JPH10325519A - Incinerator of waste - Google Patents

Incinerator of waste

Info

Publication number
JPH10325519A
JPH10325519A JP13312497A JP13312497A JPH10325519A JP H10325519 A JPH10325519 A JP H10325519A JP 13312497 A JP13312497 A JP 13312497A JP 13312497 A JP13312497 A JP 13312497A JP H10325519 A JPH10325519 A JP H10325519A
Authority
JP
Japan
Prior art keywords
combustion chamber
incineration
inner cylinder
incinerator
primary combustion
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.)
Granted
Application number
JP13312497A
Other languages
Japanese (ja)
Other versions
JP3676033B2 (en
Inventor
Hideaki Ota
英明 太田
Shoichi Kai
昭一 甲斐
Masaru Nakajima
中島  勝
Hisao Yamamoto
久夫 山本
Masayasu Sakai
正康 坂井
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 JP13312497A priority Critical patent/JP3676033B2/en
Publication of JPH10325519A publication Critical patent/JPH10325519A/en
Application granted granted Critical
Publication of JP3676033B2 publication Critical patent/JP3676033B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Incineration Of Waste (AREA)

Abstract

PROBLEM TO BE SOLVED: To achieve a higher incineration efficiency while shortening incineration time by supplying a combustion gas evenly to wastes to be incinerated in an incinerator for the wastes. SOLUTION: A fire grating 12 is provided in a heat resisting body 11 of an incinerator. A primary combustion chamber 13 and a secondary combustion chamber 14, upper and lower zones, are formed and the primary combustion chamber 13 is provided with a feeding port 15 for wastes. An invertedcone shaped incineration, inner cylinder 31 is rotatably supported in the primary combustion chamber 13 with a vertical shaft and a flat agitation blade 36 is mounted in the inner circumferential surface of the incineration inner cylinder 31 along the vertical direction while a flat fixed blade 37 is provided along the vertical direction At the center part of rotation of the incineration inner cylinder 31 along the vertical direction.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、家庭の一般ごみや
生ごみ、食堂の生ごみ、あるいは紙おむつなどの廃棄物
を燃焼して処理する廃棄物の焼却炉に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste incinerator for burning and processing waste such as household garbage and garbage, kitchen garbage, and disposable diapers.

【0002】[0002]

【従来の技術】図3に従来の廃棄物の焼却炉の概略断面
を示す。
2. Description of the Related Art FIG. 3 shows a schematic cross section of a conventional waste incinerator.

【0003】従来の廃棄物の焼却炉において、図3に示
すように、焼却炉本体101は耐火材あるいはセラミック
多孔体などによって壁面が形成されており、火格子102
が取付けられることで、上部の一次燃焼室103と下部の
二次燃焼室104に区画されている。この一次燃焼室103の
上部には廃棄物としてのごみ201を投入する投入口105が
形成され、蓋106によって開閉自在となっている。二次
燃焼室104の一方には燃焼ガス導入路107が接続され、こ
の燃焼ガス導入路107にはバーナ108が装着されている。
このバーナ108は燃焼用空気と燃料ガスの混合物(燃焼
ガス)を二次燃焼室104に直接噴射するものである。そ
して、この燃焼ガス導入路107の基端部には、一端部が
一次燃焼室103に連通した循環通路109の他端部が連通し
ている。また、二次燃焼室104の他方には排気ガス排出
路110が接続され、この排気ガス排出路110の先端部は煙
突111に接続されている。
In a conventional waste incinerator, as shown in FIG. 3, a wall of an incinerator main body 101 is formed of a refractory material or a porous ceramic body, and a fire grate 102 is provided.
Is divided into an upper primary combustion chamber 103 and a lower secondary combustion chamber 104. In the upper part of the primary combustion chamber 103, there is formed an inlet 105 into which refuse 201 as waste is injected, and the opening 106 can be opened and closed by a lid 106. A combustion gas introduction passage 107 is connected to one of the secondary combustion chambers 104, and a burner 108 is mounted on the combustion gas introduction passage 107.
The burner 108 directly injects a mixture of combustion air and fuel gas (combustion gas) into the secondary combustion chamber 104. The other end of the circulation passage 109 whose one end communicates with the primary combustion chamber 103 communicates with the base end of the combustion gas introduction passage 107. Further, an exhaust gas exhaust passage 110 is connected to the other end of the secondary combustion chamber 104, and a tip end of the exhaust gas exhaust passage 110 is connected to a chimney 111.

