JP2003083518A - Waste disposal device - Google Patents

Waste disposal device

Info

Publication number
JP2003083518A
JP2003083518A JP2001276278A JP2001276278A JP2003083518A JP 2003083518 A JP2003083518 A JP 2003083518A JP 2001276278 A JP2001276278 A JP 2001276278A JP 2001276278 A JP2001276278 A JP 2001276278A JP 2003083518 A JP2003083518 A JP 2003083518A
Authority
JP
Japan
Prior art keywords
heating chamber
dry distillation
heating
gas
container
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2001276278A
Other languages
Japanese (ja)
Inventor
Hideo Tomita
英夫 富田
Takeshi Hatano
剛 羽田野
Masanobu Kawai
雅信 河合
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP2001276278A priority Critical patent/JP2003083518A/en
Publication of JP2003083518A publication Critical patent/JP2003083518A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve a heating efficiency and save energy. SOLUTION: A waste disposal device comprises a heating chamber 20 which surrounds a carbonizing vessel 21 for housing waste, a heating chamber outlet opened in the heating chamber 20, a heating chamber inlet 26 facing the heating chamber 20 corresponding to the substantially central part of the bottom surface of the carbonizing vessel 21 and a heating means 27 corresponding to the heating chamber inlet 26. Then, the heating means 27 starts a combustion. Generated combustion gas is mixed with air jetted from an air injection port 33 to form heating gas in a carbonizing and combustion chamber 28. The heating gas entering from the heating chamber inlet 26 to the heating chamber 20 collides with the substantially central part of the bottom surface of the carbonizing vessel 21 to heat to a high load. Then, the heating gas flows toward the heating chamber outlet 24 to heat the side surface of the carbonizing vessel 21. As a result, the waste B comes into contact with the bottom surface of the highest temperature in the carbonizing vessel 21, so that the waste is efficiently heated due to a thermal conduction.

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、加熱手段を利用し
て、生ごみなどの廃棄物を乾留処理する廃棄物処理装置
に関し、その運転の制御に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste treatment apparatus for dry-distilling waste such as food waste by using heating means, and relates to control of its operation.

【0002】[0002]

【従来の技術】従来のこの種の廃棄物処理装置は特開2
000−26863号公報に記載されているようなもの
が知られている。従来の燃焼熱を利用した廃棄物処理装
置は図6に示すように1は廃棄物を収容し乾留する乾留
容器、2は乾留容器1を囲むように構成した加熱室、3
は乾留に必要な熱を発生し、さらに乾留容器1で発生し
た乾留ガスを燃焼するバーナからなる加熱手段、4は燃
焼を促進する乾留燃焼室、5は排ガスを排出する排気筒
である。6は乾留燃焼室4で発生したガスを加熱室2に
搬送する加熱ガス通路、7は乾留容器1で発生した乾留
ガスを乾留燃焼室4に搬送する乾留ガス通路、8はファ
ンからなる燃焼用の空気供給部である。
2. Description of the Related Art A conventional waste treatment device of this type is disclosed in Japanese Patent Application Laid-Open No.
The one described in Japanese Patent Application Publication No. 000-26863 is known. As shown in FIG. 6, a conventional waste treatment apparatus utilizing combustion heat is as follows: 1 is a dry distillation container for storing waste and performing dry distillation; 2 is a heating chamber configured to surround the dry distillation container 1;
Is a heating means including a burner for generating heat necessary for dry distillation and burning the dry distillation gas generated in the dry distillation container 1, 4 is a dry combustion chamber for promoting combustion, and 5 is an exhaust stack for discharging exhaust gas. 6 is a heating gas passage for conveying the gas generated in the dry distillation combustion chamber 4 to the heating chamber 2, 7 is a dry distillation gas passage for conveying the dry distillation gas generated in the dry distillation container 1 to the dry distillation combustion chamber 4, and 8 is a combustion fan. Is an air supply unit of.

【0003】そして上記構成において、乾留容器1に生
ごみなどの廃棄物Aを収納し、加熱手段3を燃焼させ、
発生した燃焼ガスは加熱ガス通路6を通って加熱室2に
至り乾留容器1を加熱し、排気筒5から外に排出され
る。燃焼ガスで加熱された乾留容器1に収容された廃棄
物Aは熱分解され乾留されるとともに可燃性ガスである
乾留ガスや蒸気が発生する。これらの乾留ガスや蒸気は
乾留ガス通路7を通って乾留燃焼室4に至り、空気供給
部8から供給される空気と加熱手段3から発生する燃焼
ガスと混合して燃焼する。燃焼によって発生する加熱ガ
スは加熱ガス通路6を通って加熱室2に至り、乾留に必
要な熱として供給させるようになっていた。
In the above structure, the waste A such as raw garbage is stored in the dry distillation container 1 and the heating means 3 is burned,
The generated combustion gas passes through the heating gas passage 6 to reach the heating chamber 2, heats the carbonization container 1, and is discharged from the exhaust pipe 5 to the outside. The waste A stored in the dry distillation container 1 heated by the combustion gas is pyrolyzed and dry-distilled, and at the same time, the dry-distillation gas or steam which is a combustible gas is generated. These dry distillation gas and steam reach the dry distillation combustion chamber 4 through the dry distillation gas passage 7, and are mixed with the air supplied from the air supply unit 8 and the combustion gas generated from the heating means 3 and burned. The heating gas generated by combustion reaches the heating chamber 2 through the heating gas passage 6 and is supplied as heat necessary for dry distillation.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、加熱ガ
スは非対称に乾留容器1の外壁を加熱するので、乾留容
器1は不均一な温度分布になるという課題があった。し
たがって、廃棄物Aを効率よく加熱するためには、乾留
容器1の内部を攪拌させるような工夫が必要である。ま
た、加熱ガス通路6は乾留燃焼室4と加熱室2の底部ま
で連通しているので長く、かつ、加熱ガスが通るため非
常に高温になるので、放熱損失が大きく、また廃棄物処
理装置内の温度上昇が大きくなるという課題があった。
However, since the heating gas asymmetrically heats the outer wall of the dry distillation container 1, there is a problem that the dry distillation container 1 has an uneven temperature distribution. Therefore, in order to efficiently heat the waste A, it is necessary to devise a method for stirring the inside of the dry distillation container 1. Further, the heating gas passage 6 is long since it communicates with the bottoms of the dry distillation combustion chamber 4 and the heating chamber 2, and since the heating gas passes therethrough, the temperature becomes extremely high, so that the heat radiation loss is large, and the inside of the waste treatment device is large. However, there was a problem that the temperature rise was large.

