JPH02157511A - Incinerating device - Google Patents
Incinerating deviceInfo
- Publication number
- JPH02157511A JPH02157511A JP31447388A JP31447388A JPH02157511A JP H02157511 A JPH02157511 A JP H02157511A JP 31447388 A JP31447388 A JP 31447388A JP 31447388 A JP31447388 A JP 31447388A JP H02157511 A JPH02157511 A JP H02157511A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- furnace
- air
- duct
- ash
- 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
- 239000000428 dust Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 3
- 239000002956 ash Substances 0.000 abstract 4
- 235000002918 Fraxinus excelsior Nutrition 0.000 abstract 2
- 230000000149 penetrating effect Effects 0.000 abstract 1
- 230000002093 peripheral effect Effects 0.000 abstract 1
- 239000000843 powder Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- 238000002485 combustion reaction Methods 0.000 description 22
- 239000000463 material Substances 0.000 description 20
- 239000002699 waste material Substances 0.000 description 8
- 239000004033 plastic Substances 0.000 description 6
- 229920003023 plastic Polymers 0.000 description 6
- 239000005060 rubber Substances 0.000 description 6
- 239000002023 wood Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000007664 blowing Methods 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- -1 miscellaneous light Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
この発明は、焼却装置に関し、廃棄物の燃焼後の排出粉
塵濃度を低く抑えることができ、公害防止に役立つ焼却
装置に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to an incinerator, and more particularly, to an incinerator that can suppress the concentration of dust emitted after combustion of waste to a low level and is useful for preventing pollution.
〈従来技術〉
従来、雑光、木材、プラスチックス、ゴム等からなる廃
棄物を燃焼処理する焼却装置としては、焼却炉下部に、
残灰は通すが燃焼物は通さない網目状部材を配設し、焼
却炉下部に空間部を形成して、この空間部から燃焼に必
要な空気を送り込みつつ、燃焼物を燃焼させる構造のも
のが知られている。<Prior art> Conventionally, incinerators for burning waste such as miscellaneous light, wood, plastics, rubber, etc. have been equipped with a
An incinerator with a structure in which a mesh member is installed that allows the remaining ash to pass through but not the combustible materials, and a space is formed at the bottom of the incinerator, and the air necessary for combustion is sent through this space while the combustible materials are combusted. It has been known.
〈発明が解決しようとする課題〉
しかしながら、上記焼却装置にあっては、網目状部材を
通って、焼却炉下部の空間に堆積した残灰が空気の送り
込みのさまたげとなり、そのため空間部から残灰を定期
的に除去しなければならず、残灰の焼却炉内からの除去
作業は面倒なうえ、その間焼却作業を中止しなければな
らない等の弊害があった。<Problems to be Solved by the Invention> However, in the above-mentioned incinerator, the residual ash accumulated in the space at the bottom of the incinerator through the mesh member obstructs the feeding of air, so that the residual ash is removed from the space. The residual ash must be removed periodically, and the work of removing the remaining ash from inside the incinerator is troublesome, and the incineration work has to be stopped during that time.
そこで、上記焼却炉内の空間部から高温圧縮空気を炉内
に送り込み残灰を燃焼物ともども焼却炉上方へ吹き上げ
、この吹き上げられた残灰を焼却炉の上方で回収し、残
灰が焼却炉内下部に、堆積しないようにした構造のもの
も発明されたが、残灰を燃焼中の燃焼物とともに、焼却
炉上方へ一気に吹き上げるものであったため、高温の燃
焼物から残灰を分離回収するための冷却装置等を焼却炉
上部に設ける等の必要があり、装置が非常に犬山りとな
るほか、コスト的にも割高なものであった。Therefore, high-temperature compressed air is sent into the incinerator from the space inside the incinerator, the remaining ash is blown up into the incinerator together with the combustion materials, and the blown up remaining ash is collected above the incinerator. An incinerator with a structure that prevented it from accumulating in the lower part of the incinerator was also invented, but since the remaining ash was blown up into the upper part of the incinerator along with the burning materials, the remaining ash was separated and recovered from the high-temperature combustion materials. It was necessary to install a cooling device etc. on the top of the incinerator for this purpose, which made the equipment extremely complicated and also expensive.