【0004】従って、バーナ108は燃焼ガスを燃焼ガス
導入路107を通して二次燃焼室104に噴射しており、この
二次燃焼室104に高温場を形成すると共に、一部の燃焼
ガスを火格子102を通って一次燃焼室103に流動し、投入
口105からこの一次燃焼室103に投入されたごみ201を部
分燃焼ガス化する。この部分燃焼ガスは、バーナ108か
らの燃焼ガスの噴射に伴う負圧の発生によって循環通路
109に吸引され、この循環通路109及び燃焼ガス導入路10
7を介してバーナ108に燃焼用空気と共に吸引され、二次
燃焼室104の高温場で完全に焼却された後、排気ガス排
出路110を通して煙突111から外部に排出される。なお、
バーナ108で燃焼される燃焼用空気と燃料ガスとの流量
比は一定であり、また、二次燃焼室104の温度は800
〜1000℃、残酸素濃度は5〜10%に設定されてい
る。
[0004] Accordingly, the burner 108 injects the combustion gas into the secondary combustion chamber 104 through the combustion gas introduction path 107, and forms a high-temperature field in the secondary combustion chamber 104 and transfers a part of the combustion gas to the grate. It flows into the primary combustion chamber 103 through 102, and the refuse 201 introduced into the primary combustion chamber 103 from the input port 105 is partially burned into gas. This partial combustion gas is generated in the circulation passage by the generation of a negative pressure accompanying the injection of the combustion gas from the burner 108.
The circulation passage 109 and the combustion gas introduction passage 10
The air is sucked into the burner 108 through the burner 108 together with the combustion air, is completely incinerated in the high-temperature field of the secondary combustion chamber 104, and is then discharged to the outside from the chimney 111 through the exhaust gas discharge passage 110. In addition,
The flow rate ratio between the combustion air and fuel gas burned in the burner 108 is constant, and the temperature of the secondary combustion chamber 104 is 800
10001000 ° C., and the residual oxygen concentration is set at 5-10%.

【0005】このように二次燃焼室104にて、高温度、
低酸素濃度の燃焼ガスのうち、30%程度をガス化剤と
して使用することで、前述した作用により、燃焼速度の
低い高水分低カロリーごみを安定して処理できると共
に、燃焼速度の高い廃プラスチックごみの熱分解速度を
抑制し、焼却物としてのごみの性状に関わりなく、この
ごみを安定して部分燃焼ガス化できる。
As described above, in the secondary combustion chamber 104, high temperature,
By using about 30% of the combustion gas having a low oxygen concentration as a gasifying agent, the above-mentioned operation enables stable treatment of high-moisture and low-calorie refuse having a low combustion rate and waste plastic having a high combustion rate. The thermal decomposition rate of the refuse can be suppressed, and this refuse can be stably partially gasified regardless of the properties of the refuse as incineration.

【0006】[0006]

【発明が解決しようとする課題】ところが、上述した従
来の廃棄物の焼却炉にあっては、投入口105から一次燃
焼室103内に投入されたのごみ201は、火格子102の上に
厚積みされた状態、即ち、固定層を形成するために反応
の進行と共に層内下部の燃焼層、中間の部分燃焼ガス化
層、層内上部の水分蒸発層の各反応層が断面方向に不均
一となって、所謂、片燃え現象を起こし易いという問題
がある。そして、この片燃え現象が成長すると、層内の
高さ方向に吹き抜けを起こし、燃焼ガスが層内断面方向
に均等に供給されなくなってしまう。また、ごみの中で
も、紙おむつや生ごみなど水分の含有率が90%を占め
るような高含水性で高断熱性を有する難燃性のごみは、
燃え切り時間が一般のごみに比べて極端に長くなってし
まうという問題がある。
However, in the above-mentioned conventional waste incinerator, the refuse 201 injected into the primary combustion chamber 103 from the inlet 105 is thick on the grate 102. In the stacked state, that is, as the reaction progresses to form a fixed layer, the reaction layers of the lower combustion layer, the middle partial combustion gasification layer, and the upper water evaporation layer in the layer become uneven in the cross-sectional direction as the reaction proceeds. Thus, there is a problem that a so-called one-sided burning phenomenon easily occurs. When the one-sided burning phenomenon grows, blow-through occurs in the height direction in the layer, and the combustion gas is not evenly supplied in the cross-sectional direction in the layer. In addition, among the refuse, flame-retardant refuse having high water content and high heat insulation such as disposable diapers and garbage having a water content of 90%,
There is a problem that the burn-out time becomes extremely long compared to general waste.

