JP2002121562A - Structure of carbonization chamber flue and carbonization device - Google Patents

Structure of carbonization chamber flue and carbonization device

Info

Publication number
JP2002121562A
JP2002121562A JP2000319506A JP2000319506A JP2002121562A JP 2002121562 A JP2002121562 A JP 2002121562A JP 2000319506 A JP2000319506 A JP 2000319506A JP 2000319506 A JP2000319506 A JP 2000319506A JP 2002121562 A JP2002121562 A JP 2002121562A
Authority
JP
Japan
Prior art keywords
carbonization
chamber
carbonization chamber
combustion
flue
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
JP2000319506A
Other languages
Japanese (ja)
Inventor
Kazunari Aida
一成 会田
Shigeo Watanabe
成夫 渡辺
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.)
Showa Denko Materials Co Ltd
Original Assignee
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP2000319506A priority Critical patent/JP2002121562A/en
Publication of JP2002121562A publication Critical patent/JP2002121562A/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
    • Y02E50/10Biofuels, e.g. bio-diesel

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To provide a carbonization device which does not generate any ignition source in carbides and inhibits combustion of carbides when taking them out. SOLUTION: In a structure of a carbonization chamber flue 4 communicating a carbonization chamber 1 having an agitating blade for stirring wastes inside with a combustion chamber 3 positioned near the carbonization chamber, the carbonization chamber 1 and the combustion chamber 3 are connected via a tubular member. In the middle of the tubular member, a one-way damper 21 is arranged to allow gas to flow in only one direction and block the circulation of the flow from the opposite 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、炭化室煙道の構造
及び炭化装に関し、更に詳しくは、生ごみ、紙類、木
材、紙おむつ等の可燃性ごみを炭化処理して、減容、減
量化するごみ炭化装置の炭化室煙道の構造、及びそれを
利用した炭化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the structure and carbonization of a carbonization chamber flue, and more particularly to carbonization of combustible waste such as garbage, paper, wood, and disposable diapers to reduce the volume and weight. The present invention relates to a structure of a carbonization chamber flue of a refuse carbonization device and a carbonization device using the same.

【0002】[0002]

【従来の技術】生ごみ、紙類、木材、紙おむつ等の可燃
性ごみを炭化処理して、減容、減量するごみ炭化装置
は、従来、いくつか知られている(例えば、特開平7−
280236号公報、特開平10−160136号公報
等)。これらの炭化装置には生ごみ、紙類、木材、紙お
むつ等の可燃性ごみを収納しごみを炭化処理する炭化
室、その炭化室を囲むように形成されると共に加熱機
(第一バーナ)を有する加熱室、炭化室とは炭化室煙道
で連通し炭化室で発生した可燃性ガス等を燃焼させる燃
焼機(第二バーナ)を有する燃焼室、その他排気筒等が
備えられている。
2. Description of the Related Art There are several known carbonizing apparatuses for carbonizing flammable refuse such as garbage, paper, wood, and disposable diapers to reduce the volume and weight of the refuse (see, for example, Japanese Patent Application Laid-Open No. Hei 7-1995).
280236, JP-A-10-160136, etc.). These carbonization devices are provided with a carbonization chamber for storing combustible waste such as garbage, paper, wood, and disposable diapers and carbonizing the waste, and a heating machine (first burner) formed around the carbonization chamber. The heating chamber and the carbonization chamber are provided with a combustion chamber having a combustor (second burner) for communicating combustible gas and the like generated in the carbonization chamber by communicating with a carbonization chamber flue, and other exhaust pipes.