また、上記いずれの焼却装置にあっても、プラスチック
ス、ゴム等の加熱により流動する廃棄物を燃焼させた場
合には、焼却炉の下部に配設した網目状部材の網目がこ
れら流動燃焼物にて塞がれ、燃焼に必要な空気を炉内に
供給できなくなる等の弊害があった。In addition, in any of the above incinerators, when fluid wastes such as plastics and rubber are burned by heating, the mesh of the mesh member installed at the bottom of the incinerator will prevent these fluids from being burned. This caused problems such as the inability to supply the air necessary for combustion into the furnace.
この発明は、これら従来の焼却装置の実情に鑑み発明し
たものであって、残灰の除去作業等を要さず、また冷却
機構等大川りな装置を必要とせず、しかもコスト安価な
焼却装置を提供することを目的としている。This invention was invented in view of the actual situation of these conventional incinerators, and it is an incineration device that does not require work to remove residual ash, does not require any equipment such as a cooling mechanism, and is inexpensive. is intended to provide.
く課題を解決するための手段〉
上記課題を解決するためのこの発明の焼却装置の構成は
、焼却炉、焼却炉内に空気を送り込む循環送風機および
サイクロンを具備し、焼却炉壁下部近傍には、炉内の燃
焼物を燃焼させ、残灰を上方へ吹き上げる循環送風機か
らの空気の導入口を、炉内下方側に向けてまたは水平に
形成してあり、焼却炉上方のダクト部分には、吹き上げ
られた残灰を上方へ吸い上げる負圧発生機構を設けてな
るとともに、吸い上げられた残灰を旋回上昇させる旋回
羽根が配設してあり、さらにダクト上部には、負圧発生
機構にて吸い上げられた残灰を送風空気と分離して回収
するサイクロンへの連結管を接続してあり、サイクロン
には、残灰分離後の空気を上記循環送風機に送り込む連
結管が接続されてなる点に存する。Means for Solving the Problems> The incinerator of the present invention for solving the above problems is equipped with an incinerator, a circulation blower for feeding air into the incinerator, and a cyclone, and a cyclone near the bottom of the incinerator wall. The air inlet from the circulation blower that burns the combustion materials in the incinerator and blows the remaining ash upwards is formed toward the lower side of the incinerator or horizontally, and in the duct part above the incinerator, A negative pressure generating mechanism is installed to suck up the blown up residual ash upwards, and a swirling blade is also installed to swirl and raise the sucked up residual ash.Furthermore, at the top of the duct, a negative pressure generating mechanism is installed to suck up the blown up residual ash. A connecting pipe is connected to a cyclone that separates the remaining ash from the blast air and collects it, and a connecting pipe that sends the air after separating the residual ash to the circulation blower is connected to the cyclone. .
く作用〉
上記構成からなるこの発明の焼却装置によれば、焼却炉
壁下部近傍に、炉内の燃焼物を燃焼させ、残灰を上方へ
吹き上げる空気の導入口を、炉内下方側に向けてまたは
水平に形成してなるものゆえ、燃焼後の残灰を炉内上方
に吹き上げることができる。According to the incinerator of the present invention having the above configuration, the inlet for the air that burns the combustion material in the furnace and blows up the remaining ash upward is provided near the lower part of the incinerator wall and is directed toward the lower side of the furnace. Because it is formed vertically or horizontally, the remaining ash after combustion can be blown upward into the furnace.
