JPH07248104A - Incinerator for solid waste - Google Patents

Incinerator for solid waste

Info

Publication number
JPH07248104A
JPH07248104A JP4226694A JP4226694A JPH07248104A JP H07248104 A JPH07248104 A JP H07248104A JP 4226694 A JP4226694 A JP 4226694A JP 4226694 A JP4226694 A JP 4226694A JP H07248104 A JPH07248104 A JP H07248104A
Authority
JP
Japan
Prior art keywords
grate
furnace
incinerator
great
dust
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.)
Withdrawn
Application number
JP4226694A
Other languages
Japanese (ja)
Inventor
Masayasu Sakai
正康 坂井
Kunihisa Fujiwara
邦久 藤原
Yoshimine Jiyafuku
良峰 蛇蝮
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP4226694A priority Critical patent/JPH07248104A/en
Publication of JPH07248104A publication Critical patent/JPH07248104A/en
Withdrawn legal-status Critical Current

Links

Abstract

PURPOSE:To provide an incinerator for solid waste, wherein the efficiency of incineration is good and the discharge of an unburnt part of the solid waste is less. CONSTITUTION:An incinerator is formed of two steps of grate furnaces 1A, 1B and a shaft furnace 22 which is provided in array subsequently to the grate furnaces. Each of the grate furnaces 1A, 1B has grates wherein a moving grate and a stationary grate are alternately arranged, and vent means. The shaft furnace 22 located subsequently to the grate furnaces has vent means 23, and ash push-out plate 25 and a damper 26 for discharging burnt ashes while shutting off communication between the inside and the outside of the shaft furnace.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は産業廃棄物や都市ゴミ等
の固形廃棄物の焼却装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an incinerator for solid waste such as industrial waste and municipal waste.

【0002】[0002]

【従来の技術】産業廃棄物、都市ゴミを焼却処理した場
合、焼却灰の外に普通数%の未燃分が残渣として残る
が、ゴミ量の増加に伴ってこれ等残渣も急増しており、
燃焼効率の高い焼却炉が切望されている。図3は一般的
な固形廃棄物焼却システムの概要を示したものである。
この焼却システムについて説明すると、トラック13等
で運ばれて来たゴミaは一旦ゴミピット8内に貯留され
た後、ゴミクレーン11によってホッパ9内に投入され
フィーダ10を介して焼却炉内に適量づつ供給される。
2. Description of the Related Art When industrial waste and municipal waste are incinerated, a few percent of unburned matter usually remains as a residue outside the incinerated ash, but these residues are rapidly increasing as the amount of waste increases. ,
An incinerator with high combustion efficiency is earnestly desired. FIG. 3 shows an outline of a general solid waste incineration system.
Explaining this incineration system, the garbage a transported by the truck 13 or the like is once stored in the garbage pit 8 and then put into the hopper 9 by the garbage crane 11 and is put into the incinerator via the feeder 10 in an appropriate amount. Supplied.

【0003】図3はグレート炉1a,1b,1cを3段
に配置した従来の焼却炉を示しており、供給されてグレ
ート2a,2b,2c上に堆積したゴミaに対して通気
装置3a,3b,3cよりそれぞれ空気が供給され、こ
れによりゴミaは焼却される。この際各グレート上のゴ
ミaは自動的に押出され(構造の詳細は省略する)、前
段側から後段側に流れる間に焼却されて行く。
FIG. 3 shows a conventional incinerator in which the great furnaces 1a, 1b, 1c are arranged in three stages, and the ventilation device 3a, for the dust a supplied and accumulated on the greats 2a, 2b, 2c. Air is supplied from 3b and 3c, respectively, whereby the dust a is incinerated. At this time, the dust a on each grate is automatically extruded (details of the structure are omitted) and incinerated while flowing from the front stage side to the rear stage side.

