combustion chamber 21, a secondary combustion chamber 22, a cyclone and a chimney (not shown), as in the first embodiment. The primary combustion chamber 21 and the secondary combustion chamber 22 are close to each other, and the heat in the primary combustion chamber 21 reaches the secondary combustion chamber 22 as it is, and the secondary burner is omitted. is there.
【0024】前記二次燃焼室22は、鋼板製の二重構造
の略円筒体で形成され、一次燃焼室21の上面の一部か
ら上方に突出して配設され、下部を一次燃焼室21内に
連通させてなる構成である。前記一次燃焼室21同様、
二次燃焼室22の二重構造の中間部には水が注入され
る。二次燃焼室22内には、メッシュ状に孔を多数穿設
された円筒体で形成される補助燃焼筒22a及びこの補
助燃焼筒22aを支持する円板でメッシュ状に孔を多数
穿設されてなる隔壁板22bが配設される。さらに、二
基の空気供給ファン22cが吹出口を水平に二次燃焼室
22内に向け、且つ吹出方向を二次燃焼室22中心から
ずらして補助燃焼筒22aの接線方向とするようにして
二次燃焼室22の側壁に配設される。The secondary combustion chamber 22 is formed of a substantially cylindrical body having a double structure made of a steel plate, is disposed so as to protrude upward from a part of the upper surface of the primary combustion chamber 21, and has a lower portion inside the primary combustion chamber 21. It is the structure made to communicate with. Like the primary combustion chamber 21,
Water is injected into the intermediate portion of the double structure of the secondary combustion chamber 22. In the secondary combustion chamber 22, a large number of holes are formed in a mesh shape with an auxiliary combustion tube 22a formed of a cylindrical body having a large number of holes formed in a mesh shape and a disk supporting the auxiliary combustion tube 22a. Is provided. Furthermore, the two air supply fans 22c direct the outlet horizontally into the secondary combustion chamber 22, and shift the outlet direction from the center of the secondary combustion chamber 22 so as to be tangential to the auxiliary combustion cylinder 22a. It is arranged on the side wall of the next combustion chamber 22.
【0025】次に、前記構成に基づく焼却炉における焼
却動作について説明する。前記第1の実施形態と同様
に、廃棄物50を廃棄物投入口21aより一次燃焼室2
1内に投入し、扉21cを閉じて廃棄物50に着火する
と共に空気吹出口21eから一次燃焼室21内に圧搾空
気を供給する。圧搾空気の供給は、燃焼開始時には複数
段の空気吹出口21eがより下段になるほど吹出させる
空気量を多く、定常燃焼状態では空気吹出口21eがよ
り上段になるほど吹出させる空気量を多くして、常に廃
棄物50へ空気を適切に供給して燃焼させる。Next, the incineration operation in the incinerator based on the above configuration will be described. Similarly to the first embodiment, the waste 50 is supplied from the waste inlet 21a to the primary combustion chamber 2.
1, the door 21c is closed, the waste 50 is ignited, and compressed air is supplied into the primary combustion chamber 21 from the air outlet 21e. At the start of combustion, the supply of compressed air increases the amount of air to be blown out as the air outlets 21e of a plurality of stages become lower, and in the steady combustion state, increases the amount of air to blow out as the air outlet 21e becomes upper. The air is always appropriately supplied to the waste 50 and burned.
【0026】こうした一次燃焼室21内の燃焼により、
廃棄物50は残灰を残して排ガス(ガス化あるいは蒸気
化した未燃成分を含む)及び燃残りの飛塵となり、二次
燃焼室22に送込まれる。温度を保ったまま二次燃焼室
22に入った排ガス及び飛塵は、隔壁板22bに規制さ
れて補助燃焼筒22a内に入り、周壁の側部に配設され
た多数の孔を経て二次燃焼室22内に噴出する。これら
排ガス及び飛塵は二次燃焼室22内における圧搾空気の
供給を受けて、撹拌と共に再燃焼が行われ、未燃分が完
全に燃焼する。完全燃焼により生じた排ガス及び飛灰は
二次燃焼室22から排出されて前記第1の実施形態と同
様にサイクロンに送込まれて排ガスと灰とに分離され、
別々に排出される。By the combustion in the primary combustion chamber 21,
The waste 50 leaves the residual ash and becomes exhaust gas (including unburned components that have been gasified or vaporized) and residual dust, and is sent to the secondary combustion chamber 22. Exhaust gas and flying dust entering the secondary combustion chamber 22 while maintaining the temperature are regulated by the partition plate 22b, enter the auxiliary combustion cylinder 22a, and pass through a large number of holes provided on the side of the peripheral wall to form the secondary exhaust gas. It is jetted into the combustion chamber 22. These exhaust gas and flying dust are supplied with compressed air in the secondary combustion chamber 22, are re-burned with stirring, and the unburned components are completely burned. Exhaust gas and fly ash generated by complete combustion are discharged from the secondary combustion chamber 22, sent to the cyclone as in the first embodiment, and separated into exhaust gas and ash,
Discharged separately.