焼却炉上方のダクト部分に、負圧発生機構を設けるとと
もに、残灰を旋回上昇させる旋回羽根を配設し、ダクト
上部にサイクロンへの連結管を接続してなるものゆえ、
吹き上げられた残灰は負圧発生機構にてさらに焼却炉上
方のダクト部分へと上昇し、旋回羽根による旋回にてダ
クトの内壁面に衝突しながら1臂する。そして、ダクト
上部に設けられた連結管にてサイクロンへと導かれ、サ
イクロンにて残灰は送風空気と分離し、回収できる。A negative pressure generation mechanism is installed in the duct above the incinerator, as well as swirling blades that swirl and lift the remaining ash, and a connecting pipe to the cyclone is connected to the top of the duct.
The blown-up residual ash further rises to the duct part above the incinerator by the negative pressure generating mechanism, and collides with the inner wall surface of the duct as it is swirled by the swirling blades. The remaining ash is then led to a cyclone through a connecting pipe installed at the top of the duct, where the remaining ash is separated from the blown air and can be recovered.
残灰を分離した後の送風空気は連結管にて循環送風機に
運ばれ、循環送風機にて焼却炉内の燃焼物を燃焼させ、
残灰を炉内上方へと吹き上げるのに再使用できる。After the residual ash has been separated, the blown air is conveyed through a connecting pipe to a circulation blower, which burns the combustion materials in the incinerator.
It can be reused to blow the remaining ash upwards into the furnace.
〈実施例〉
以下にこの発明の実施例について図を参照しながら詳述
する。<Examples> Examples of the present invention will be described in detail below with reference to the drawings.
第1図は、この発明の焼却装置の概略断面図を示すもの
である。FIG. 1 shows a schematic sectional view of the incinerator of the present invention.
焼却装置は、雑界、木材、プラスチックス、ゴム等から
なる廃棄物を燃焼させる焼却炉(1)、焼却炉(1)内
に空気を送り込む循環送風機(2)および燃焼後の残灰
を送風空気より分離回収するサイクロン(3)から構成
されている。The incinerator consists of an incinerator (1) that burns waste made of miscellaneous materials, wood, plastics, rubber, etc., a circulation blower (2) that blows air into the incinerator (1), and a blower that blows the remaining ash after combustion. It consists of a cyclone (3) that separates and collects air.
焼却炉(1)の壁下部近傍には、循環送風機(2)から
の送風空気の導入口(11)が、周囲適宜個所に複数個
(図の場合には3個所)貫通形成されている(第2図、
第3図参照)。この空気導入口(11〉は、炉(1)内
の燃焼物を燃焼させ、残灰を上方へ吹き上げるものであ
り、第1図に示すように炉(1)内の下方側へ傾斜を付
けて貫通形成したものが好適であるが、水平に貫通形成
して実施してもよい。なお、(12)は焼却炉内の清掃
用の小窓である。Near the bottom of the wall of the incinerator (1), a plurality of inlets (11) for introducing air from the circulation blower (2) are formed at appropriate locations around the periphery (three in the case of the figure). Figure 2,
(See Figure 3). This air inlet (11) is for burning the combustion material in the furnace (1) and blowing up the remaining ash upward, and as shown in Figure 1, it is slanted downward in the furnace (1). Although it is preferable to form the hole through the incinerator horizontally, it is also possible to form the hole through the incinerator horizontally.Note that (12) is a small window for cleaning inside the incinerator.
焼却炉(1)上方のダクト(13)部分には、吹き上げ
られた残灰を上方へ吸い上げる負圧発生機構(4)が設
けられている。この負圧発生機構(4)は焼却炉(1)
内の上方に空気を送り込む送風機(40)、炉内中央部
分に配設された細長円筒状吹上げ管(41)、送風機(
40)と細長円筒状吹上げ管(41〉を連結する連結管
(42)および炉(1)内で吹上げ管(41〉の先端上
方に配設された板材(12)より構成されている。A negative pressure generating mechanism (4) is provided in the duct (13) above the incinerator (1) to suck up the blown up residual ash. This negative pressure generation mechanism (4) is the incinerator (1)
A blower (40) that blows air upwards inside the furnace, an elongated cylindrical blow-up pipe (41) disposed in the central part of the furnace,
40) and the elongated cylindrical blow-up pipe (41>), and a plate material (12) disposed above the tip of the blow-off pipe (41>) in the furnace (1). .