【0005】本発明は、前記従来の課題を解決するもの
で、加熱効率の向上と省エネルギーが図れる廃棄物処理
装置を提供することを目的とする。
The present invention solves the above-mentioned conventional problems, and an object of the present invention is to provide a waste treatment apparatus capable of improving heating efficiency and saving energy.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題を解決
するために、廃棄物を収容する乾留容器を囲む加熱室
と、前記加熱室に開口した加熱室出口と、前記乾留容器
の底面略中央に対応して前記加熱室に臨ませた加熱室入
口と、前記加熱室入口に対応した加熱手段とを備えたも
のである。
In order to solve the above problems, the present invention provides a heating chamber surrounding a dry distillation container for storing waste, a heating chamber outlet opening in the heating chamber, and a bottom surface of the dry distillation container. A heating chamber inlet facing the heating chamber corresponding to the center, and heating means corresponding to the heating chamber inlet are provided.

【0007】上記発明によれば、加熱室入口から加熱室
に流入した加熱ガスは、乾留容器の底面略中央に衝突
し、高負荷に加熱する。その後、加熱ガスは加熱室出口
に向かって流れ、乾留容器の側面を加熱する。この結
果、乾留容器の温度分布は底面から側面に順次温度低下
しているので、乾留容器の底面にある廃棄物は効率よく
加熱できる。また、加熱手段と加熱室入口との距離が短
いので、放熱損失が低減できる。
According to the above-mentioned invention, the heating gas flowing into the heating chamber from the heating chamber inlet collides with substantially the center of the bottom surface of the dry distillation container and is heated to a high load. After that, the heating gas flows toward the outlet of the heating chamber to heat the side surface of the dry distillation container. As a result, the temperature distribution of the dry distillation container gradually decreases from the bottom surface to the side surfaces, so that the waste on the bottom surface of the dry distillation container can be efficiently heated. Moreover, since the distance between the heating means and the inlet of the heating chamber is short, the heat radiation loss can be reduced.

【0008】[0008]

【発明の実施の形態】請求項1に記載の発明は、廃棄物
を収容する乾留容器を囲む加熱室と、前記加熱室に開口
した加熱室出口と、前記乾留容器の底面略中央に対応し
て前記加熱室に臨ませた加熱室入口と、前記加熱室入口
に対応した加熱手段とを備えたものである。そして、加
熱手段から発生し、加熱室入口から加熱室に流入した加
熱ガスは、乾留容器の底面略中央に衝突し、高負荷に加
熱する。その後、加熱ガスは加熱室出口に向かって流
れ、乾留容器の側面をも加熱する。この結果、乾留容器
に投入された廃棄物は乾留容器の中で最も高温の底面に
接触しているので、熱伝導により効率よく加熱される。
また、加熱手段と加熱室入口との距離が短いので、放熱
損失が低減できる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The invention according to claim 1 corresponds to a heating chamber that surrounds a dry distillation container that stores waste, a heating chamber outlet that is open to the heating chamber, and approximately the center of the bottom surface of the dry distillation container. A heating chamber inlet facing the heating chamber and a heating means corresponding to the heating chamber inlet. Then, the heating gas generated from the heating means and flowing into the heating chamber from the inlet of the heating chamber collides with the substantially center of the bottom surface of the dry distillation container, and heats to a high load. After that, the heating gas flows toward the outlet of the heating chamber and also heats the side surface of the dry distillation container. As a result, the waste placed in the dry distillation container is in contact with the hottest bottom surface of the dry distillation container, so that it is efficiently heated by heat conduction.
Moreover, since the distance between the heating means and the inlet of the heating chamber is short, the heat radiation loss can be reduced.

【0009】請求項2に記載の発明は、特に、請求項1
に記載の加熱室出口を乾留容器の側面に対応して加熱室
に複数開口したものである。そして、乾留容器の底面略
中央に衝突した加熱ガスは複数の加熱室出口に向かって
流れ、乾留容器の底面を広く加熱する。この結果、乾留
容器に投入された廃棄物は広く、高温の底面に接触して
いるので、熱伝導により非常に効率よく、安定して加熱
される。
The invention as defined in claim 2 is particularly characterized by claim 1.
A plurality of heating chamber outlets are opened in the heating chamber so as to correspond to the side surfaces of the dry distillation container. Then, the heating gas that has collided with approximately the center of the bottom surface of the dry distillation container flows toward the outlets of the plurality of heating chambers, and widely heats the bottom surface of the dry distillation container. As a result, since the waste put in the dry distillation container is wide and is in contact with the high temperature bottom surface, it is heated very efficiently and stably by heat conduction.

【0010】請求項3に記載の発明は、特に、請求項1
に記載の乾留容器を略円柱または多角柱形状に構成した
ものである。そして、加熱手段から発生し、加熱室入口
から加熱室に流入した加熱ガスは、乾留容器の底面略中
央に衝突し、高負荷に加熱する。その後、加熱ガスは複
数の加熱室出口に向かってほぼ均一に流れ、その際、乾
留容器の全側面を加熱する。この結果、乾留容器の温度
分布は底面から側面に向かって均一に、かつ順次温度低
下しているので、乾留容器の底面にある廃棄物は高温の
底面からの熱伝導と均一な温度分布の側面からの輻射に
より非常に効率よく加熱できる。
The invention as defined in claim 3 is particularly defined by claim 1.
The dry distillation container described in 1. is configured in a substantially columnar or polygonal columnar shape. Then, the heating gas generated from the heating means and flowing into the heating chamber from the inlet of the heating chamber collides with the substantially center of the bottom surface of the dry distillation container, and heats to a high load. Then, the heating gas flows substantially uniformly toward the outlets of the plurality of heating chambers, while heating all side surfaces of the carbonization container. As a result, the temperature distribution of the carbonization container is decreasing uniformly from the bottom surface to the side surface, so that the waste material on the bottom surface of the carbonization container has heat conduction from the high temperature bottom surface and the side surface of uniform temperature distribution. It can be heated very efficiently by radiation from.