【0007】本発明はこのような問題点を解決するもの
であり、焼却する廃棄物に対して均一に燃焼ガスを供給
して焼却効率の向上を図ると共に焼却時間の短縮を図っ
た廃棄物の焼却炉を提供することを目的とする。
The present invention has been made to solve the above-mentioned problems, and a uniform combustion gas is supplied to the waste to be incinerated to improve the incineration efficiency and reduce the incineration time. It aims to provide an incinerator.

【0008】[0008]

【課題を解決するための手段】上述の目的を達成するた
めの本発明の廃棄物の焼却炉は、耐火性の焼却炉内に火
格子を設けることで、上下に区画された一次燃焼室及び
二次燃焼室を形成し、前記一次燃焼室に廃棄物の投入口
が設けられた廃棄物の焼却炉において、前記一次燃焼室
内に逆円錐台形状をなす焼却内筒が鉛直軸をもって回転
自在に支持され、該焼却内筒の内周面に上下方向に沿っ
た平板状の攪拌翼が装着される一方、該焼却内筒の回転
中心部に鉛直方向に沿った平板状の固定翼が設けられた
ことを特徴とするものである。
The waste incinerator according to the present invention for achieving the above-mentioned object has a grate in a refractory incinerator, whereby a vertically divided primary combustion chamber and In a waste incinerator in which a secondary combustion chamber is formed and an inlet for the waste is provided in the primary combustion chamber, an inverted frustoconical inner cylinder in the primary combustion chamber is rotatable with a vertical axis. Supported are flat plate-like agitating blades along the vertical direction on the inner peripheral surface of the incineration inner cylinder, and flat plate-like fixed blades along the vertical direction are provided at the center of rotation of the incineration inner cylinder. It is characterized by having.

【0009】[0009]

【発明の実施の形態】以下、図面に基づいて本発明の実
施の形態を詳細に説明する。
Embodiments of the present invention will be described below in detail with reference to the drawings.

【0010】図1に本発明の一実施形態に係る廃棄物の
焼却炉を表す概略断面、図2に焼却内筒の平面視を示
す。
FIG. 1 is a schematic cross section showing a waste incinerator according to one embodiment of the present invention, and FIG. 2 is a plan view of an incineration inner cylinder.

【0011】本実施形態の廃棄物の焼却炉において、図
1及び図2に示すように、焼却炉本体11は耐火材ある
いはセラミック多孔体などによってその壁面が形成され
ており、内部に水平な平板円盤状をなす火格子12が取
付けられることで、上部の一次燃焼室13と下部の二次
燃焼室14とに区画されている。そして、この一次燃焼
室13の上部には廃棄物としてのごみ51を投入する投
入口15が形成され、この投入口15は蓋16によって
開閉自在となっている。また、二次燃焼室14の一側に
は燃焼ガス導入路17が接続され、この燃焼ガス導入路
17にはバーナ18が装着されている。このバーナ18
は燃焼用空気と燃料ガスの混合物(燃焼ガス)を二次燃
焼室14に直接噴射するものである。そして、この燃焼
ガス導入路17の基端部には、一端部が一次燃焼室13
に連通した循環通路19の他端部が連通している。一
方、二次燃焼室14の他側には排気ガス排出路20が接
続され、この排気ガス排出路20の先端部は煙突21に
接続されている。
In the waste incinerator according to the present embodiment, as shown in FIGS. 1 and 2, the incinerator body 11 has a wall surface formed of a refractory material or a porous ceramic body, and has a horizontal flat plate inside. The disk-shaped grate 12 is attached so that it is partitioned into an upper primary combustion chamber 13 and a lower secondary combustion chamber 14. In the upper part of the primary combustion chamber 13, there is formed an inlet 15 into which refuse 51 as waste is charged, and the inlet 15 can be opened and closed by a lid 16. Further, a combustion gas introduction passage 17 is connected to one side of the secondary combustion chamber 14, and a burner 18 is mounted on the combustion gas introduction passage 17. This burner 18
Is for directly injecting a mixture of combustion air and fuel gas (combustion gas) into the secondary combustion chamber 14. At the base end of the combustion gas introduction passage 17, one end is connected to the primary combustion chamber 13.
The other end of the circulation passage 19 which communicates with the communication port is connected. On the other hand, an exhaust gas discharge passage 20 is connected to the other side of the secondary combustion chamber 14, and a tip end of the exhaust gas discharge passage 20 is connected to a chimney 21.