【0003】炭化処理の運転は、炭化室に設置した温度
測定装置で炭化室の温度を測定しながら、その温度が一
定になるように加熱機11の運転を調節すると共に、撹
拌翼を駆動してごみを撹拌しながら炭化運転(炭化工
程)が行われる。ごみが炭化し炭化物になると、次に炭
化物の温度を下げるために、撹拌翼は炭化工程と同様の
運転を継続したまま、加熱室の加熱機の運転を停止し、
ファンを駆動させながら炭化室を周囲から空冷する冷却
運転(冷却工程)が行われ、その後、全運転を終える。
ここで、ごみや炭化物から発生する臭気や可燃性ガスは
炭化運転中は勿論、冷却運転中でも炭化物の温度が高い
間は継続して発生するので、燃焼室の燃焼機は全運転に
わたり燃焼を継続している。
In the operation of the carbonization treatment, while measuring the temperature of the carbonization chamber with a temperature measuring device installed in the carbonization chamber, the operation of the heater 11 is adjusted so that the temperature becomes constant, and the stirring blade is driven. The carbonization operation (carbonization step) is performed while stirring the garbage. When the refuse is carbonized and turned into carbide, the stirring blade stops the operation of the heater in the heating chamber, while continuing the same operation as in the carbonization process, in order to lower the temperature of the carbide.
A cooling operation (cooling step) of cooling the carbonization chamber from the surroundings while driving the fan is performed, and then the entire operation is completed.
Here, the odor and flammable gas generated from the refuse and carbides are generated continuously during the carbonization operation and also during the cooling operation while the temperature of the carbides is high, so that the combustor in the combustion chamber continues combustion during the entire operation. are doing.

【0004】[0004]

【発明が解決しようとする課題】炭化装置で処理するご
みの種類によっては、全運転が終了し、炭化物を取り出
すときに、炭化物の内部に火種が発生している場合があ
り、時間が経過すると炭化物の燃焼が加速されて、炭化
物から煙や炎が発生するという問題があった。本発明の
目的は、このような問題を解消すること、すなわち、炭
化物に火種が発生せず、炭化物を取り出すときに炭化物
が燃焼しない炭化装置を提供することである。
Depending on the type of refuse to be treated by the carbonization device, a fire may be generated inside the carbide when the entire operation is completed and the carbide is taken out. There is a problem that the combustion of the carbide is accelerated and smoke and a flame are generated from the carbide. An object of the present invention is to solve such a problem, that is, to provide a carbonization apparatus in which no ignition is generated in the carbide and the carbide does not burn when the carbide is taken out.

【0005】[0005]

【課題を解決するための手段】本発明者らは、上記目的
を達成するため、まず、炭化物の発火現象を検討し、次
のことが分かった。すなわち、炭化工程では火種の発生
がなく、冷却工程で火種が発生している。冷却工程で
は、炭化物の温度の低下と共に可燃ガスの発生が少なく
なり、炭化室の圧力が低下するので、燃焼を継続してい
る燃焼室の圧力が相対的に高くなり、燃焼室の高温の燃
焼ガスが炭化室の内部に流入、または、炭化室内部のガ
スと置換する現象が起こる。そして、炭化室の中に流入
した燃焼ガス中の酸素によって、炭化室内の炭化物が発
火し、全運転終了後でも炭化物の内部に発火した炭化物
が火種として残存していた。そして、炭化物を取出す時
に炭化室の扉を開けて炭化室を大気開放すると、炭化室
内部に外気が流入して燃焼が促進され、その結果、炭化
物から煙や炎が発生していたものである。
Means for Solving the Problems In order to achieve the above object, the present inventors first studied the ignition phenomenon of carbides and found the following. That is, no fire is generated in the carbonization step, and a fire is generated in the cooling step. In the cooling process, the generation of combustible gas decreases with the decrease in the temperature of the carbides, and the pressure in the carbonization chamber decreases, so that the pressure in the combustion chamber that continues combustion becomes relatively high, and the high-temperature combustion in the combustion chamber A phenomenon occurs in which the gas flows into the inside of the coking chamber or replaces the gas inside the coking chamber. Then, the carbide in the carbonization chamber was ignited by the oxygen in the combustion gas flowing into the carbonization chamber, and the ignited carbide remained in the interior of the carbide even after the entire operation was completed. When the door of the carbonization chamber is opened to remove the carbide and the carbonization chamber is opened to the atmosphere, outside air flows into the interior of the carbonization chamber to promote combustion, and as a result, smoke and flame are generated from the carbide. .