【0004】こうして、焼却中に発生した燃焼ガスcは
炉出口7より煙道7aを通り空気予熱器14に導かれて
後記するように空気と熱交換された後、有害ガス除去装
置、電気集塵機(図示せず)等を経て外部に排出され、
また、各グレート炉1a,1b,1cから出た焼却灰b
及び未燃分は灰排出口から直接灰押出し装置17に集め
られ、次いで灰ピット18内に貯留された後、適宜、外
部に排出・処理される。
Thus, the combustion gas c generated during incineration passes through the flue 7a from the furnace outlet 7 and is guided to the air preheater 14 where it is heat-exchanged with air as described later, and thereafter, a harmful gas removing device and an electrostatic precipitator are used. (Not shown), etc.
In addition, incineration ash b emitted from each great furnace 1a, 1b, 1c
The unburned component and the unburned component are directly collected from the ash discharge port to the ash extrusion device 17, then stored in the ash pit 18, and then appropriately discharged and treated to the outside.

【0005】なお、送風機6によって供給される燃焼用
空気は燃焼効率を高めるため、その一部が空気予熱器1
4に導かれ適温に昇温されたのち、通気路5を経てそれ
ぞれ各通気装置3a,3b,3cより供給される。な
お、前記において、通気装置3a,3b,3cより供給
するのは空気のほか酸素及びこれらに適宜添加する水蒸
気などがある。
The combustion air supplied by the blower 6 has a part thereof in order to improve the combustion efficiency.
After being led to 4 and heated to an appropriate temperature, they are supplied from the respective ventilation devices 3a, 3b, 3c through the ventilation path 5. In the above description, oxygen is supplied from the aeration devices 3a, 3b, 3c in addition to air and oxygen and water vapor appropriately added thereto.

【0006】[0006]

【発明が解決しようとする課題】前述のように、従来の
燃焼炉では、フィーダ10によって供給されたゴミaは
各グレート2a,2b,2c上に堆積された状態で燃焼
しながら前段側から後段側へ流れる。従って各グレート
2a,2b,2c上のゴミaの層厚は前段グレート2a
上で厚かったものが焼却によって最後段グレート2c上
ではかなり薄くなっている。
As described above, in the conventional combustion furnace, the dust a supplied by the feeder 10 is combusted in a state of being deposited on each of the grate 2a, 2b, 2c, and is burned from the front stage side to the rear stage side. Flowing to the side. Therefore, the layer thickness of the dust a on each of the greats 2a, 2b, 2c is equal to
The thing that was thick above has become considerably thin on the last stage Great 2c due to incineration.

【0007】一方、各通気装置3a,3b,3cより供
給された空気は各グレートの複数の通気口からゴミaの
層内へ流れ、層内を分散しながら上方へ流れて吹き抜け
るが、この際、層が厚いほど層全体への空気の分散が良
く、分散が良いほどゴミは平均して良く燃焼する。
On the other hand, the air supplied from each of the ventilation devices 3a, 3b, 3c flows into the layer of the dust a from the plurality of ventilation holes of each grate, and flows upward while dispersing in the layer. The thicker the layer, the better the air distribution throughout the layer, and the better the dispersion, the better the dust burns on average.

【0008】ところが従来の炉では最後段グレート2c
上のゴミ層厚は燃焼に伴ってどうしても薄くなってしま
うので、供給された空気はゴミ層内で良く分散すること
なく一部から上方へ吹き抜けてしまい、このためゴミの
燃焼が偏って行われるようになり、未燃分が多く発生す
るという欠点があった。本発明は、燃焼効率が良く、未
燃分排出の少ない固形廃棄物の焼却装置を提供すること
を課題としている。
However, in the conventional furnace, the last stage grate 2c
Since the upper dust layer thickness inevitably becomes thinner with combustion, the supplied air does not disperse well in the dust layer and blows upward from a part, which causes uneven combustion of dust. As a result, there is a drawback that a large amount of unburned matter is generated. It is an object of the present invention to provide an incinerator for solid waste, which has good combustion efficiency and small discharge of unburned components.