【0012】また、一次燃焼室13内には焼却内筒31
が位置しており、この焼却内筒31の上部には支持棒3
2を介して駆動軸33が連結され、この駆動軸33は焼
却炉本体11の上部に軸シール34によって吊下げ回転
自在に支持されている。そして、この駆動軸33の上端
部には駆動モータ35の図示しない出力軸が固結されて
いる。従って、この駆動モータ35によって駆動軸33
を回転駆動すると、一次燃焼室13にて焼却内筒31を
鉛直軸線をもって回転することができる。
In the primary combustion chamber 13, an incineration inner cylinder 31 is provided.
Is located at the top of the incineration inner cylinder 31.
The drive shaft 33 is connected to the incinerator body 11 via a shaft seal 34 so as to be suspended and rotatable. An output shaft (not shown) of the drive motor 35 is fixed to an upper end of the drive shaft 33. Therefore, the drive shaft 33 is driven by the drive motor 35.
, The incineration inner cylinder 31 can be rotated about the vertical axis in the primary combustion chamber 13.

【0013】この焼却内筒31は下部に対して上部の径
が大きい逆円錐台形状をなしており、内周面には上下方
向に沿った平板状の攪拌翼36が周方向等間隔で4個固
着されている。また、焼却内筒31内にはその回転中心
部に鉛直方向に沿った平板状の固定翼37が火格子12
から立設されている。また、焼却内筒31の外周下部に
はフランジ部38が形成されており、このフランジ部3
8は焼却炉本体11に形成された円周溝39にガスシー
ル(鋳物砂などの耐熱シール材)40を介して支持され
ており、焼却内筒31と二次燃焼室14との隙間からの
ガスショートパスを防止している。
The incineration inner cylinder 31 has an inverted truncated cone shape having a larger diameter at the upper part than at the lower part. A flat stirring blade 36 along the vertical direction is provided on the inner peripheral surface at equal circumferential intervals. Individually fixed. In the incineration inner cylinder 31, a flat fixed blade 37 extending vertically along the center of rotation is provided with a grate 12.
It is erected from. Further, a flange portion 38 is formed at a lower portion of the outer periphery of the incineration inner cylinder 31.
Numeral 8 is supported in a circumferential groove 39 formed in the incinerator main body 11 via a gas seal (heat-resistant sealing material such as foundry sand) 40, and is provided through a gap between the incineration inner cylinder 31 and the secondary combustion chamber 14. Gas short path is prevented.

【0014】従って、バーナ18は燃焼ガスを燃焼ガス
導入路17を通して二次燃焼室14に噴射しており、こ
の二次燃焼室14に高温場を形成すると共に、一部の燃
焼ガスを火格子12を通って一次燃焼室13に流動す
る。一方、一次燃焼室13の焼却内筒31内には投入口
15からごみ51が投入され、駆動モータ35によって
焼却内筒31が回転することで、ごみ51は各攪拌翼3
6及び固定翼37によって攪拌されている。即ち、焼却
内筒31は1分間に数回転程度の低速で緩やかに回転し
ており、この焼却内筒31の攪拌翼36と火格子12上
のごみ51との間に相対速度が発生し、また、攪拌翼3
6に攪拌されるごみ51と火格子12に固定された固定
翼37との間にも相対速度が発生する。これによってご
み51を層状とせずに掻き乱すこととなる。そのため、
固定層内で発生する片燃えによる燃料不均一や層内の高
さ方向での吹き抜けによるガスショートパスを防止する
ことができ、ごみ51の断面方向に対して均一に燃焼ガ
スを供給できる。
Accordingly, the burner 18 injects the combustion gas into the secondary combustion chamber 14 through the combustion gas introduction passage 17 to form a high-temperature field in the secondary combustion chamber 14 and to transfer a part of the combustion gas to the grate. It flows into the primary combustion chamber 13 through 12. On the other hand, refuse 51 is thrown into the incineration inner cylinder 31 of the primary combustion chamber 13 from the charging port 15, and the incineration inner cylinder 31 is rotated by the drive motor 35, so that the refuse 51 is
6 and the fixed blade 37. That is, the incineration inner cylinder 31 is slowly rotating at a low speed of about several rotations per minute, and a relative speed is generated between the stirring blade 36 of the incineration inner cylinder 31 and the dust 51 on the grate 12, In addition, stirring blade 3
Relative speed is also generated between the refuse 51 agitated at 6 and the fixed wing 37 fixed to the grate 12. As a result, the refuse 51 is disturbed without forming a layer. for that reason,
It is possible to prevent non-uniform fuel due to one-sided combustion generated in the fixed bed and a gas short path due to blow-through in the height direction in the bed, so that the combustion gas can be supplied uniformly to the cross-sectional direction of the refuse 51.