【0027】このように、本実施の形態に係る焼却炉で
は、前記第1の実施の形態と同様、一次燃焼室21にお
いては廃棄物50自体の燃焼温度を高温になりすぎない
ようにして火格子21b等の過熱損傷が生じにくい上、
排ガス中からは有害成分をより効果的に減少させられ、
さらに、二次燃焼室22内で排ガス及び未燃成分の流れ
を適切に制御しながら、二次バーナーを用いずに空気の
吹込みのみで未燃成分を再燃焼させることにより、有害
成分の外部への放出低減はそのままに二次バーナーを省
いて装置の低コスト化を実現できる。As described above, in the incinerator according to the present embodiment, similarly to the first embodiment, in the primary combustion chamber 21, the combustion temperature of the waste 50 itself is set so as not to become too high. Overheating damage to the lattice 21b and the like is unlikely to occur, and
Harmful components can be more effectively reduced from exhaust gas,
Furthermore, by appropriately controlling the flow of the exhaust gas and the unburned components in the secondary combustion chamber 22 and reburning the unburned components only by blowing air without using the secondary burner, the harmful components can be reduced. It is possible to reduce the cost of the apparatus by omitting the secondary burner while maintaining the reduction of the emission to the apparatus.
【0028】[0028]
【発明の効果】以上のように本発明においては、一次燃
焼室に圧搾空気の吹出口を配設し、廃棄物の燃焼中に一
次燃焼室内に圧搾空気を吹込むことにより、圧搾空気を
吹込んだ部分が局所的に十分な空気で燃焼することとな
り、吹込んだ部分においてガス化した燃焼成分が高温で
且つ燃焼速度が速い状態で完全燃焼して有害な成分を発
生させず、焼却炉全体でこうした有害成分の排出量を抑
えられると共に、この圧搾空気の吹込みが局所的で燃焼
室全体の空気量に著しく影響を与えないことにより、廃
棄物全体が高温燃焼することはなく、燃焼室の過熱損傷
が起りにくく耐久性に優れるという効果を奏する。ま
た、本発明においては、吹出口を向い合う側壁において
互違いにずらして配設し、吹出した圧搾空気が互いに干
渉しないようにすることにより、干渉で圧搾空気が空気
量十分の領域を広く形成して廃棄物の燃焼を過度に促進
させることがなく、局所的な吹込みを維持しつつ吹込み
箇所を増やせることとなり、有害成分をより効果的に減
少させられるという効果を有する。また、本発明におい
ては、吹出口を上下に複数段に亘って配設し、燃焼室上
部と下部で圧搾空気の吹出状態を異ならせることができ
ることにより、燃焼室下部の廃棄物と燃焼室上部に上昇
した排ガス及び未燃ガスとの燃焼状態をそれぞれ最適な
状態に調整できることとなり、完全燃焼による有害成分
の低減と同時に燃焼室の底面及び側壁の過熱防止が図れ
るという効果を有する。また、本発明においては、圧搾
空気の吹出量を燃焼開始時には燃焼室上部側に比べ下部
側をより多くし、定常燃焼状態には逆に燃焼室上部側を
より多くすることにより、廃棄物全体を確実に着火させ
た後は適度な空気を供給して燃焼温度が高温になりすぎ
ないようにすると共に、排ガス中に含まれる未燃ガスや
飛塵には十分な空気を吹込んで高い燃焼温度で完全燃焼
させることができ、着火性を悪化させることなく有害成
分の流出量低減と燃焼室の過熱防止とが一連の焼却プロ
セスで確実に両立できるという効果を有する。また、本
発明においては、一次燃焼室と二次燃焼室の間に副燃焼
筒を配設し、副燃焼筒の周側壁の孔に排ガス及び未燃成
分を通過させることにより、孔の通過抵抗で排ガスの流
速を低下させることとなり、二次燃焼室内で排ガス及び
未燃成分の滞留時間を長くでき、燃焼を確実に進行させ
られることに加え、一次燃焼室内の熱で赤熱した副燃焼
筒への排ガス及び未燃成分の接触で未燃成分の燃焼を促
進させられることとなり、放出される排ガス中から有害
成分をより一層低減できるという効果を有する。また、
本発明においては、二次燃焼室内にそれぞれ多数の孔を
穿設された補助燃焼筒及び隔壁板を配設し、二次燃焼室
に入った排ガス及び未燃成分を隔壁で規制して補助燃焼
筒内に入れ、周側壁の多数の孔を経て二次燃焼室内に噴
出する排ガス及び未燃成分に二次バーナーによる火炎放
射で補助燃焼筒周りの回転運動を生じさせながら燃焼さ
せることにより、未燃成分が排ガスと共に撹拌されなが
ら再燃焼することとなり、未燃成分が完全に燃焼して有
害成分の外部への放出量を著しく抑えられるという効果
を有する。また、本発明においては、二次燃焼室内に一
次燃焼室から熱を導入し、未燃成分を燃焼させることに
より、二次燃焼室においてバーナー等の助燃手段が不要
となり、コストダウンが図れるという効果を有する。As described above, in the present invention, the compressed air is blown into the primary combustion chamber by arranging the compressed air outlet in the primary combustion chamber and blowing the compressed air into the primary combustion chamber during the combustion of waste. The burned part will be locally burned with sufficient air, and the gasified combustion component in the blown part will be completely burned at a high temperature and a fast burning rate to generate no harmful components, and the incinerator The emission of such harmful components can be reduced as a whole, and the compressed air blowing does not significantly affect the air volume in the entire combustion chamber. This produces an effect that the room is hardly damaged by overheating and has excellent durability. Further, in the present invention, the air outlets are arranged so as to be staggered on the facing side walls so that the blown air does not interfere with each other, so that the compressed air forms a wide enough area of the air by the