【0006】さらに、冷却工程での発火は次のようにし
て発生していた。従来の炭化処理方法では、冷却工程で
も炭化工程と同様に撹拌翼を駆動していたので、炭化さ
れて、細かく、軽くなった炭化物が撹拌翼により粉末状
に舞い上がって炭化室内を充満し、そこに、燃焼室の高
温の燃焼ガスが流入することによって、炭化物の粉末が
発火するのである。特に、冷却工程で炭化室の温度が高
いときは、炭化物から可燃性ガスの発生が継続している
ので、非常に発火しやすい条件がそろっている。そし
て、空間で発火した炭化物は撹拌により炭化室の底部に
堆積した炭化物の内部にも入りこみ、さらに、炭化物の
内部に入った発火した炭化物は周囲の炭化物の保温効果
によって、全運転終了後でも発火したままの状態で、火
種として炭化物中に残存していたのである。
Further, ignition in the cooling step has occurred as follows. In the conventional carbonization method, the stirring blades were driven in the cooling step in the same manner as in the carbonization step.Therefore, the carbonized, fine and light carbides flew up into powder by the stirring blades and filled the carbonization chamber. Then, when the high-temperature combustion gas in the combustion chamber flows, the carbide powder is ignited. In particular, when the temperature of the carbonization chamber is high in the cooling step, the condition in which the combustible gas continues to be generated from the carbide is extremely easy to ignite. Then, the carbide ignited in the space enters into the carbide deposited at the bottom of the carbonization chamber due to the agitation, and the ignited carbide entering the interior of the carbide ignites even after the entire operation is completed due to the heat retaining effect of the surrounding carbide. As it was, it remained in the carbide as a kind of fire.

【0007】以上の知見から、本発明における炭化室煙
道の構造は、次の通りの構成とした。すなわち、本発明
は、内部にごみを撹拌するための撹拌翼を有する炭化室
1と、その炭化室の近傍に配置される燃焼室3とを連通
させる炭化室煙道4の構造であって、前記炭化室1と前
記燃焼室3とは管状部材で接続され、前記管状部材に
は、気体の流れが一方向のみに可能で、逆方向からの流
れに対してはその流通を妨げる逆止ダンパ21が設けら
れていることを特徴とする炭化室煙道の構造である。
[0007] From the above findings, the structure of the carbonization chamber flue according to the present invention has the following configuration. That is, the present invention is a structure of a carbonization chamber flue 4 that connects a carbonization chamber 1 having a stirring blade for agitating refuse therein and a combustion chamber 3 arranged near the carbonization chamber, The carbonization chamber 1 and the combustion chamber 3 are connected by a tubular member, and the tubular member allows a gas flow in only one direction, and prevents a flow from the opposite direction from flowing through the non-return damper. 21 is a structure of a carbonization chamber flue characterized by having 21 provided.

【0008】[0008]

【作用】通常、炭化工程では炭化室の圧力は水柱で数十
から数百mmで燃焼室の圧力より高まり、炭化室内のご
みから発生した水蒸気や可燃性ガスは燃焼室へ流入し
て、高温処理される。炭化工程初期の水蒸気の発生によ
り、炭化室の内部はほぼ無酸素状態となるので、炭化運
転中に炭化室内部での発火は発生しない。冷却工程で
は、炭化室のごみ(炭化物)からのガスの発生が少なく
なり、次第に炭化室の圧力が低下して燃焼室の圧力以下
となるので、燃焼室と連通している炭化煙道から炭化室
内に燃焼室の燃焼ガスが流入し、または、炭化室内部の
ガスと置換する現象が起こる。しかし、本発明の炭化室
煙道の構造によれば、逆止弁によって(炭化室と燃焼室
に各々圧力計を設けた場合にあっては、各々の圧力計の
圧力差によって逆止ダンパが閉じられ)、炭化室への燃
焼室の燃焼ガス、または炭化室内部のガスとの置換現象
は発生しないため、発火は発生しにくい。さらに、発火
したとしても、炭化室内は密閉状態で酸素の流入はない
ので火種は消える。
Normally, in the carbonization step, the pressure in the carbonization chamber is higher than the pressure in the combustion chamber by several tens to several hundreds of millimeters of water, and the steam and combustible gas generated from the refuse in the carbonization chamber flow into the combustion chamber and become hot. It is processed. Since the inside of the carbonization chamber becomes almost anoxic due to the generation of steam in the early stage of the carbonization step, no ignition occurs in the carbonization chamber during the carbonization operation. In the cooling step, the generation of gas from the dust (carbide) in the carbonization chamber decreases, and the pressure in the carbonization chamber gradually decreases to become equal to or lower than the pressure in the combustion chamber. A phenomenon occurs in which the combustion gas in the combustion chamber flows into the chamber or replaces the gas in the carbonization chamber. However, according to the structure of the flue gas chamber of the present invention, the check valve is provided by a check valve (when a pressure gauge is provided in each of the carbonization chamber and the combustion chamber, the check damper is formed by a pressure difference between the respective pressure gauges). (Closed), and there is no replacement of the combustion gas in the combustion chamber with the gas in the combustion chamber or the gas inside the carbonization chamber. Furthermore, even if it ignites, the fire extinguishes because the inside of the carbonization chamber is closed and there is no oxygen inflow.