【0015】また、攪拌翼36及び固定翼37によるご
み51の掻き乱し作用により、ごみ51のある程度の水
分蒸発や焼却が進行し、構造強度が低下してごみ51を
解砕することで、被表面積を増大させてごみ51の燃え
切り時間(処理時間)を短縮できる。
[0015] Further, due to the agitating action of the refuse 51 by the stirring blade 36 and the fixed wing 37, a certain amount of water evaporation and incineration of the refuse 51 progress, and the structural strength is reduced, and the refuse 51 is crushed. By increasing the surface area, the burn-out time (processing time) of the refuse 51 can be reduced.

【0016】その後、一次燃焼室13に流動した燃焼ガ
スは、バーナ18からの燃焼ガスの噴射に伴って発生し
た負圧によって循環通路19に吸引され、この循環通路
19及び燃焼ガス導入路17を介してバーナ18に燃焼
用空気と共に吸引され、二次燃焼室14の高温場で完全
に焼却された後、排気ガス排出路20を通して煙突21
から外部に排出される。
Thereafter, the combustion gas flowing into the primary combustion chamber 13 is sucked into the circulation passage 19 by the negative pressure generated by the injection of the combustion gas from the burner 18, and flows through the circulation passage 19 and the combustion gas introduction passage 17. After being sucked into the burner 18 together with the combustion air via the burner 18 and completely incinerated in the high temperature field of the secondary combustion chamber 14,
Is discharged to the outside.

【0017】このように本実施形態の廃棄物の焼却炉に
あっては、一次燃焼室13内に回転自在な焼却内筒31
を設けてこの焼却内筒31に平板状の攪拌翼36を一体
回転可能に取付けると共に、焼却内筒31の中央部に位
置して平板状の固定翼37を火格子12に固定したこと
で、攪拌翼36及び固定翼37と焼却内筒31との間に
相対速度が発生してごみ51を層状とせずに掻き乱し、
ごみ51の断面方向に対して均一に燃焼ガスを供給し、
焼却効率の向上が図れる。
As described above, in the waste incinerator of the present embodiment, the rotatable incineration cylinder 31 is provided in the primary combustion chamber 13.
By attaching a flat stirring blade 36 to the incineration inner cylinder 31 so as to be integrally rotatable, and fixing the flat stationary blade 37 to the grate 12 at the center of the incineration inner cylinder 31, The relative speed is generated between the stirring blades 36 and the fixed blades 37 and the incineration inner cylinder 31, and the dusts 51 are disturbed without being layered,
The combustion gas is uniformly supplied to the cross-sectional direction of the refuse 51,
The incineration efficiency can be improved.

【0018】そして、上述した本実施形態の廃棄物の焼
却炉において、焼却内筒31を下部に対して上部の径が
大きい逆円錐台形状としたことで、火格子12上のごみ
51の燃焼層に供給する燃焼ガス量を断面方向に均一化
し、片燃えを起こし難くすることができ、且つ、焼却内
筒31の下部にいくにしたがって攪拌翼36と固定翼3
7との間隔が短くなって、攪拌作用及び解砕作用が必要
となる主反応域である下層域に効果的にこの攪拌作用及
び解砕作用を与えると共に、駆動モータ35の所要動力
を押さえることができる。
In the above-described waste incinerator of the present embodiment, the incineration inner cylinder 31 has an inverted truncated cone shape in which the diameter of the upper part is larger than that of the lower part, so that the debris 51 on the grate 12 is burned. The amount of combustion gas supplied to the bed can be made uniform in the cross-sectional direction, making it difficult for one-sided burning to occur.
7, the stirring action and the crushing action are effectively given to the lower layer area, which is the main reaction zone where the stirring action and the crushing action are required, and the required power of the drive motor 35 is suppressed. Can be.