interference. Therefore, it is possible to increase the number of blowing points while maintaining the local blowing without excessively promoting the combustion of the waste, which has the effect of reducing harmful components more effectively. Further, in the present invention, the outlets are disposed in a plurality of stages vertically, and the blowing state of the compressed air can be different between the upper part and the lower part of the combustion chamber. Thus, the combustion state of the exhaust gas and the unburned gas that have risen to an optimum level can be adjusted to optimal states, respectively. This has the effect of reducing harmful components due to complete combustion and preventing overheating of the bottom and side walls of the combustion chamber. Further, in the present invention, by increasing the amount of compressed air blowout at the lower side at the start of combustion as compared to the upper side of the combustion chamber, and by increasing the amount at the upper side of the combustion chamber in the steady combustion state, the entire waste is reduced. After igniting properly, supply appropriate air to prevent the combustion temperature from becoming too high, and blow enough air to unburned gas and flying dust contained in exhaust gas to increase the combustion temperature. Thus, there is an effect that the reduction of harmful components and the prevention of overheating of the combustion chamber can be reliably achieved in a series of incineration processes without deteriorating ignitability. Further, in the present invention, a sub-combustion cylinder is disposed between the primary combustion chamber and the secondary combustion chamber, and the exhaust gas and unburned components are passed through the holes on the peripheral side wall of the sub-combustion cylinder, so that the passage resistance of the holes is reduced. As a result, the flow rate of the exhaust gas is reduced, so that the residence time of the exhaust gas and unburned components in the secondary combustion chamber can be lengthened, combustion can proceed reliably, and the sub-combustion cylinder glows with heat in the primary combustion chamber. As a result, the combustion of the unburned components can be promoted by the contact between the exhaust gas and the unburned components, and the harmful components can be further reduced from the discharged exhaust gas. Also,
In the present invention, an auxiliary combustion cylinder and a partition plate each having a large number of holes are disposed in the secondary combustion chamber, and the exhaust gas and unburned components entering the secondary combustion chamber are regulated by the partition to perform auxiliary combustion. The exhaust gas and unburned components ejected into the secondary combustion chamber through a number of holes in the peripheral side wall are burned into the cylinder while generating rotational motion around the auxiliary combustion cylinder by flame radiation of the secondary burner. The combustible component is recombusted while being stirred with the exhaust gas, so that the unburned component is completely burned and the amount of harmful components released to the outside can be significantly suppressed. Further, in the present invention, by introducing heat from the primary combustion chamber into the secondary combustion chamber and burning unburned components, an auxiliary combustion means such as a burner is not required in the secondary combustion chamber, so that the cost can be reduced. Having.