そして、細長円筒状吹上げ管(41)は、送風機(40
)より送られてくる空気が、炉(1)内に勢いよく噴出
するように、その先端が先細形状に形成されている。ま
た吸材(12)には、中央に貫通孔が形成されている。The elongated cylindrical blow-up pipe (41) is connected to the blower (40).
) The tip thereof is formed into a tapered shape so that the air sent from the furnace (1) is blown out with force into the furnace (1). Moreover, a through hole is formed in the center of the absorbent material (12).
送風機(40)より送られてきた空気は、吹上げ管(4
1)の先端先細部分より勢いよく噴出する。そして、こ
の勢いよく噴出した空気が板材(12)に形成された中
央の貫通孔を勢いよく通過することにより、炉(1)内
の板材(12〉より下方側部分が負圧状態となり、送風
空気にて吹き上げられた残灰は、さらに炉(1)内上方
のダクト(13)部分へと吸い上げられる。The air sent from the blower (40) is passed through the blow-up pipe (4
1) It ejects forcefully from the tapered part of the tip. Then, this vigorously blown air passes through the central through-hole formed in the plate material (12), creating a negative pressure in the area below the plate material (12>) in the furnace (1), causing the air to blow out. The remaining ash blown up by the air is further sucked up into the duct (13) above the furnace (1).
また、炉(1)内上方のダクト(13)部分には、吸い
上げられた残灰を旋回上昇させる断面扇形の多数の旋回
羽根(5)が傾斜を付けて配設しである。この旋回羽根
(5)の一端は前記吹上げ管(41)の外壁に取付けら
れ、他端は炉(1)の内壁に取付けられている。Further, in the upper part of the duct (13) inside the furnace (1), a large number of swirling vanes (5) having a fan-shaped cross section are arranged at an angle to swirl and raise the sucked up residual ash. One end of the swirl vane (5) is attached to the outer wall of the blow-up pipe (41), and the other end is attached to the inner wall of the furnace (1).
そして、炉(1)外に設けられた傾斜調整部材(5o)
によって、羽根(5)の傾斜が調整できるようになって
いる。And an inclination adjustment member (5o) provided outside the furnace (1)
This allows the inclination of the blade (5) to be adjusted.
ダクト(13)の上部には、負圧発生機構(4)にて吸
い上げられた残灰を送風空気より分離して回収するサイ
クロン(3)への連結管(6)が接続されている。A connecting pipe (6) to the cyclone (3) is connected to the upper part of the duct (13), which separates the residual ash sucked up by the negative pressure generating mechanism (4) from the blown air and collects it.
残灰は、旋回羽根(5)による旋回にてダクト(13)
の内壁面に衝突旋回しながら上昇し、この連結管(6)
にて一部の送風空気とともにサイクロン(3)に導かれ
る。The remaining ash is sent to the duct (13) by swirling by the swirling vane (5).
This connecting pipe (6) collides with the inner wall of the
It is guided to the cyclone (3) along with some of the blown air.
サイクロン(3)はロート状をなしており、下部に残灰
回収部(30)が設けられている。連結管(6)にて焼
却炉(1)より送風空気にて運ばれてきた残灰は、サイ
クロン(3)内の円筒(31)の外周面に衝突し、回収
部(30)へと落下回収される。The cyclone (3) has a funnel shape, and a residual ash collection section (30) is provided at the bottom. The remaining ash carried by the blown air from the incinerator (1) through the connecting pipe (6) collides with the outer circumferential surface of the cylinder (31) in the cyclone (3) and falls into the collection section (30). It will be collected.
なお、トラック等の残灰搬送手段を、回収部(30)の
下方に、あるいは回収部(30)を省略して直接サイク
ロン(3)の下方に配置し、サイクロンにて分離回収し
た残灰を搬送する。In addition, the remaining ash conveying means such as a truck is arranged below the collection part (30) or directly below the cyclone (3) by omitting the collection part (30), and the remaining ash separated and collected by the cyclone is disposed. transport.