【0019】また、上述した本実施形態の廃棄物の焼却
炉において、一次燃焼室13の側壁に平板状の固定翼3
7を取付け、火格子12を回転自在としてこの火格子1
2に平板状の攪拌翼36を固定することも考えられる
が、この構造とすることで下記の問題が発生する。即
ち、通常の焼却炉では、酸化剤としての空気の供給温度
が自然通風式の場合に常温であり、強制通風式の場合に
200〜350℃である。焼却炉では、800〜100
0℃の高温バーナ燃焼ガスを酸化剤として使用してお
り、中心部を攪拌翼とすると、高温の火格子を回転させ
ることとなり、併せて回転駆動部もこの火格子の近傍に
設けることとなり、それぞれ耐熱構造としなければなら
ず、複雑で高価なものとなってしまう。また、中心部を
攪拌翼によって攪拌するよりも、外周部をを攪拌翼によ
って攪拌するほうが、攪拌翼とごみとの相対的に外周移
動距離が長くなり、攪拌効率が高い。
Further, in the waste incinerator according to the above-described embodiment, the flat stationary blades 3 are provided on the side wall of the primary combustion chamber 13.
7 and the grate 12 is made rotatable.
It is conceivable to fix the plate-like stirring blade 36 to 2, but this structure causes the following problems. That is, in a normal incinerator, the supply temperature of air as an oxidizing agent is room temperature in the case of a natural ventilation system, and is 200 to 350 ° C. in the case of a forced ventilation system. 800 to 100 for incinerators
When the high-temperature burner combustion gas of 0 ° C. is used as an oxidizing agent, and the central part is a stirring blade, the high-temperature grate is rotated, and a rotation drive unit is also provided near the grate. Each must have a heat-resistant structure, which is complicated and expensive. In addition, when the center portion is agitated by the stirring blade, the outer peripheral portion is relatively agitated by the agitating blade, so that the distance between the agitating blade and the debris relatively moves around the outer periphery, and the stirring efficiency is higher.

【0020】[0020]

【発明の効果】以上、実施形態において詳細に説明した
ように本発明の廃棄物の焼却炉によれば、焼却炉内に火
格子を設けて上下に区画した一次燃焼室及び二次燃焼室
を形成し、一次燃焼室内に逆円錐台形状をなす焼却内筒
を鉛直軸をもって回転自在に支持し、この焼却内筒の内
周面に上下方向に沿った平板状の攪拌翼を装着する一
方、焼却内筒の回転中心部に鉛直方向に沿った平板状の
固定翼を設けたので、焼却内筒が回転するときに、攪拌
翼と火格子上の廃棄物と固定翼との間に相対速度が生
じ、廃棄物を掻き乱して断面方向に対して均一に燃焼ガ
スを供給することで、焼却効率の向上を図ることができ
ると共に焼却時間の短縮を図ることができる。
As described above in detail in the embodiment, according to the waste incinerator of the present invention, the primary combustion chamber and the secondary combustion chamber divided into upper and lower parts by providing a grate in the incinerator. The incineration inner cylinder having an inverted truncated cone shape is rotatably supported with a vertical axis in the primary combustion chamber, and a plate-like stirring blade along the vertical direction is mounted on the inner peripheral surface of the incineration inner cylinder, A flat stationary blade along the vertical direction is provided at the center of rotation of the incineration inner cylinder, so that when the incineration cylinder rotates, the relative speed between the agitating blade, the waste on the grate, and the fixed blade Is generated and the waste gas is disturbed and the combustion gas is supplied uniformly in the cross-sectional direction, so that the incineration efficiency can be improved and the incineration time can be shortened.

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

【図1】本発明の一実施形態に係る廃棄物の焼却炉を表
す概略断面図である。
FIG. 1 is a schematic sectional view showing a waste incinerator according to one embodiment of the present invention.