【0009】[0009]

【課題を解決するための手段】本発明は前記課題を解決
するため、移動グレートと固定グレートが交互に配置さ
れたグレート及び通気装置を備えた複数のグレート炉、
及びそのグレート炉の後に配設され、通気装置と、灰押
出し板と、炉内外の連通を遮断しつゝ焼却灰を排出する
ダンパとを備えたシャフト炉を有する構成の固形廃棄物
の焼却装置を提供する。
In order to solve the above-mentioned problems, the present invention provides a plurality of grate furnaces equipped with a grate in which a moving grate and a fixed grate are alternately arranged, and a ventilation device,
And a solid waste incinerator having a shaft furnace disposed after the great furnace and having a ventilation device, an ash extruding plate, and a damper that cuts off communication between the inside and outside of the furnace and discharges incinerated ash. I will provide a.

【0010】本発明による焼却装置で採用する通気装置
としては特に限定はなく、従来の焼却装置における通気
装置と同様、空気のほか酸素及びこれらに適宜添加する
水蒸気等を供給するものであってよい。
There is no particular limitation on the ventilator used in the incinerator according to the present invention, and it may supply oxygen as well as oxygen and steam appropriately added thereto, as in the ventilator in the conventional incinerator. .

【0011】また、本発明による焼却装置で採用するダ
ンパとしては、複数の開閉扉を備えそれを交互に開閉し
て焼却灰を通過させて排出するが炉内外のガスの流出・
入を遮断する構成のもの等を採用してよい。
Further, the damper employed in the incinerator according to the present invention is provided with a plurality of opening / closing doors and alternately opened and closed to allow the incineration ash to pass therethrough and to be discharged.
It is also possible to adopt a structure that shuts off the entry.

【0012】[0012]

【作用】本発明による固形廃棄物の焼却装置は前記した
構成を有しているので、フィーダ等を介して焼却装置内
に次々に送り込まれたゴミ等の固形廃棄物はまず、前段
に配設された複数のグレート炉のグレート上に所定の層
厚に堆積された状態で焼却されながら移動グレートによ
り順次下流へ送り出される。こうして前段グレート炉の
最後のグレート上に残置している未燃ゴミは次いで後段
に配設されたシャフト炉内に送り込まれる。
Since the solid waste incinerator according to the present invention has the above-mentioned structure, the solid waste such as dust sent one after another into the incinerator through the feeder or the like is first arranged in the preceding stage. While being incinerated in a state of being deposited on the grate of the plurality of grate furnaces having a predetermined layer thickness, it is sequentially sent out to the downstream by the moving grate. In this way, the unburned dust left on the last grate of the former stage grate furnace is then fed into the shaft furnace arranged in the latter stage.

【0013】シャフト炉内では、通気装置から送り込ま
れる空気等によって未燃分の焼却が行われ、焼却灰は灰
押出し板によって炉内から押し出された後、ダンパによ
って炉内外の連通を遮断しつゝシャフト炉の外へ排出さ
れる。こうして、本発明による焼却装置ではグレート炉
とシャフト炉の結合により、未燃分排出が少ない状態で
効率良く固形廃棄物を焼却することができる。
In the shaft furnace, the unburned components are incinerated by the air sent from the ventilation device, the incinerated ash is pushed out of the furnace by the ash push plate, and then the damper is used to block the communication between the inside and outside of the furnace.ゝ Discharged outside the shaft furnace. Thus, in the incinerator according to the present invention, the solid waste can be efficiently incinerated by connecting the great furnace and the shaft furnace with a small amount of unburned components discharged.