【0011】請求項4に記載の発明は、特に、請求項1
に記載の加熱室の内壁と乾留容器の外壁の間隙に位置決
めスペーサを備えたものである。そして、位置決めスペ
ーサにより加熱室と乾留容器との間隙が精度よく設定で
きるので、間隙は通路抵抗が許される範囲まで狭められ
る。この結果、加熱室と乾留容器との間隙では加熱ガス
の流速が速く、熱伝達率が向上するので、加熱ガスは効
率よく乾留容器を加熱できる。また、廃棄物処理装置が
コンパクトにできる。
The invention as defined in claim 4 is particularly characterized by claim 1.
A positioning spacer is provided in the gap between the inner wall of the heating chamber and the outer wall of the dry distillation container. Since the positioning spacer can accurately set the gap between the heating chamber and the dry distillation container, the gap can be narrowed to the range where the passage resistance is allowed. As a result, the flow velocity of the heating gas is high in the gap between the heating chamber and the dry distillation container, and the heat transfer coefficient is improved, so that the heating gas can efficiently heat the dry distillation container. Further, the waste treatment device can be made compact.

【0012】請求項5に記載の発明は、特に、請求項1
に記載の乾留容器の底面近傍に設けた乾留燃焼室の上流
側へ乾留ガスを供給するガス供給部と、前記ガス供給部
と前記乾留容器とを連結する乾留ガス管を備えたもので
ある。そして、乾留容器の底面近傍に乾留燃焼室の上流
側へ乾留ガスを供給するガス供給部を設けたので、乾留
ガス管が短く、乾留ガス管からの放熱損失が抑えられ
る。
The invention as defined in claim 5 is particularly characterized by claim 1.
The dry distillation container is provided with a gas supply unit for supplying dry distillation gas to the upstream side of the dry distillation combustion chamber provided near the bottom surface of the dry distillation container, and a dry distillation gas pipe connecting the gas supply unit and the dry distillation container. Further, since the gas supply unit for supplying the dry distillation gas to the upstream side of the dry distillation combustion chamber is provided near the bottom of the dry distillation container, the dry distillation gas pipe is short, and the heat dissipation loss from the dry distillation gas pipe is suppressed.

【0013】請求項6に記載の発明は、特に、請求項1
に記載の複数の加熱室出口を覆う集合部と、前記集合部
に設けた集合排気通路を備えたものである。そして、排
気ガスは複数の加熱室出口から複数の排気通路に流入
し、その後、集合部に流入する。すなわち、排気ガスは
集合排気通路のみから排出できるので、この排気ガスの
処理が容易である。
The invention according to claim 6 is particularly characterized by claim 1.
And a collecting exhaust passage provided in the collecting unit. Then, the exhaust gas flows into the plurality of exhaust passages from the plurality of heating chamber outlets, and then flows into the collecting portion. That is, since the exhaust gas can be discharged only from the collective exhaust passage, the processing of this exhaust gas is easy.

【0014】請求項7に記載の発明は、特に、請求項1
に記載の集合部と集合排気通路との間に設けた小径の連
絡通路と、前記連絡通路近傍の集合排気通路に開口した
空気口を備えたものである。そして、連絡通路から集合
排気通路に流入する排気ガスにより空気口から空気が引
き込まれるので、排気ガスの温度を低下することができ
る。また、停電等により廃棄物処理装置が停止した場
合、乾留ガスが空気口から引き込んだ空気と混合して予
混合気を形成し集合排気通路から噴出する。その際、何
らかの着火源によりこの予混合気が着火しても、直ちに
逆火して空気口に保炎し集合排気通路内で燃焼が完了す
る。この結果、炎が廃棄物処理装置から噴出することが
防止できる。
The invention as defined in claim 7 is particularly defined by claim 1.
And a small-diameter communication passage provided between the collecting portion and the collection exhaust passage, and an air port opened in the collection exhaust passage near the communication passage. Then, the air is drawn from the air port by the exhaust gas flowing into the collective exhaust passage from the communication passage, so that the temperature of the exhaust gas can be lowered. Further, when the waste treatment device is stopped due to a power failure or the like, the dry distillation gas mixes with the air drawn in from the air port to form a premixed gas and is ejected from the collective exhaust passage. At this time, even if this premixed gas is ignited by some ignition source, it immediately backfires, flames are maintained in the air ports, and combustion is completed in the collective exhaust passage. As a result, it is possible to prevent the flame from ejecting from the waste treatment device.

【0015】[0015]

【実施例】以下、本発明の実施例について図面を用いて
説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0016】(実施例1)図1は、本発明の実施例1に
おける廃棄物処理装置の構成を示す断面図である。
(Embodiment 1) FIG. 1 is a sectional view showing the structure of a waste treatment apparatus according to Embodiment 1 of the present invention.