【0009】[0009]

【発明の実施の形態】本発明の実施の形態を更に具体的
に説明する。図1は、本発明の一実施例の炭化装置の構
成図である。図示したごみ炭化装置は、生ごみ、紙類、
木材、紙おむつ等の可燃性のごみ20を収納する炭化室
1と、炭化室1を囲むように形成され加熱用の加熱機1
1を備えた加熱室2と、炭化室1とは炭化室煙道4で連
通し、ごみ20から発生した可燃性ガス等を燃焼させる
ための燃焼機12を備えた燃焼室3と、加熱室2の排ガ
スを排出するための加熱室煙道5及び燃焼室3の排ガス
を排出するための燃焼室煙道6にそれぞれ連通する排気
筒7とから構成され、燃焼室3には燃焼促進用の二次空
気を供給する二次空気ファン13が接続して設けられて
いる。また、炭化室1の内部には、ごみ20を撹拌する
ための撹拌翼8が設けられ、モータ9により、駆動伝達
部10を介して駆動される。ここで、炭化室煙道4の内
部には、開閉可能な逆止ダンパ21が設けられ、炭化室
1からの可燃性ガスと、燃焼室3からの燃焼ガスの置換
を防止している。また加熱室2には、冷却ファン14が
設けられており、燃焼室煙道6には排ガス温度低減用の
希釈ファン15が設けられている。さらに、炭化室1に
は炭化室1の温度を測定する温度測定装置(図示せず)
が配置され、燃焼室3にも温度測定装置(図示せず)が
配置されて、炭化装置の運転制御を行う制御盤17も備
えられている。
Embodiments of the present invention will be described more specifically. FIG. 1 is a configuration diagram of a carbonizing apparatus according to one embodiment of the present invention. The illustrated garbage carbonizers are garbage, paper,
A carbonization chamber 1 for storing combustible waste 20 such as wood and disposable diapers, and a heating machine 1 formed to surround the carbonization chamber 1 for heating.
A heating chamber 2 provided with a combustion chamber 3 provided with a combustion chamber 12 for burning combustible gas and the like generated from the refuse 20; 2 and an exhaust pipe 7 communicating with a combustion chamber flue 6 for discharging exhaust gas from the combustion chamber 3, respectively. The combustion chamber 3 includes a flue gas for promoting combustion. A secondary air fan 13 for supplying secondary air is connected and provided. Further, a stirring blade 8 for stirring the dust 20 is provided inside the carbonization chamber 1, and is driven by a motor 9 via a drive transmission unit 10. Here, a check damper 21 that can be opened and closed is provided inside the flue gas chamber 4 to prevent replacement of combustible gas from the combustion chamber 1 with combustion gas from the combustion chamber 3. The heating chamber 2 is provided with a cooling fan 14, and the combustion chamber flue 6 is provided with a dilution fan 15 for reducing exhaust gas temperature. Further, a temperature measuring device (not shown) for measuring the temperature of the carbonization chamber 1 is provided in the carbonization chamber 1.
, A temperature measuring device (not shown) is also disposed in the combustion chamber 3, and a control panel 17 for controlling the operation of the carbonizing device is also provided.