【0014】[0014]

【実施例】以下本発明による焼却装置を図示した実施例
によって具体的に説明する。図1は本発明の一実施例に
よる焼却装置の主要構成を示したものである。なお、焼
却システムの全体構成は前記図3と同様なのでここでは
図示しない。
EXAMPLES The incinerator according to the present invention will be specifically described below with reference to the illustrated examples. FIG. 1 shows the main configuration of an incinerator according to an embodiment of the present invention. The overall structure of the incineration system is the same as that shown in FIG. 3 and is not shown here.

【0015】図1に示すように、本実施例の焼却装置は
前段側に2段のグレート炉1A,1Bが、後段側にシャ
フト炉22が接続・設置された構成になっている。グレ
ート炉1A,1Bはそれぞれグレート2A,2Bを備え
ている。
As shown in FIG. 1, the incinerator of this embodiment has a structure in which two stages of great furnaces 1A and 1B are connected to the front side and a shaft furnace 22 is connected to the rear side. Great furnaces 1A and 1B are provided with greats 2A and 2B, respectively.

【0016】その詳細を図2に示すように、各グレート
は、複数の移動グレート2’と固定グレート2''とが交
互に配置されていて、移動グレート2’は架台19上の
車輪20に支持された駆動台18を駆動することによっ
て矢印方向に往復移動し、これによってグレート上に堆
積したゴミaを下流側(矢印方向)へ移動させ、滑り台
21を介して次のグレート炉またはシャフト炉へ送り出
すようになっている。
As shown in FIG. 2 in detail, a plurality of moving grate 2'and fixed grate 2 "are alternately arranged in each grate, and the moving grate 2'is attached to the wheels 20 on the pedestal 19. By driving the supported drive base 18, the reciprocating movement in the direction of the arrow moves the dust a accumulated on the grate to the downstream side (direction of the arrow), and the next great furnace or shaft furnace moves through the slide 21. It is designed to be sent to.

【0017】また、ここでは図示していないが各グレー
ト炉1A,1Bには通気装置(図3に示す3a,3b…
…と同様のもの)が配設されていて、移動グレート2’
と固定グレート2''間に設けた通気口よりゴミaの層内
に空気を供給するようになっている。
Although not shown here, a ventilator (3a, 3b ... Shown in FIG. 3) is provided in each of the great furnaces 1A, 1B.
(Similar to ...) is provided, and the movement great 2 '
Air is supplied into the layer of the dust a through a vent provided between the fixed grate 2 '' and the fixed grate 2 ''.

【0018】一方、シャフト炉22は最終段グレート炉
1Bに接続して設置され、別途通気装置(図示していな
い)に通ずる通気口23、シャフト炉22内を落下する
未燃ゴミや燃焼灰等を遮蔽して空気の吹込みを助けるた
めの遮蔽板24、炉底に留った燃焼灰等を押出すための
灰押出し板25、複数の開閉扉を交互に開閉して焼却灰
を通過・排出すると共に炉内外のガスの流入・流出を遮
断するためのダンパ26などを備えている。
On the other hand, the shaft furnace 22 is installed by being connected to the final stage great furnace 1B, and a ventilation port 23 communicating with another ventilation device (not shown), unburned dust and combustion ash falling in the shaft furnace 22. A shield plate 24 for shielding air to help blow air, an ash extruding plate 25 for extruding combustion ash and the like remaining on the furnace bottom, and a plurality of open / close doors are alternately opened and closed to pass incinerated ash. A damper 26 and the like for discharging and blocking the inflow and outflow of gas inside and outside the furnace are provided.

【0019】以下に、本実施例の焼却装置の作用を説明
する。ホッパ9内に投入されたゴミaは、フィーダ10
を介して次々に炉内に送り込まれ、まずグレート炉1A
のグレート2A上に所定の層高に堆積された後、別途着
火装置によって着火され、また通気装置3a,3b……
より空気が供給されて燃焼が始まる。
The operation of the incinerator of this embodiment will be described below. The dust a thrown into the hopper 9 is fed to the feeder 10
It is sent into the furnace one after another via the
After being deposited at a predetermined layer height on the Great 2A, it is separately ignited by an igniter, and the ventilation devices 3a, 3b ...
More air is supplied and combustion begins.