【0017】図1において、20は有底の加熱室で、生
ごみ等の廃棄物を収容する四角柱形状の乾留容器21を
挿入している。22は加熱室20の外周を囲む断熱材で
あり、外筒23により保持されている。24は加熱室出
口で、乾留容器21の側面に対応して加熱室20に開口
している。25は排気通路であり、断熱材22を突っ切
り加熱室出口24に連通している。26は加熱室入口で
あり、乾留容器21の底面略中央に対応して加熱室20
に臨んでいる。27は天然ガスや灯油を燃料とするバー
ナからなる加熱手段で、円筒形状の乾留燃焼室28を介
して加熱室入口26に連通している。29は乾留燃焼室
28と加熱手段27の間に設けたリング形状に形成した
ガス供給部である。30はガス導入管で、乾留容器21
とガス供給部29とを連通している。31はガス供給部
29の内周面に多数開口するガス噴出口であり、乾留燃
焼室28の中心軸に向かって可燃ガスを噴出する。32
はファンからなる空気供給部であり、空気を噴出する空
気噴出口33をガス供給部29の下流に設けている。3
4は内蓋であり、乾留容器21とガス導入管30とをつ
なぐ空間を形成している。35は内蓋34の外に設けた
蓋である。
In FIG. 1, reference numeral 20 denotes a bottomed heating chamber into which a square column-shaped dry distillation container 21 for storing waste such as food waste is inserted. Reference numeral 22 denotes a heat insulating material that surrounds the outer periphery of the heating chamber 20 and is held by the outer cylinder 23. The heating chamber outlet 24 is open to the heating chamber 20 in correspondence with the side surface of the dry distillation container 21. An exhaust passage 25 cuts through the heat insulating material 22 and communicates with the heating chamber outlet 24. 26 is an inlet of the heating chamber, which corresponds to the approximate center of the bottom surface of the dry distillation container 21.
Facing. Reference numeral 27 denotes a heating means composed of a burner using natural gas or kerosene as a fuel, and communicates with the heating chamber inlet 26 via a cylindrical carbonization combustion chamber 28. Reference numeral 29 is a ring-shaped gas supply portion provided between the dry distillation combustion chamber 28 and the heating means 27. Reference numeral 30 denotes a gas introduction pipe, which is a dry distillation container 21.
And the gas supply unit 29 are in communication with each other. Reference numeral 31 denotes a gas ejection port that opens on the inner peripheral surface of the gas supply unit 29 and ejects a combustible gas toward the central axis of the carbonization combustion chamber 28. 32
Is an air supply unit composed of a fan, and an air ejection port 33 for ejecting air is provided downstream of the gas supply unit 29. Three
An inner lid 4 forms a space connecting the dry distillation container 21 and the gas introduction pipe 30. Reference numeral 35 is a lid provided outside the inner lid 34.

【0018】以上のように構成された廃棄物処理装置に
ついて、以下その動作、作用を説明する。
The operation and action of the waste treatment apparatus configured as described above will be described below.

【0019】まず、蓋35と内蓋34を開けて、生ごみ
等の廃棄物Bを乾留容器21に挿入後、再び蓋35と内
蓋34を密閉する。そして、加熱手段27が燃焼を開始
し、発生した燃焼ガスは乾留燃焼室28で空気噴出口3
3から噴出する空気と混合して加熱ガスを形成する。加
熱室入口26から加熱室20に流入した加熱ガスは乾留
容器21の底面略中央に衝突し、高負荷に加熱する。そ
の後、加熱ガスは加熱室出口24に向かって流れなが
ら、乾留容器21の側面を加熱する。この結果、乾留容
器21の温度分布は底面から側面に沿って温度低下して
いる。そして、廃棄物Bは乾留容器21の中で最も高温
の底面に接触しているので、熱伝導により効率よく加熱
される。
First, the lid 35 and the inner lid 34 are opened, the waste B such as food waste is inserted into the dry distillation container 21, and then the lid 35 and the inner lid 34 are sealed again. Then, the heating means 27 starts combustion, and the generated combustion gas is discharged from the air jet port 3 in the carbonization combustion chamber 28.
It mixes with the air ejected from 3 to form a heated gas. The heating gas flowing into the heating chamber 20 through the heating chamber inlet 26 collides with the substantially center of the bottom surface of the dry distillation container 21 and heats it with a high load. Then, the heating gas flows toward the heating chamber outlet 24 to heat the side surface of the dry distillation container 21. As a result, the temperature distribution of the dry distillation container 21 decreases from the bottom surface to the side surfaces. Since the waste B is in contact with the hottest bottom surface of the dry distillation container 21, it is efficiently heated by heat conduction.

【0020】続いて、乾留容器21の内部は温度上昇
し、廃棄物Bから蒸気、乾留ガスが順次発生し、ガス導
入管30を介してガス供給部29に流入する。
Subsequently, the temperature inside the dry distillation container 21 rises, and steam and dry distillation gas are sequentially generated from the waste B and flow into the gas supply unit 29 through the gas introduction pipe 30.

【0021】その後、可燃ガスである乾留ガスがガス噴
出口31から乾留燃焼室28の中心軸に向かって噴出す
る。その際、乾留ガスは加熱手段27から発生する燃焼
ガスにより着火し、空気噴出口33から噴出される空気
へ拡散しながら拡散燃焼する。この結果、乾留ガスや蒸
気は燃焼処理(脱臭、クリーン化)され、かつ発生する
熱は乾留容器21の加熱に使われる。また、従来例に比
べて加熱手段27と加熱室入口26との距離が短く、か
つ空気供給部32の空気が乾留燃焼室28の内壁から熱
回収するので、放熱損失が低減でき、省エネルギーが図
れる。
Thereafter, the dry distillation gas which is a combustible gas is ejected from the gas ejection port 31 toward the central axis of the dry distillation combustion chamber 28. At that time, the dry distillation gas is ignited by the combustion gas generated from the heating means 27 and diffuse-combusted while diffusing into the air jetted from the air jet port 33. As a result, the dry distillation gas and steam are burnt (deodorized, cleaned), and the heat generated is used to heat the dry distillation container 21. Further, the distance between the heating means 27 and the heating chamber inlet 26 is shorter than that in the conventional example, and the air in the air supply part 32 recovers heat from the inner wall of the carbonization combustion chamber 28, so that the heat radiation loss can be reduced and energy can be saved. .

【0022】以上のように、本実施例においては、乾留
容器21の底面略中央に対応して加熱室20に臨ませた
加熱室入口26と、加熱室入口26に連通した加熱手段
27を設けた乾留燃焼室28を備えたことにより、加熱
ガスは乾留容器21の底面略中央に衝突し、高負荷に加
熱する。この結果、廃棄物Bは乾留容器21の中で最も
高温の底面に接触しているので、熱伝導により効率よく
加熱される。
As described above, in the present embodiment, the heating chamber inlet 26 facing the heating chamber 20 and the heating means 27 communicating with the heating chamber inlet 26 are provided so as to correspond to the approximate center of the bottom surface of the dry distillation container 21. Since the dry distillation combustion chamber 28 is provided, the heating gas collides with the center of the bottom surface of the dry distillation container 21 and heats it with a high load. As a result, since the waste B is in contact with the bottom of the dry distillation container 21 having the highest temperature, the waste B is efficiently heated by heat conduction.