【0010】図1の装置により運転を開始すると、炭化
室1に設置した温度測定装置(図示せず)で炭化室1の
温度を測定しながら、その温度が一定になるように加熱
機11の燃焼をオン/オフ(ON/OFF)等で制御し
ながら、ごみを炭化する炭化運転が行われる。撹拌翼8
は炭化運転開始と同時か、数十分遅れて連続駆動され、
ごみ20を撹拌して伝熱を促進する。図2は炭化室煙道
の断面図であり、図3、図4は逆止ダンパ21の斜視図
である。炭化室煙道4の管内には、開閉可能な逆止ダン
パ21が配置されている。逆止ダンパ21は、円形状の
ものを略中央部で2分割し、右弁体22と左弁体23は
数個の自在金具24により、接合されている。自在金具
の中央部には、逆止ダンパ21を固定するための支持用
ピン27が貫通している。装置を運転していない場合
は、右弁体22と左弁体23は、炭化煙道4の内壁面に
設けられたリブ25と密着しており、炭化室1と燃焼室
3はこの逆止ダンパ21により仕切られた状態となる。
When the operation is started by the apparatus shown in FIG. 1, the temperature of the coking chamber 1 is measured by a temperature measuring device (not shown) installed in the coking chamber 1, and the heating device 11 is controlled so as to keep the temperature constant. A carbonization operation for carbonizing refuse is performed while controlling combustion by ON / OFF (ON / OFF) or the like. Stirring blade 8
Is driven simultaneously with the start of carbonization operation or several ten minutes later,
Stir the refuse 20 to promote heat transfer. FIG. 2 is a cross-sectional view of the flue gas stack, and FIGS. 3 and 4 are perspective views of the check damper 21. A check damper 21 which can be opened and closed is disposed in the tube of the coking chamber flue 4. The check damper 21 is formed by dividing a circular one into two substantially at the center, and the right valve body 22 and the left valve body 23 are joined by several free metal fittings 24. A support pin 27 for fixing the check damper 21 passes through the center of the universal fitting. When the apparatus is not operating, the right valve body 22 and the left valve body 23 are in close contact with the ribs 25 provided on the inner wall surface of the carbonized flue 4 and the carbonized chamber 1 and the combustion chamber 3 are checked by this check. It is in a state of being partitioned by the damper 21.

【0011】一方、炭化運転中においては、炭化室1の
方が、燃焼室3よりも圧力は高い状態であり、炭化室煙
道4に配置した逆止ダンパ21は炭化室1からの圧力に
より、右弁体22と左弁体23は押し上げられ、リブ2
5と夫々の弁体との隙間より可燃性のガスは燃焼室へと
流入し、燃焼室3に設けた燃焼機12により燃焼され
る。約4〜8時間炭化運転を継続し可燃性有機物20の
炭化が終了すると、炭化物を冷却するため、加熱機11
の燃焼が停止すると共に、加熱機11のファンと冷却フ
ァン14が駆動し、炭化室1を周囲から空冷する。この
冷却運転にはいると、炭化室1は冷却されるため、炭化
室1からの可燃性ガスの発生量は徐々に減少するととも
に、炭化室1と燃焼室3の圧力差もなくなってくるた
め、炭化室煙道4内の逆止ダンパ21の弁体は、押し上
げられなくなり、リブと密着し、炭化室1から燃焼室3
への可燃性ガスの流入はなくなる。すなわち、燃焼室3
の燃焼ガスと炭化室1からの可燃性ガスの置換はなくな
る。その後、炭化室1の温度が所定の温度になったとき
に全運転は終了し、炭排出口19から炭化物を排出す
る。
On the other hand, during the carbonization operation, the pressure in the carbonization chamber 1 is higher than the pressure in the combustion chamber 3, and the check damper 21 disposed in the flue 4 of the carbonization chamber depends on the pressure from the carbonization chamber 1. , Right valve body 22 and left valve body 23 are pushed up, and rib 2
The flammable gas flows into the combustion chamber from the gaps between the fuel cell 5 and the respective valve elements, and is combusted by the combustor 12 provided in the combustion chamber 3. When the carbonization operation is continued for about 4 to 8 hours and the carbonization of the combustible organic matter 20 is completed, the heating machine 11 is used to cool the carbide.
Is stopped, and the fan of the heater 11 and the cooling fan 14 are driven to cool the carbonization chamber 1 from the surroundings. During this cooling operation, the carbonized chamber 1 is cooled, so that the amount of combustible gas generated from the carbonized chamber 1 gradually decreases, and the pressure difference between the carbonized chamber 1 and the combustion chamber 3 disappears. The valve body of the check damper 21 in the flue 4 of the coking chamber cannot be pushed up, and is in intimate contact with the rib.
No inflammable gas flows into the tank. That is, the combustion chamber 3
There is no replacement of the combustible gas from the carbonization chamber 1 with the combustion gas. Thereafter, when the temperature of the carbonization chamber 1 reaches a predetermined temperature, the entire operation ends, and the carbide is discharged from the coal discharge port 19.