【0020】同時に移動グレート2' が駆動されて、グ
レート2A上のゴミaは燃焼しながら下流側へ移動し、
次段のグレート炉1Bに送り込まれてグレート2B上に
堆積され、同様に燃焼しながら下流側へ流されて未燃分
が後段のシャフト炉22内へ送り込まれる。こうしてシ
ャフト炉22内に堆積された未燃ゴミに対して通気口2
3より空気が供給され、焼却が行われる。
At the same time, the moving grate 2'is driven so that the dust a on the grate 2A moves to the downstream side while burning.
It is sent to the next-stage great furnace 1B and deposited on the great 2B, and likewise burns while flowing to the downstream side, and unburned components are sent into the shaft furnace 22 at the latter stage. The vent 2 is provided for the unburned dust thus accumulated in the shaft furnace 22.
Air is supplied from 3 and incineration is performed.

【0021】上記ゴミ燃焼中に発生する燃焼ガスcは、
図3に示したように炉出口7を通り空気予熱器14に導
かれて、熱交換され、燃焼効率を高めるための供給空気
の予熱に利用され、また各グレート炉1A,1B内及び
シャフト炉22内に発生する燃焼灰bは、図3に示した
ように未燃ゴミと一緒に灰出コンベア16を介して或い
は直接灰押出し装置17に集められ、灰ピット18内に
貯留ののち、適宜外部に排出・処理される。
The combustion gas c generated during the burning of the dust is
As shown in FIG. 3, it is guided to the air preheater 14 through the furnace outlet 7, is heat-exchanged, and is used for preheating the supply air for increasing the combustion efficiency, and also in each of the great furnaces 1A and 1B and the shaft furnace. As shown in FIG. 3, the combustion ash b generated in 22 is collected together with the unburned dust through the ash discharge conveyor 16 or directly in the ash extrusion device 17, is stored in the ash pit 18, and is appropriately stored. It is discharged and processed outside.

【0022】このような燃焼過程において、前段炉(グ
レート炉)内のゴミの層厚は最初のグレート2A上はも
とより、次のグレート2B上でも比較的大きいので、層
内における供給空気の分散は良好で、このため燃焼は効
率的かつ平均的に行われ、また、シャフト炉22内で
も、遮蔽板24及びダンパ26の作用に基づく良好な空
気の供給と相まって燃焼は効率的かつ平均的に行われる
ようになり、その結果未燃ゴミの発生が非常に少なくな
る。
In such a combustion process, the layer thickness of dust in the pre-stage furnace (Great furnace) is relatively large not only on the first Great 2A but also on the second Great 2B, so that the dispersion of the supply air in the layer is Good, and therefore the combustion is efficient and average, and in the shaft furnace 22 the combustion is also efficient and average in combination with the good air supply due to the action of the shielding plate 24 and the damper 26. As a result, the generation of unburned dust is greatly reduced.

【0023】以上、本発明を図示した実施例に基づいて
具体的に説明したが、本発明がこれらの実施例に限定さ
れず特許請求の範囲に示す本発明の範囲内で、その形
状、構造に種々の変更を加えてよいことはいうまでもな
い。例えば、前記実施例では2段のグレート炉1A,1
Bを採用しているが、3段以上のグレート炉で構成して
もよい。
The present invention has been specifically described above based on the illustrated embodiments, but the present invention is not limited to these embodiments, and the shape and structure thereof are within the scope of the present invention shown in the claims. It goes without saying that various changes may be added to the. For example, in the above embodiment, the two-stage great furnaces 1A, 1
Although B is adopted, it may be composed of three or more stages of great furnaces.