そして、残灰を分離した送風空気は連結管(7)にて循
環送風機(2)に運ばれ、再び焼却炉(1)内の燃焼物
を燃焼させ、燃焼後の残灰を焼却炉(1)上方のダクト
(13)部分へと吹き上げるのに使用する。Then, the blast air from which the residual ash has been separated is conveyed to the circulation blower (2) through the connecting pipe (7), and the combustion materials in the incinerator (1) are combusted again, and the residual ash after combustion is transferred to the incinerator (1). ) Used to blow air up to the upper duct (13).
なお、第1図中(9)(10)はともにダンパーを示し
ており、ダンパー(9)は連結管(7)の途中に取付け
られ、循環送風機(2)へ運ばれ炉(1)内で再燃焼等
に使用される送風空気の吸引空気量の調整を行なうもの
である。一方ダンバー(10)は、外部から取入られる
空気の取入れ口に取付けられており、燃焼に使用される
空気の酸素濃度を適性に保つと共に送風空気の温度調整
を行なうものである。In addition, (9) and (10) in Fig. 1 both indicate dampers, and the damper (9) is installed in the middle of the connecting pipe (7), and is carried to the circulation blower (2) in the furnace (1). This adjusts the amount of air sucked into the blown air used for re-combustion, etc. On the other hand, the damper (10) is attached to the intake port for air taken in from the outside, and serves to keep the oxygen concentration of the air used for combustion at an appropriate level and to adjust the temperature of the blown air.
上記構成からなる焼却装置にて、プラスチック。An incinerator with the above configuration is used to dispose of plastic.
木材、ゴム分等からなる廃棄物をそれぞれ燃焼させ、焼
却炉(1)のダクト(13)上方開口部付近での排出粉
塵濃度を測定したところ、いずれも0.2g/Nm’以
下の直を示し、好適な結果が得られた。When wastes consisting of wood, rubber, etc. were burned and the emitted dust concentration near the upper opening of the duct (13) of the incinerator (1) was measured, all of them were found to be less than 0.2 g/Nm'. and favorable results were obtained.
なお、焼却炉(1)の形状としては、第2図に示すよう
に水平断面円状のものであってもよく、第3図に示すよ
うに水平断面角形のものであってもよい。また、上記実
施例では、空気導入口(11)を上下−段で複数設けた
ものを示したが、上下複数段に形成してもよく(図示せ
ず)、ざらに負圧発生機構(4)における吹上げ管(4
1)への送風を送風機(2)に兼用させ、送風機(40
)を省略する実施も可能である。その他この発明の要旨
を変更しない範囲で種々の設計変更を施すことができる
。The shape of the incinerator (1) may be circular in horizontal cross section as shown in FIG. 2, or rectangular in horizontal cross section as shown in FIG. 3. Further, in the above embodiment, a plurality of air inlets (11) are provided in upper and lower stages, but they may be formed in multiple upper and lower stages (not shown). ) in the blow-up pipe (4
The blower (2) is also used to blow air to 1), and the blower (40
) is also possible. Various other design changes can be made without changing the gist of the invention.
〈発明の効果〉
上記構成からなるこの発明の焼却装置によれば、焼却炉
壁下部近傍に、炉内の燃焼物を燃焼させ、残灰を上りへ
吹き上げる空気の導入口を炉内下方側に向けてまたは水
平に形成しであるゆえ、燃焼後の残灰を炉内上方に吹き
上げることができ、炉内下部に燃焼後の残灰が堆積する
のを防ぐことができる。<Effects of the Invention> According to the incinerator of the present invention having the above-mentioned configuration, an air inlet for combusting the combustion materials in the furnace and blowing up the remaining ash is provided near the lower part of the incinerator wall on the lower side of the furnace. Since it is formed facing or horizontally, the residual ash after combustion can be blown upward into the furnace, and it is possible to prevent the residual ash after combustion from accumulating in the lower part of the furnace.