【0012】図5は、本発明に係る別の例を示す炭化室
煙道部の断面構造を示す。炭化室1と燃焼室3には、そ
れぞれの圧力を検知するための炭化室圧力計27と燃焼
室圧力計28が設けられており、例えば炭化室の圧力を
P1、燃焼室の圧力をP2と仮定した場合、P1≦P2
のときは逆止ダンパ21が閉状態で、P1>P2の時は
逆止ダンパ21が開状態となるように、炭化室圧力計2
7と燃焼室圧力計28の値を検出するとともに、電気変
換して信号を出力させ、制御盤17に入力し、逆止ダン
パ21の開閉制御を行うものである。この逆止ダンパ2
1を開閉させる手段としては、電気に限らず油圧、空気
圧等を用いて開閉させる方法であってもよい。また、構
造として本考案では、両開きの構造としたが、片開きの
構造としてもよい。
FIG. 5 shows a sectional structure of a flue section of a coking chamber showing another example according to the present invention. The carbonization chamber 1 and the combustion chamber 3 are provided with a carbonization chamber pressure gauge 27 and a combustion chamber pressure gauge 28 for detecting respective pressures. For example, the pressure in the carbonization chamber is P1, and the pressure in the combustion chamber is P2. Assuming, P1 ≦ P2
, The non-return damper 21 is in a closed state, and when P1> P2, the non-return damper 21 is in an open state.
7 and the value of the combustion chamber pressure gauge 28 are detected and converted into electric signals to output signals, which are input to the control panel 17 to control the opening and closing of the check damper 21. This check damper 2
The means for opening and closing 1 is not limited to electricity, but may be a method of opening and closing using hydraulic pressure, pneumatic pressure, or the like. Further, in the present invention, the structure is a double opening structure, but may be a single opening structure.

【0013】[0013]

【発明の効果】本発明によれば、炭化室に燃焼室からの
気体や熱気が逆流しないような逆止ダンパを炭化煙道に
設けたので、炭化室と燃焼室において燃焼ガスや可燃性
ガスあるいは酸素の置換が防止できるため炭化物の発火
はおこりにくく、万が一炭化物が発火しても、炭化室へ
の酸素の流入がないため炭化室の冷却が進むにつれて消
火するので、全運転終了時には火種は残らず、安全に炭
化物を取出すことができる。
According to the present invention, since the non-return damper for preventing the gas or hot air from the combustion chamber from flowing back in the carbonization chamber is provided in the carbonization flue, the combustion gas and the flammable gas in the carbonization chamber and the combustion chamber are provided. Alternatively, since the replacement of oxygen can be prevented, the ignition of the carbide is unlikely to occur.Even if the carbide is ignited, the fire extinguishes as the cooling of the carbonization chamber progresses because there is no inflow of oxygen into the carbonization chamber. It is possible to safely remove carbides without leaving.

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

【図1】本発明の一例の炭化装置の正面断面図。FIG. 1 is a front sectional view of a carbonizing apparatus according to an example of the present invention.

【図2】炭化室煙道の断面図FIG. 2 is a cross-sectional view of a carbonization chamber flue.

【図3】逆止ダンパの閉状態の斜視図。FIG. 3 is a perspective view of the check damper in a closed state.