【図2】焼却内筒の平面図である。FIG. 2 is a plan view of an incineration inner cylinder.

【図3】従来の廃棄物の焼却炉の概略断面図である。FIG. 3 is a schematic sectional view of a conventional waste incinerator.

【符号の説明】[Explanation of symbols]

11 焼却炉本体 12 火格子 13 一次燃焼室 14 二次燃焼室 15 投入口 18 バーナ 19 循環通路 31 焼却内筒 33 駆動軸 35 駆動モータ 36 攪拌翼 37 固定翼 DESCRIPTION OF SYMBOLS 11 Incinerator main body 12 Grate 13 Primary combustion chamber 14 Secondary combustion chamber 15 Input port 18 Burner 19 Circulation path 31 Incinerator inner cylinder 33 Drive shaft 35 Drive motor 36 Stirrer blade 37 Fixed blade

フロントページの続き (72)発明者 山本 久夫 長崎県長崎市深堀町五丁目717番地1 長 菱エンジニアリング株式会社内 (72)発明者 坂井 正康 長崎県長崎市女の都二丁目35番18号Continuation of the front page (72) Inventor Hisao Yamamoto 5-717-1, Fukahori-cho, Nagasaki-shi, Nagasaki Nagasaki Engineering Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 耐火性の焼却炉内に火格子を設けること
で、上下に区画された一次燃焼室及び二次燃焼室を形成
し、前記一次燃焼室に廃棄物の投入口が設けられた廃棄
物の焼却炉において、前記一次燃焼室内に逆円錐台形状
をなす焼却内筒が鉛直軸をもって回転自在に支持され、
該焼却内筒の内周面に上下方向に沿った平板状の攪拌翼
が装着される一方、該焼却内筒の回転中心部に鉛直方向
に沿った平板状の固定翼が設けられたことを特徴とする
廃棄物の焼却炉。
1. A fire grate is provided in a refractory incinerator to form a primary combustion chamber and a secondary combustion chamber which are divided into upper and lower sections, and a waste material inlet is provided in the primary combustion chamber. In a waste incinerator, an incineration inner cylinder having an inverted truncated cone shape is rotatably supported with a vertical axis in the primary combustion chamber,
While the flat stirring blades along the vertical direction are mounted on the inner peripheral surface of the incineration inner cylinder, the flat stationary blades along the vertical direction are provided at the center of rotation of the incineration inner cylinder. Characterized waste incinerator.
JP13312497A 1997-05-23 1997-05-23 Waste incinerator Expired - Fee Related JP3676033B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13312497A JP3676033B2 (en) 1997-05-23 1997-05-23 Waste incinerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13312497A JP3676033B2 (en) 1997-05-23 1997-05-23 Waste incinerator

Publications (2)

Publication Number Publication Date
JPH10325519A true JPH10325519A (en) 1998-12-08
JP3676033B2 JP3676033B2 (en) 2005-07-27

Family

ID=15097358

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13312497A Expired - Fee Related JP3676033B2 (en) 1997-05-23 1997-05-23 Waste incinerator

Country Status (1)

Country Link
JP (1) JP3676033B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007255880A (en) * 2006-02-24 2007-10-04 Fujiyoshi Kogyo Kk Waste treating device
JP2016070518A (en) * 2014-09-26 2016-05-09 隆次 大野 Incinerator
JP2017520748A (en) * 2014-05-14 2017-07-27 エスジーティー カンパニー, リミテッドSgt Co., Ltd. Waste plastic solid fuel incinerator
CN113551233A (en) * 2021-07-30 2021-10-26 深圳市绿世纪环境技术有限公司 Hazardous waste pyrolysis incinerator

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007255880A (en) * 2006-02-24 2007-10-04 Fujiyoshi Kogyo Kk Waste treating device
JP4517131B2 (en) * 2006-02-24 2010-08-04 富士善工業株式会社 Waste treatment equipment
JP2017520748A (en) * 2014-05-14 2017-07-27 エスジーティー カンパニー, リミテッドSgt Co., Ltd. Waste plastic solid fuel incinerator
JP2016070518A (en) * 2014-09-26 2016-05-09 隆次 大野 Incinerator
CN113551233A (en) * 2021-07-30 2021-10-26 深圳市绿世纪环境技术有限公司 Hazardous waste pyrolysis incinerator

Also Published As

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