【0023】(実施例2)図2は、本発明の実施例2に
おける廃棄物処理装置の平面断面図を示すものである。
図2において、実施例1の構成と異なるところは加熱室
出口36と排気通路37を乾留容器38の側面に対応し
て加熱室39に複数均等に開口した点である。
(Embodiment 2) FIG. 2 is a plan sectional view of a waste treatment apparatus according to Embodiment 2 of the present invention.
In FIG. 2, the difference from the configuration of the first embodiment is that a plurality of heating chamber outlets 36 and exhaust passages 37 are evenly opened in the heating chamber 39 corresponding to the side surface of the dry distillation container 38.

【0024】以上のように構成された廃棄物処理装置に
ついて、以下その動作、作用を説明する。加熱手段27
が燃焼を開始すると、発生した燃焼ガスは乾留燃焼室2
8で空気噴出口33から噴出する空気と混合して加熱ガ
スを形成する。加熱室入口26から加熱室20に流入し
た加熱ガスは乾留容器21の底面略中央に衝突し、高負
荷に加熱する。その後、加熱ガスは複数の加熱室出口3
6に向かって流れながら、乾留容器38の底面を広く加
熱する。この結果、乾留容器38に投入された廃棄物B
は広く、乾留容器38の高温の底面に接触しているの
で、熱伝導により非常に効率よく、安定して加熱され
る。
The operation and action of the waste treatment apparatus configured as described above will be described below. Heating means 27
When the combustion starts, the combustion gas generated is generated by the carbonization combustion chamber 2
At 8, the mixture is mixed with the air ejected from the air ejection port 33 to form a heating gas. The heating gas flowing into the heating chamber 20 through the heating chamber inlet 26 collides with the substantially center of the bottom surface of the dry distillation container 21 and heats it with a high load. After that, the heating gas is supplied to the heating chamber outlets 3
While flowing toward 6, the bottom of the dry distillation container 38 is heated widely. As a result, the waste B put in the dry distillation container 38
Is in wide contact with the high temperature bottom surface of the dry distillation container 38, so that it is heated very efficiently and stably by heat conduction.

【0025】以上のように、本実施例においては、加熱
室出口36を乾留容器38の側面に対応して加熱室39
に複数均等に開口したので、加熱ガスは複数の加熱室出
口36に向かって流れながら、乾留容器38の底面を広
く加熱する。この結果、廃棄物Bは広く、乾留容器38
の高温の底面に接触しているので、熱伝導により非常に
効率よく、安定して加熱される。
As described above, in this embodiment, the heating chamber outlet 36 corresponds to the side surface of the carbonization container 38 and the heating chamber 39.
Since the plurality of openings are evenly opened, the heating gas flows toward the plurality of heating chamber outlets 36 and widely heats the bottom surface of the dry distillation container 38. As a result, the waste B is wide and the dry distillation container 38
Since it is in contact with the high temperature bottom surface of the, it is heated very efficiently and stably by heat conduction.

【0026】(実施例3)図2は、本発明の実施例3に
おける廃棄物処理装置の平面断面図を示すものである。
図2において、実施例1の構成と異なるところは乾留容
器38を円柱形状にした点である。以上のように構成さ
れた廃棄物処理装置について、以下その動作、作用を説
明する。
(Embodiment 3) FIG. 2 is a plan sectional view of a waste treatment apparatus according to Embodiment 3 of the present invention.
In FIG. 2, the difference from the configuration of the first embodiment is that the dry distillation container 38 has a cylindrical shape. The operation and action of the waste treatment apparatus configured as described above will be described below.

【0027】加熱手段27が燃焼を開始すると、発生し
た燃焼ガスは乾留燃焼室28で空気噴出口33から噴出
する空気と混合して加熱ガスを形成する。加熱室入口2
6から加熱室20に流入した加熱ガスは乾留容器21の
底面略中央に衝突し、高負荷に加熱する。その後、乾留
容器38の底面略中央から側面までの距離がほぼ同じな
ので、加熱ガスは複数の加熱室出口36に向かってほぼ
均一に広がり、乾留容器38の全側面を直接加熱する。
この結果、乾留容器38の温度分布は底面から側面に向
かって均一に、かつ温度低下している。そして、乾留容
器38に投入された廃棄物Bは乾留容器38の高温の底
面からの熱伝導と乾留容器38の側面から輻射により非
常に効率よく、かつ、均一に加熱される。
When the heating means 27 starts combustion, the generated combustion gas is mixed with the air ejected from the air ejection port 33 in the carbonization combustion chamber 28 to form a heating gas. Heating chamber entrance 2
The heating gas flowing from 6 into the heating chamber 20 collides with the approximate center of the bottom surface of the dry distillation container 21 and heats to a high load. After that, since the distance from the substantially center of the bottom surface of the dry distillation container 38 to the side surface is substantially the same, the heating gas spreads substantially uniformly toward the plurality of heating chamber outlets 36, and directly heats all the side surfaces of the dry distillation container 38.
As a result, the temperature distribution of the dry distillation container 38 decreases uniformly from the bottom surface to the side surfaces. The waste B put in the dry distillation container 38 is heated very efficiently and uniformly by heat conduction from the high temperature bottom surface of the dry distillation container 38 and radiation from the side surface of the dry distillation container 38.

【0028】以上のように、本実施例においては、乾留
容器38を円柱形状にしたので、乾留容器38の底面略
中央に衝突した加熱ガスは複数の加熱室出口24に向か
ってほぼ均一に広がる。この結果、廃棄物Bは乾留容器
38の高温の底面からの熱伝導と乾留容器38の側面か
ら輻射により非常に効率よく、かつ、均一に加熱され
る。なお、乾留容器の形状は円柱に比べて効果は若干劣
るが多角柱でよい。
As described above, in the present embodiment, since the dry distillation container 38 has a cylindrical shape, the heating gas colliding with the substantially center of the bottom surface of the dry distillation container 38 spreads substantially uniformly toward the plurality of heating chamber outlets 24. . As a result, the waste B is heated very efficiently and uniformly by heat conduction from the hot bottom surface of the carbonization container 38 and radiation from the side surface of the carbonization container 38. The shape of the dry distillation container may be a polygonal prism, although the effect is slightly inferior to that of a cylinder.

【0029】(実施例4)図3は、本発明の実施例4に
おける廃棄物処理装置の要部断面構成図を示すものであ
る。図3において、実施例1の構成と異なるところは加
熱室40の内壁を乾留容器41に向って突出した位置決
めスペーサ42を設けた点である。
(Embodiment 4) FIG. 3 is a sectional view showing the essential parts of a waste treatment apparatus according to Embodiment 4 of the present invention. In FIG. 3, the difference from the configuration of the first embodiment is that a positioning spacer 42 is provided which projects the inner wall of the heating chamber 40 toward the dry distillation container 41.