【図4】逆止ダンパの開状態の斜視図。FIG. 4 is a perspective view of the check damper in an open state.

【図5】本発明の別の例の炭化装置の正面断面図。FIG. 5 is a front sectional view of another example of the carbonizing apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1:炭化室 2:加熱室 3:燃焼室 4:炭化室煙道 5:加熱室煙道 6:燃焼室煙道 7:排気筒 8:撹拌翼 9:モータ 10:駆動伝達部 11:第一バーナ 12:第二バーナ 13:二次空気ファン 14:冷却ファン 15:希釈ファン 17:制御盤 18:ごみ投入口 19:炭排出口 20:ごみ 21:逆止ダンパ 22:右弁体 23:左弁体 24:自在金具 25:リブ 26:支持用ピン 27:炭化室圧力計 28:燃焼室圧力計 1: Carbonization room 2: Heating room 3: Combustion room 4: Carbonization room flue 5: Heating room flue 6: Combustion room flue 7: Exhaust stack 8: Stirrer blade 9: Motor 10: Drive transmission unit 11: First Burner 12: Second burner 13: Secondary air fan 14: Cooling fan 15: Dilution fan 17: Control panel 18: Waste inlet 19: Charcoal outlet 20: Waste 21: Check damper 22: Right valve 23: Left Valve body 24: Swivel fitting 25: Rib 26: Support pin 27: Carbonization chamber pressure gauge 28: Combustion chamber pressure gauge

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23G 5/16 ZAB F23G 5/16 ZABB 5/50 ZAB 5/50 ZABP Fターム(参考) 3K061 AB02 AC01 CA01 FA21 3K062 AA23 AB02 AC01 BA02 CB03 DA12 DB30 3K078 BA02 CA02 CA07 CA11 4D004 AA03 AA12 CA15 CA26 CA32 CB04 CB28 CB34 CB37 DA01 DA02 DA06 DA07 DA20 4H012 HA02 JA03 JA11 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) F23G 5/16 ZAB F23G 5/16 ZABB 5/50 ZAB 5/50 ZABP F-term (Reference) 3K061 AB02 AC01 CA01 FA21 3K062 AA23 AB02 AC01 BA02 CB03 DA12 DB30 3K078 BA02 CA02 CA07 CA11 4D004 AA03 AA12 CA15 CA26 CA32 CB04 CB28 CB34 CB37 DA01 DA02 DA06 DA07 DA20 4H012 HA02 JA03 JA11

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】撹拌翼を有する炭化室と、その炭化室の近
傍に配置される燃焼室とを連通させる炭化室煙道の構造
であって、 前記炭化室と前記燃焼室とは管状部材で接続され、 前記管状部材の内部には逆止ダンパが設けられている、
炭化室煙道の構造。
1. A carbonization chamber flue structure for communicating a carbonization chamber having a stirring blade and a combustion chamber disposed near the carbonization chamber, wherein the carbonization chamber and the combustion chamber are tubular members. Connected, a check damper is provided inside the tubular member,
Structure of coking chamber flue.
【請求項2】炭化室と燃焼室には各々圧力計を設け、各
々の圧力計の圧力差により逆止ダンパの開閉を行う、請
求項1の炭化室煙道の構造。
2. The structure of the carbonization chamber flue according to claim 1, wherein a pressure gauge is provided in each of the carbonization chamber and the combustion chamber, and the check damper is opened and closed by a pressure difference between the respective pressure gauges.
JP2000319506A 2000-10-19 2000-10-19 Structure of carbonization chamber flue and carbonization device Pending JP2002121562A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000319506A JP2002121562A (en) 2000-10-19 2000-10-19 Structure of carbonization chamber flue and carbonization device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000319506A JP2002121562A (en) 2000-10-19 2000-10-19 Structure of carbonization chamber flue and carbonization device

Publications (1)

Publication Number Publication Date
JP2002121562A true JP2002121562A (en) 2002-04-26

Family

ID=18797956

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000319506A Pending JP2002121562A (en) 2000-10-19 2000-10-19 Structure of carbonization chamber flue and carbonization device

Country Status (1)

Country Link
JP (1) JP2002121562A (en)

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