【図面の簡単な説明】[Brief description of the drawings]
【図1】本発明の第1の実施の形態に係る焼却炉の正面
図である。FIG. 1 is a front view of an incinerator according to a first embodiment of the present invention.
【図2】本発明の第1の実施の形態に係る焼却炉の平面
図である。FIG. 2 is a plan view of the incinerator according to the first embodiment of the present invention.
【図3】本発明の第1の実施の形態に係る焼却炉の側面
図である。FIG. 3 is a side view of the incinerator according to the first embodiment of the present invention.
【図4】本発明の第1の実施の形態に係る焼却炉の要部
概略構成図である。FIG. 4 is a schematic configuration diagram of a main part of the incinerator according to the first embodiment of the present invention.
【図5】本発明の第1の実施の形態に係る焼却炉の圧搾
空気吹出状態説明図である。FIG. 5 is an explanatory view of a compressed air blowing state of the incinerator according to the first embodiment of the present invention.
【図6】(A)は本発明の第1の実施の形態に係る焼却
炉の二次燃焼室の縦断面図である。(B)は本発明の第
1の実施の形態に係る焼却炉の二次燃焼室の横断面図で
ある。FIG. 6A is a longitudinal sectional view of a secondary combustion chamber of the incinerator according to the first embodiment of the present invention. (B) is a cross-sectional view of the secondary combustion chamber of the incinerator according to the first embodiment of the present invention.
【図7】(A)は本発明の第1の実施の形態に係る焼却
炉の一次燃焼室の燃焼初期状態説明図である。(B)は
本発明の第1の実施の形態に係る焼却炉の一次燃焼室の
定常燃焼状態説明図である。FIG. 7A is an explanatory diagram of an initial combustion state of a primary combustion chamber of an incinerator according to the first embodiment of the present invention. (B) is an explanatory diagram of a steady combustion state of the primary combustion chamber of the incinerator according to the first embodiment of the present invention.
【図8】本発明の第1の実施の形態に係る焼却炉の一次
燃焼室の焼却プロセス説明図である。FIG. 8 is an explanatory diagram of the incineration process of the primary combustion chamber of the incinerator according to the first embodiment of the present invention.
【図9】本発明の第2の実施の形態に係る焼却炉の要部
概略構成図である。FIG. 9 is a schematic configuration diagram of a main part of an incinerator according to a second embodiment of the present invention.
1、2 焼却炉 11、21 一次燃焼室 11a、21a 廃棄物投入口 11b、21b 火格子 11c、21c 扉 11d、21d 水 11e、21e 空気吹出口 11f、21f 一次バーナー 12、22 二次燃焼室 12a、22a 補助燃焼筒 12b、22b 隔壁板 12c 二次バーナー 13 サイクロン 14 煙突 15 副燃焼筒 22c 空気供給ファン 50 廃棄物 1, 2 incinerator 11, 21 primary combustion chamber 11a, 21a waste inlet 11b, 21b grate 11c, 21c door 11d, 21d water 11e, 21e air outlet 11f, 21f primary burner 12, 22 secondary combustion chamber 12a , 22a Auxiliary combustion cylinder 12b, 22b Partition plate 12c Secondary burner 13 Cyclone 14 Chimney 15 Secondary combustion cylinder 22c Air supply fan 50 Waste
Claims (7)
一次燃焼室に連通し、一次燃焼室における未燃成分を燃
焼させる二次燃焼室とを有する焼却炉において、 前記一次燃焼室の内側壁に複数の圧搾空気の吹出口が配
設されることを特徴とする焼却炉。1. An incinerator having a primary combustion chamber for burning waste and a secondary combustion chamber communicating with the primary combustion chamber and burning unburned components in the primary combustion chamber, wherein an inside of the primary combustion chamber is provided. An incinerator wherein a plurality of compressed air outlets are provided on a wall.
配設位置を互違いにずらして配設されることを特徴とす
る焼却炉。2. The incinerator according to claim 1, wherein the plurality of outlets are arranged so that respective arrangement positions on inner walls facing each other are staggered. Furnace.
いて、 前記複数の吹出口が、内側壁上下方向へ複数段配設され
ることを特徴とする焼却炉。3. The incinerator according to claim 1, wherein the plurality of outlets are arranged in a plurality of stages in a vertical direction of an inner wall.