焼却炉上方のダクト部分に、負圧発生機構を設けるとと
もに、残灰を旋回上昇させる旋回羽根を配設し、ダクト
上部にサイクロンへの連結管を接続してなるものゆえ、
吹き上げられた残灰は負圧発生機構にてダクト上方へと
上昇し、旋回羽根による旋回にてダクトの内壁面に衝突
しながら上昇する。そして、ダクト上部に設けられた連
結管にてサイクロンへと導かれる。したがって、ダクト
上方開口部でのυト出粉塵濃度を低く押さ得ることがで
き、好適なものとなる。A negative pressure generation mechanism is installed in the duct above the incinerator, as well as swirling blades that swirl and lift the remaining ash, and a connecting pipe to the cyclone is connected to the top of the duct.
The blown up residual ash rises to the upper part of the duct by the negative pressure generating mechanism, and rises while colliding with the inner wall surface of the duct by swirling by the swirling blades. Then, it is guided to the cyclone through a connecting pipe installed at the top of the duct. Therefore, the concentration of emitted dust at the upper opening of the duct can be kept low, which is preferable.
サイクロンにて、残灰は送風空気と分離され、例えば、
サイクロンの下部に設けた回収箱にて回収でき、従来の
焼却装置のように残灰回収のため、焼却作業を中止した
りする必要はなく、容易に残灰の回収処理ができるもの
となる。In the cyclone, the remaining ash is separated from the blast air, e.g.
The ash can be collected in a collection box installed at the bottom of the cyclone, and unlike conventional incinerators, there is no need to stop the incineration operation to collect the ash, making it easy to collect and process the ash.
また、残灰を燃焼物から分離回収するための冷却装置等
犬山りな機構を設ける必要はなく、コスト安価にて廃棄
物を焼却処理できるものとなる。Further, there is no need to provide a complicated mechanism such as a cooling device for separating and recovering residual ash from the combustion material, and the waste can be incinerated at low cost.
残灰を分離した後の送風空気は連結管にて循環送風機に
運ばれ、循環送風機にて焼却炉内の燃焼物を燃焼させる
のに再使用でき好適である。The blown air after the residual ash has been separated is conveyed to a circulation blower through a connecting pipe, and can be reused by the circulation blower to burn the combustion materials in the incinerator.
さらに、この発明によれば従来の焼却装置にあって、プ
ラスチックス、ゴム等の加熱により流動するものを有す
る廃棄物を燃焼させたさいに生じていた網目状部材の網
目がこれら流動燃焼物にて塞がれ燃焼に必要な空気を炉
内に供給できなくなる等の弊害を解消できる等、雑光、
木材、プラスチックス、ゴム等を有するあらゆるの廃棄
物の焼却装置として従来にない好適なものを提供できる
。Furthermore, according to the present invention, in conventional incinerators, the network of the mesh member that is generated when burning waste that has materials that flow when heated, such as plastics and rubber, can be used to prevent these fluid combustion materials. Eliminates harmful effects such as the inability to supply the air necessary for combustion into the furnace due to blockage, etc.
It is possible to provide an unprecedented and suitable incineration device for all types of waste including wood, plastics, rubber, etc.