【0030】以上のように構成された廃棄物処理装置に
ついて、以下その動作、作用を説明する。加熱室40に
挿入された乾留容器41は位置決めスペーサ42により
位置がきまる。位置決めスペーサ42は加熱室40の内
壁と乾留容器41の外壁との間隙Lを任意に精度よく設
定できる。すなわち、間隙Lは通路抵抗が許される範囲
(加熱手段27や空気供給部32の性能維持できる範
囲)まで狭められ、かつどの場所でも間隙Lをほぼ同一
にできる。この結果、間隙Lでは加熱ガスの流速が速
く、熱伝達率が向上するので、加熱ガスは効率よく乾留
容器21の側面を加熱できる。なお、乾留容器41の外
壁を加熱室40に向って突出して位置決めスペーサを形
成してよく、また、別部品でもよい。
The operation and action of the waste treatment apparatus configured as above will be described below. The position of the dry distillation container 41 inserted into the heating chamber 40 is determined by the positioning spacer 42. The positioning spacer 42 can arbitrarily and accurately set the gap L between the inner wall of the heating chamber 40 and the outer wall of the carbonization container 41. That is, the gap L is narrowed to the range where the passage resistance is allowed (the range in which the performance of the heating means 27 and the air supply part 32 can be maintained), and the gap L can be made almost the same at any place. As a result, the flow velocity of the heating gas is high in the gap L and the heat transfer rate is improved, so that the heating gas can efficiently heat the side surface of the dry distillation container 21. The outer wall of the dry distillation container 41 may be projected toward the heating chamber 40 to form a positioning spacer, or may be a separate component.

【0031】以上のように、本実施例においては、加熱
室40の内壁を乾留容器41に向って突出した位置決め
スペーサ42を設けたので、間隙Lは通路抵抗が許され
る範囲まで狭められ、かつどの場所でも間隙Lをほぼ同
一にできる。この結果、加熱ガスは効率よく乾留容器2
1の側面を加熱できる。
As described above, in this embodiment, since the positioning spacer 42 is provided which projects the inner wall of the heating chamber 40 toward the dry distillation container 41, the gap L is narrowed to the range where passage resistance is allowed, and The gap L can be made almost the same at any place. As a result, the heating gas is efficiently used in the dry distillation container 2.
One side can be heated.

【0032】(実施例5)図4は、本発明の実施例5に
おける廃棄物処理装置の断面構成図を示すものである。
図4において、実施例1の構成と異なるところはガス供
給部43を乾留容器44の底面近傍に設け、乾留容器4
4とガス供給部43とを連結して乾留容器44から発生
する乾留ガスが流入する乾留ガス管45を設けた点であ
る。さらに、乾留燃焼室46と加熱手段47とを乾留容
器44の底面に沿って横方向にもうけている。
(Embodiment 5) FIG. 4 is a sectional view showing the construction of a waste treatment apparatus according to Embodiment 5 of the present invention.
In FIG. 4, the difference from the configuration of the first embodiment is that the gas supply unit 43 is provided near the bottom of the dry distillation container 44,
4 is connected to the gas supply unit 43, and a dry distillation gas pipe 45 into which the dry distillation gas generated from the dry distillation container 44 flows is provided. Further, a dry distillation combustion chamber 46 and a heating means 47 are provided laterally along the bottom surface of the dry distillation container 44.

【0033】以上のように構成された廃棄物処理装置に
ついて、以下その動作、作用を説明する。加熱手段47
が燃焼を開始すると、発生した燃焼ガスは乾留燃焼室4
6で空気噴出口33から噴出する空気と混合して加熱ガ
スを形成する。この加熱ガスが乾留容器44を加熱する
ので、乾留容器44の内部は温度上昇し、廃棄物Bから
蒸気、乾留ガスが順次発生し、ガス導入管45を介して
ガス供給部43に流入する。
The operation and action of the waste treatment apparatus configured as described above will be described below. Heating means 47
When the combustion starts, the combustion gas generated is generated by the carbonization combustion chamber 4
At 6, the mixture is mixed with the air ejected from the air ejection port 33 to form a heating gas. Since the heating gas heats the dry distillation container 44, the temperature inside the dry distillation container 44 rises, and steam and dry distillation gas are sequentially generated from the waste B and flow into the gas supply unit 43 through the gas introduction pipe 45.

【0034】その後、乾留ガスがガス噴出口31から乾
留燃焼室46の中心軸に向かって噴出する。その際、乾
留ガスは加熱手段47から発生する燃焼ガスにより着火
し、空気噴出口33から噴出される空気へ拡散しながら
拡散燃焼する。この結果、乾留ガスは燃焼処理され、か
つ発生する熱は乾留容器44の加熱に使われる。また、
従来例に比べて乾留容器44の底面近傍にガス供給部4
3を設けたので、乾留ガス管45が短くなる分、乾留ガ
ス管45からの放熱損失が抑えられる。
Then, the carbonization gas is ejected from the gas ejection port 31 toward the central axis of the carbonization combustion chamber 46. At that time, the dry distillation gas is ignited by the combustion gas generated from the heating means 47, and diffuses and burns while diffusing into the air jetted from the air jet port 33. As a result, the carbonization gas is burned and the heat generated is used to heat the carbonization container 44. Also,
Compared with the conventional example, the gas supply unit 4 is provided near the bottom of the dry distillation container 44.
Since 3 is provided, the heat dissipation loss from the dry distillation gas pipe 45 can be suppressed as the dry distillation gas pipe 45 becomes shorter.

【0035】以上のように、本実施例においては、ガス
供給部43を乾留容器44の底面近傍に設け、乾留容器
44とガス供給部43とを連結する乾留ガス管45を設
けたので、乾留ガス管45が短くなる分、乾留ガス管4
5からの放熱損失が抑えられる。
As described above, in this embodiment, the gas supply part 43 is provided near the bottom of the dry distillation container 44, and the dry distillation gas pipe 45 connecting the dry distillation container 44 and the gas supply part 43 is provided. As the gas pipe 45 becomes shorter, the dry distillation gas pipe 4
The heat radiation loss from 5 can be suppressed.