どより多くの空気を吹出し、定常燃焼状態にはより上段
になるほどより多くの空気を吹出すことを特徴とする焼
却炉。4. The incinerator according to claim 3, wherein the plurality of outlets blows out more air at a lower stage at the start of combustion, and more air at a higher stage in a steady combustion state. An incinerator characterized by blowing air.
の焼却炉において、 多数の孔が穿設された金属穿孔体又はメッシュ状の金属
編目体からなる周側壁を有する略筒状体で形成され、当
該筒状体内部を二次燃焼室に連通させ、前記一次燃焼室
内に突出して配設される副燃焼筒を備えることを特徴と
する焼却炉。5. The incinerator according to any one of claims 1 to 4, wherein the incinerator is a substantially cylindrical body having a peripheral wall made of a metal perforated body or a mesh-shaped metal stitch body having a large number of holes. An incinerator characterized in that the incinerator includes a formed sub-combustion tube that is formed and communicates the inside of the tubular body with a secondary combustion chamber and protrudes into the primary combustion chamber.
の焼却炉において、 前記二次燃焼室が、略円筒状に形成されて前記一次燃焼
室上側に配設されると共に、前記二次燃焼室の略中心に
配設されて周側壁に多数の孔が形成される略筒状体から
なる補助燃焼筒と、当該補助燃焼筒の一次燃焼室寄りの
端部に連設されて二次燃焼室を横に仕切る略円板で多数
の孔を形成されてなる隔壁板と、二次燃焼室内部におい
て補助燃焼筒の略円断面の接線方向に火炎を放射する二
次バーナーとを備えてなることを特徴とする焼却炉。6. The incinerator according to claim 1, wherein the secondary combustion chamber is formed in a substantially cylindrical shape and is disposed above the primary combustion chamber, and the secondary combustion chamber is disposed above the primary combustion chamber. An auxiliary combustion cylinder, which is disposed substantially at the center of the combustion chamber and has a substantially cylindrical body having a large number of holes formed in a peripheral side wall, and a secondary combustion chamber connected to an end of the auxiliary combustion cylinder near the primary combustion chamber. A partition plate having a large number of holes formed by a substantially circular plate that partitions a combustion chamber horizontally, and a secondary burner that emits flame in a tangential direction of a substantially circular cross section of the auxiliary combustion cylinder inside the secondary combustion chamber. An incinerator characterized by becoming.
の焼却炉において、 周側壁に多数の孔が穿設される略円筒体で形成され、当
該略円筒体内部を前記一次燃焼室上部に連通させて前記
二次燃焼室内に配設される補助燃焼筒を備え、 前記一次燃焼室における未燃成分を補助燃焼筒の孔から
二次燃焼室内に噴出させると共に、前記一次燃焼室の廃
棄物燃焼領域において生じる熱を二次燃焼室にそのまま
導入して前記未燃成分を燃焼させることを特徴とする焼
却炉。7. The incinerator according to claim 1, wherein the incinerator is formed of a substantially cylindrical body having a plurality of holes formed in a peripheral side wall, and the inside of the substantially cylindrical body is an upper part of the primary combustion chamber. An auxiliary combustion cylinder disposed in the secondary combustion chamber in communication with the secondary combustion chamber, wherein unburned components in the primary combustion chamber are ejected from a hole of the auxiliary combustion cylinder into the secondary combustion chamber, and disposal of the primary combustion chamber is performed. An incinerator characterized in that heat generated in a material combustion zone is directly introduced into a secondary combustion chamber to burn the unburned components.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17298797A JPH116609A (en) | 1997-06-13 | 1997-06-13 | Incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17298797A JPH116609A (en) | 1997-06-13 | 1997-06-13 | Incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH116609A true JPH116609A (en) | 1999-01-12 |
Family
ID=15952083
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17298797A Pending JPH116609A (en) | 1997-06-13 | 1997-06-13 | Incinerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH116609A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN120760133A (en) * | 2025-07-31 | 2025-10-10 | 佛山市顺德区豫锐涂装设备有限公司 | An intelligent air-gas linkage control system for a gas burner |
-
1997
- 1997-06-13 JP JP17298797A patent/JPH116609A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN120760133A (en) * | 2025-07-31 | 2025-10-10 | 佛山市顺德区豫锐涂装设备有限公司 | An intelligent air-gas linkage control system for a gas burner |
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