【0024】[0024]

【発明の効果】以上、詳細に説明したように、本発明の
焼却装置によると、焼却炉内に送り込まれた固形廃棄物
は、まず、前段に配設された複数のグレート炉のグレー
ト上に堆積された状態で効率的かつ平均的に焼却され、
次いでその後に残った未燃ゴミは後段に配設されたシャ
フト炉内に送り込まれて同炉内で効率良く焼却されるよ
うになり、その結果、焼却後の未燃ゴミの量が非常に少
なくなるという効果がある。
As described in detail above, according to the incinerator of the present invention, the solid waste sent into the incinerator is first placed on the grate of the plurality of great furnaces arranged in the preceding stage. Efficiently and averagely incinerated as deposited,
Then, the unburned dust remaining after that is sent into the shaft furnace arranged in the latter stage and efficiently incinerated in the same furnace, resulting in a very small amount of unburned dust after incineration. There is an effect that.

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

【図1】本発明の一実施例に係る焼却装置の構成図。FIG. 1 is a configuration diagram of an incinerator according to an embodiment of the present invention.

【図2】図1に示した焼却装置におけるグレートの要部
詳細図。
FIG. 2 is a detailed view of essential parts of the grate in the incinerator shown in FIG.

【図3】本発明による焼却装置を適用する一般的な固形
廃棄物焼却システムを示す機器配置図。
FIG. 3 is an equipment layout diagram showing a general solid waste incineration system to which the incinerator according to the present invention is applied.

【符号の説明】[Explanation of symbols]

1A,1B グレート炉 2A,2B グレート 2’ 移動グレート 2'' 固定グレート 9 ホッパ 10 フィーダ 22 シャフト炉 23 通気口 24 遮蔽板 25 灰押出し板 26 ダンパ 1A, 1B Great furnace 2A, 2B Great 2'Movement great 2 '' Fixed great 9 Hopper 10 Feeder 22 Shaft furnace 23 Vent hole 24 Shield plate 25 Ash extruded plate 26 Damper

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 移動グレートと固定グレートが交互に配
置されたグレート及び通気装置を備えた複数のグレート
炉、及び同グレート炉の後に配設され、通気装置と、灰
押出し板と、炉内外の連通を遮断しつゝ焼却灰を排出す
るダンパとを備えたシャフト炉を有することを特徴とす
る固形廃棄物焼却装置。
1. A plurality of grate furnaces having a grate and a ventilation device in which a moving grate and a fixed grate are alternately arranged, and a plurality of grate furnaces disposed after the grate furnace, the ventilation device, the ash extrusion plate, and the inside and outside of the furnace. A solid waste incinerator characterized by having a shaft furnace equipped with a damper that cuts off communication and discharges incineration ash.
JP4226694A 1994-03-14 1994-03-14 Incinerator for solid waste Withdrawn JPH07248104A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4226694A JPH07248104A (en) 1994-03-14 1994-03-14 Incinerator for solid waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4226694A JPH07248104A (en) 1994-03-14 1994-03-14 Incinerator for solid waste

Publications (1)

Publication Number Publication Date
JPH07248104A true JPH07248104A (en) 1995-09-26

Family

ID=12631242

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4226694A Withdrawn JPH07248104A (en) 1994-03-14 1994-03-14 Incinerator for solid waste

Country Status (1)

Country Link
JP (1) JPH07248104A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011163652A (en) * 2010-02-09 2011-08-25 Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd Stoker type incinerator and method of operating the same
CN107664307A (en) * 2016-07-29 2018-02-06 北京航天动力研究所 Alternating movement formula fire grate garbage incinerator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011163652A (en) * 2010-02-09 2011-08-25 Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd Stoker type incinerator and method of operating the same
CN107664307A (en) * 2016-07-29 2018-02-06 北京航天动力研究所 Alternating movement formula fire grate garbage incinerator
CN107664307B (en) * 2016-07-29 2024-02-09 北京航天动力研究所 Alternately moving fire grate garbage incinerator

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