【0036】(実施例6)図4は、本発明の実施例6に
おける廃棄物処理装置の断面構成図を示すものである。
図4において、実施例5の構成と異なるところは複数の
排気通路25を覆う集合部48と、集合排気通路49を
集合部48に設けた点である。
(Embodiment 6) FIG. 4 is a sectional view showing the construction of a waste treatment apparatus according to Embodiment 6 of the present invention.
In FIG. 4, the difference from the configuration of the fifth embodiment is that a collecting portion 48 that covers the plurality of exhaust passages 25 and a collecting exhaust passage 49 are provided in the collecting portion 48.

【0037】以上のように構成された廃棄物処理装置に
ついて、以下その動作、作用を説明する。乾留容器44
の側面を加熱した加熱ガスは複数の加熱室出口24から
複数の排気通路25に流入し、その後、排気ガスとして
集合部48に流入する。続いて、この排気ガスは集合排
気通路49のみから排出できるので、排気ガスの処理が
容易である。
The operation and action of the waste treatment apparatus configured as described above will be described below. Dry distillation container 44
The heating gas that has heated the side surface of the above flows into the plurality of exhaust passages 25 from the plurality of heating chamber outlets 24, and then flows into the collecting portion 48 as exhaust gas. Subsequently, since this exhaust gas can be discharged only from the collective exhaust passage 49, the processing of the exhaust gas is easy.

【0038】以上のように、本実施例においては、複数
の加熱室出口を覆う集合部と、集合部に設けた集合排気
通路を設けたので、排気ガスを集合排気通路のみから排
出でき、排気ガスの処理が容易である。
As described above, in this embodiment, since the collecting portion covering the plurality of heating chamber outlets and the collecting exhaust passage provided in the collecting portion are provided, the exhaust gas can be discharged only from the collecting exhaust passage. Easy to process gas.

【0039】(実施例7)図5は、本発明の実施例5に
おける廃棄物処理装置の腰部拡大断面図を示すものであ
る。図5において、実施例6の構成と異なるところは小
径の連絡通路50を集合部51と集合排気通路52の底
面との間に設け、連絡通路50近傍の集合排気通路52
の底面に空気口53を複数開口した点である。
(Embodiment 7) FIG. 5 is an enlarged sectional view of the waist of a waste treatment apparatus according to Embodiment 5 of the present invention. In FIG. 5, a difference from the configuration of the sixth embodiment is that a small-diameter connecting passage 50 is provided between the collecting portion 51 and the bottom surface of the collecting exhaust passage 52, and the collecting exhaust passage 52 near the connecting passage 50.
Is a point where a plurality of air ports 53 are opened on the bottom surface of the.

【0040】以上のように構成された廃棄物処理装置に
ついて、以下その動作、作用を説明する。乾留容器44
の側面を加熱した加熱ガスは複数の加熱室出口24から
複数の排気通路25に流入し、その後、集合部51に流
入する。続いて、加熱ガスは小径の連絡通路50から大
径の集合排気通路49に噴出した際、複数の空気口53
から空気を引き込み、混合する。この結果、集合排気通
路49から低温の排気ガスが噴出するので、安全性が高
まる。
The operation and action of the waste treatment apparatus configured as described above will be described below. Dry distillation container 44
The heating gas that has heated the side surface of the above flows into the plurality of exhaust passages 25 from the plurality of heating chamber outlets 24, and then flows into the collecting portion 51. Subsequently, when the heated gas is ejected from the small-diameter communication passage 50 to the large-diameter collective exhaust passage 49, a plurality of air ports 53 are provided.
Intake air from and mix. As a result, low-temperature exhaust gas is ejected from the collective exhaust passage 49, improving safety.

【0041】また、停電等により廃棄物処理装置が停止
した場合、熱容量の分乾留容器44の温度低下が遅く、
乾留容器44から乾留ガスの発生が長期継続する。そし
て、乾留ガスは複数の加熱室出口24から複数の排気通
路25に流入し、その後、集合部51に流入する。続い
て、乾留ガスは小径の連絡通路50から大径の集合排気
通路49に噴出した際、複数の空気口53から空気を引
き込み、混合して予混合気が形成される。そして、予混
合気が集合排気通路49から噴出した時、何らかの着火
源により予混合気が着火しても、直ちに逆火して空気口
に保炎し集合排気通路内で燃焼が完了する。この結果、
炎が集合排気通路49から噴出することを防止できる。
When the waste treatment equipment is stopped due to a power failure or the like, the temperature drop of the dry distillation container 44 due to the heat capacity is slow,
Generation of dry distillation gas from the dry distillation container 44 continues for a long time. Then, the dry distillation gas flows into the plurality of exhaust passages 25 from the plurality of heating chamber outlets 24, and then flows into the collecting portion 51. Then, when the dry distillation gas is ejected from the small-diameter communication passage 50 to the large-diameter collective exhaust passage 49, the air is drawn in from a plurality of air ports 53 and mixed to form a premixed gas. Then, when the premixed gas is ejected from the collective exhaust passage 49, even if the premixed gas is ignited by some ignition source, it immediately backfires to hold the flame in the air port, and the combustion is completed in the collective exhaust passage. As a result,
It is possible to prevent the flame from ejecting from the collective exhaust passage 49.

【0042】なお、本実施例7では、小径の連絡通路5
0を設けたが、要は加熱ガスや乾留ガス自身が空気口か
ら空気を吸引できる構成ならばよい。以上のように、本
実施例においては、連絡通路50近傍の集合排気通路5
2に空気口53を開口したので、集合排気通路49から
の噴出する排気ガスや乾留ガスの温度が下げられ、かつ
何らかの着火源により乾留ガスの予混合気が着火して
も、直ちに空気口53に逆火して安全性が確保できる。
In the seventh embodiment, the small diameter communication passage 5 is used.
Although 0 is provided, the point is that the heating gas or dry distillation gas itself can suck air from the air port. As described above, in the present embodiment, the collective exhaust passage 5 near the communication passage 50.
Since the air port 53 is opened at 2, the temperature of the exhaust gas or dry distillation gas ejected from the collective exhaust passage 49 is lowered, and even if the premixed gas of dry distillation gas is ignited by some ignition source, the air port is immediately opened. It is possible to secure safety by flashing back to 53.