第1図はこの発明の焼却装置の一実施例を示す概略断面
図、第2図は焼却炉の水平断面図、第3図は変更例を示
す水平断面図である。
(1)・・・・・・焼却炉、(11〉・・・・・・空気
導入口、(13)・・・・・・ダクト
(2)・・・・・・循環送風機、
(3)・・・・・・サイクロン、
(4)・・・・・・負圧発生機構、
(5)・・・・・・旋回羽根、
(6) (7)・・・・・・連結管。FIG. 1 is a schematic sectional view showing one embodiment of the incinerator of the present invention, FIG. 2 is a horizontal sectional view of the incinerator, and FIG. 3 is a horizontal sectional view showing a modified example. (1)...Incinerator, (11>...Air inlet, (13)...Duct (2)...Circulating blower, (3) Cyclone, (4) Negative pressure generation mechanism, (5) Swivel vane, (6) (7) Connecting pipe.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31447388A JPH02157511A (en) | 1988-12-12 | 1988-12-12 | Incinerating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31447388A JPH02157511A (en) | 1988-12-12 | 1988-12-12 | Incinerating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02157511A true JPH02157511A (en) | 1990-06-18 |
Family
ID=18053753
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31447388A Pending JPH02157511A (en) | 1988-12-12 | 1988-12-12 | Incinerating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02157511A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06331116A (en) * | 1993-05-24 | 1994-11-29 | Kawasaki Heavy Ind Ltd | Incinerating method of granulated body of waste and incinerator therefor |
JPH0972523A (en) * | 1995-09-01 | 1997-03-18 | Mie Horo Kk | Smokeless odorless incinerating furnace |
WO2000014450A1 (en) * | 1998-09-04 | 2000-03-16 | Maejima, Fumio | Incinerator for removing noxious substances |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54162863A (en) * | 1978-06-13 | 1979-12-24 | Akoo Kk | Reignition dust collector in incinerator |
JPS5514904U (en) * | 1978-07-10 | 1980-01-30 |
-
1988
- 1988-12-12 JP JP31447388A patent/JPH02157511A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS54162863A (en) * | 1978-06-13 | 1979-12-24 | Akoo Kk | Reignition dust collector in incinerator |
JPS5514904U (en) * | 1978-07-10 | 1980-01-30 |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH06331116A (en) * | 1993-05-24 | 1994-11-29 | Kawasaki Heavy Ind Ltd | Incinerating method of granulated body of waste and incinerator therefor |
JPH0972523A (en) * | 1995-09-01 | 1997-03-18 | Mie Horo Kk | Smokeless odorless incinerating furnace |
WO2000014450A1 (en) * | 1998-09-04 | 2000-03-16 | Maejima, Fumio | Incinerator for removing noxious substances |
AU744063B2 (en) * | 1998-09-04 | 2002-02-14 | Maejima, Fumio | Incinerator for removing noxious substances |
KR100594699B1 (en) * | 1998-09-04 | 2006-07-03 | 마에지마 후미오 | Incinerator for removing noxious substances |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101417233B1 (en) | Method for incinerating waste by two-stage swirling flow fluidized bed incinerator | |
US3482533A (en) | Incinerators | |
CN108730990A (en) | Utilize the hybrid burner of the thermal decomposition of water and burning air | |
US3645218A (en) | Solid waste incinerator | |
JPH02157511A (en) | Incinerating device | |
JP3151271U (en) | Dry biofuel powder combustion furnace | |
US5727482A (en) | Suspended vortex-cyclone combustion zone for waste material incineration and energy production | |
KR200291644Y1 (en) | a circulation of smoke simplicity incinerator | |
US3791319A (en) | Incinerator | |
CN208652578U (en) | Municipal refuse apparatus for continuous treatment | |
JP2006200768A (en) | Incinerator | |
JP4618580B2 (en) | Combustion furnace | |
US4246850A (en) | Incinerator | |
JP2016023912A (en) | High-temperature exhaust gas purifier, high-temperature exhaust gas generation furnace system, and high-temperature exhaust gas purification method | |
WO2011074364A1 (en) | Combustion device for solid fuel | |
JPS59205517A (en) | Waste incinerator | |
JPH0596729U (en) | Incinerator | |
KR100198734B1 (en) | Dust collector of the incinerator | |
JP3790979B2 (en) | Toxic substance removal incinerator | |
JP4010538B2 (en) | Incinerator | |
KR102069303B1 (en) | Incinerator apparatus | |
KR19990010083A (en) | Industrial waste incineration method and device | |
KR102198134B1 (en) | Combustion structure for hydrogen-incinerator | |
JP3163547B2 (en) | Swirling sand bed type fluidized-bed furnace | |
JP3107544B2 (en) | Swirl combustion furnace |