【0043】[0043]

【発明の効果】以上のように、請求項1から7に記載の
発明によれば、加熱効率の向上と省エネルギーが図れ
る。
As described above, according to the invention described in claims 1 to 7, it is possible to improve the heating efficiency and save energy.

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

【図1】本発明の実施例1における廃棄物処理装置の構
成を示す断面図
FIG. 1 is a cross-sectional view showing the configuration of a waste treatment device according to a first embodiment of the present invention.

【図2】本発明の実施例2及び3における廃棄物処理装
置の平面断面図
FIG. 2 is a plan cross-sectional view of a waste treatment device according to embodiments 2 and 3 of the present invention.

【図3】本発明の実施例4における廃棄物処理装置の要
部断面図
FIG. 3 is a cross-sectional view of essential parts of a waste treatment device according to a fourth embodiment of the present invention.

【図4】本発明の実施例5及び6における廃棄物処理装
置の構成を示す断面図
FIG. 4 is a cross-sectional view showing the configuration of a waste treatment device according to embodiments 5 and 6 of the present invention.

【図5】本発明の実施例7における廃棄物処理装置の要
部拡大断面図
FIG. 5 is an enlarged cross-sectional view of a main part of a waste treatment device according to a seventh embodiment of the present invention.

【図6】従来の廃棄物処理装置の構成図FIG. 6 is a block diagram of a conventional waste treatment device.

【符号の説明】[Explanation of symbols]

20、36、40、44 加熱室 21、38、41 乾留容器 22、47 加熱手段 24、36 加熱室出口 26 加熱室入口 27、47 加熱手段 29、43 ガス供給部 30、45 乾留ガス管 42 位置決めスペーサ 48、51 集合部 49、52 集合排気通路 50 連絡通路 53 空気口 20, 36, 40, 44 Heating chamber 21, 38, 41 Dry distillation container 22,47 heating means 24, 36 Heating chamber outlet 26 Heating chamber entrance 27, 47 heating means 29, 43 Gas supply section 30, 45 Dry distillation gas pipe 42 Positioning spacer 48, 51 Assembly 49, 52 Collective exhaust passage 50 connecting passage 53 Air port

フロントページの続き (72)発明者 河合 雅信 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 3K061 AB02 AC01 AC12 BA06 3K062 AA19 AB02 AC01 EA01 EB46 4D004 AA03 BA03 CA24 CA27 CA48 CB02 CB34 Continued front page    (72) Inventor Masanobu Kawai             1006 Kadoma, Kadoma-shi, Osaka Matsushita Electric             Sangyo Co., Ltd. F-term (reference) 3K061 AB02 AC01 AC12 BA06                 3K062 AA19 AB02 AC01 EA01 EB46                 4D004 AA03 BA03 CA24 CA27 CA48                       CB02 CB34

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物を収容する乾留容器を囲む加熱室
と、前記加熱室に開口した加熱室出口と、前記乾留容器
の底面略中央に対応して前記加熱室に臨ませた加熱室入
口と、前記加熱室入口に対応した加熱手段を備えた廃棄
物処理装置。
1. A heating chamber that surrounds a dry distillation container that stores waste, a heating chamber outlet that opens to the heating chamber, and a heating chamber inlet that faces the heating chamber in a substantially central portion of the bottom surface of the dry distillation container. And a waste treatment device provided with heating means corresponding to the inlet of the heating chamber.
【請求項2】 加熱室出口を乾留容器の側面に対応して
加熱室に複数開口した請求項1記載の廃棄物処理装置。
2. The waste treatment apparatus according to claim 1, wherein a plurality of heating chamber outlets are opened in the heating chamber so as to correspond to the side surfaces of the dry distillation container.
【請求項3】 略円柱または多角柱形状の乾留容器を備
えた請求項1記載の廃棄物処理装置。
3. The waste treatment apparatus according to claim 1, further comprising a dry distillation container having a substantially columnar shape or a polygonal columnar shape.
【請求項4】 加熱室の内壁と乾留容器の外壁の間隙に
位置決めスペーサを備えた請求項1記載の廃棄物処理装
置。
4. The waste treatment device according to claim 1, further comprising a positioning spacer provided in a gap between an inner wall of the heating chamber and an outer wall of the carbonization container.
【請求項5】 乾留容器の底面近傍に設けた乾留燃焼室
の上流側へ乾留ガスを供給するガス供給部と、前記ガス
供給部と前記乾留容器とを連通する乾留ガス管とを備え
た請求項1記載の廃棄物処理装置。
5. A gas supply unit for supplying a carbonization gas to an upstream side of a carbonization combustion chamber provided in the vicinity of the bottom of the carbonization container, and a carbonization gas pipe connecting the gas supply unit and the carbonization container. Item 1. The waste treatment device according to item 1.
【請求項6】 複数の加熱室出口を覆う集合部と、前記
集合部に設けた集合排気通路とを備えた請求項2記載の
廃棄物処理装置。
6. The waste treatment apparatus according to claim 2, further comprising: a collecting portion that covers the outlets of the plurality of heating chambers, and a collecting exhaust passage provided in the collecting portion.
【請求項7】 集合部と集合排気通路との間に設けた小
径の連絡通路と、前記連絡通路近傍の集合排気通路に開
口した空気口を備えた請求項6記載の廃棄物処理装置。
7. The waste treatment apparatus according to claim 6, further comprising a small-diameter communication passage provided between the collecting portion and the collection exhaust passage, and an air port opened in the collection exhaust passage near the communication passage.
JP2001276278A 2001-09-12 2001-09-12 Waste disposal device Pending JP2003083518A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001276278A JP2003083518A (en) 2001-09-12 2001-09-12 Waste disposal device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001276278A JP2003083518A (en) 2001-09-12 2001-09-12 Waste disposal device

Publications (1)

Publication Number Publication Date
JP2003083518A true JP2003083518A (en) 2003-03-19

Family

ID=19101003

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001276278A Pending JP2003083518A (en) 2001-09-12 2001-09-12 Waste disposal device

Country Status (1)

Country Link
JP (1) JP2003083518A (en)

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