JPH10286544A - Apparatus for carbonization-reduction of waste - Google Patents

Apparatus for carbonization-reduction of waste

Info

Publication number
JPH10286544A
JPH10286544A JP9115276A JP11527697A JPH10286544A JP H10286544 A JPH10286544 A JP H10286544A JP 9115276 A JP9115276 A JP 9115276A JP 11527697 A JP11527697 A JP 11527697A JP H10286544 A JPH10286544 A JP H10286544A
Authority
JP
Japan
Prior art keywords
waste
partition wall
carbonization
bulkhead
outlet
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
JP9115276A
Other languages
Japanese (ja)
Other versions
JP3787216B2 (en
Inventor
Kazuhiko Kawatsu
一彦 川津
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.)
ACTREE Corp
Original Assignee
ACTREE Corp
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 ACTREE Corp filed Critical ACTREE Corp
Priority to JP11527697A priority Critical patent/JP3787216B2/en
Publication of JPH10286544A publication Critical patent/JPH10286544A/en
Application granted granted Critical
Publication of JP3787216B2 publication Critical patent/JP3787216B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Coke Industry (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)

Abstract

PROBLEM TO BE SOLVED: To heat waste efficiently by using high-frequency to carbonization- reduction temperatures in an apparatus for carbonization-reducing waste by using a rotary kiln. SOLUTION: The apparatus is provided with a rotating drum 2 slightly inclining from the horizontal axis, an inflow side partition wall 3 and an outflow side partition wall 4 fixed and closing the both ends of the rotating drum, a waste feeder penetrating the inflow side partition wall 3, a discharging conveyer connecting to a discharging port 33 opening to the bottom part of the outflow side partition wall 4, a columnar heat apparatus 5 supported by penetrating the both partition walls 3, 4, an incombustible gas-feeding port 35 provided on at least one side of the partition walls 3, 4, and a reduction gas-exhausting cylinder 31. The heating apparatus 5 is provided with a metallic shell cylinder 23, a high-frequency coil 25 composed of a hollow wire provided with keeping a slight gap to the inside face of the metallic shell cylinder 23, and an electrically and thermally insulating material 26 supporting the high-frequency coil. Accordingly, high-frequency current is applied to the coil 25 and cooling water is flowed into a hollow hole of the hollow wire. The metallic shell cylinder 23 is heated at high temperature by induction heating action.

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】この発明は、回転炉を用いて
廃棄物を炭化・還元する装置に関するもので、特に廃棄
物を乾燥及び炭化させることやダイオキシン等有害物を
還元雰囲気で分解させる加熱手段に特徴がある加熱装置
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for carbonizing and reducing waste using a rotary furnace, and more particularly to a heating means for drying and carbonizing waste and decomposing harmful substances such as dioxin in a reducing atmosphere. The present invention relates to a heating device characterized in that:

【0002】[0002]

【従来の技術】廃棄物は通常焼却処理されている場合が
殆どで、このような焼却処理では、酸素によって燃焼が
行われるので、酸素を供給する為に大量の空気を必要と
する(空気中の酸素が21%であることと、空気過剰率
が約1.8倍となるため)。これにより燃焼排気ガスは
大量に発生し、窒素酸化物、硫黄酸化物、塩化水素、炭
酸ガス等の有害な副生成物が発生し、これらを除去する
為に排気ガス処理装置が大きく複雑になり、コスト的に
も不利になる。
2. Description of the Related Art Waste is usually incinerated in most cases. In such incineration, a large amount of air is required to supply oxygen because combustion is performed by oxygen (in the air). Is 21% and the excess air ratio is about 1.8 times). As a result, a large amount of combustion exhaust gas is generated, and harmful by-products such as nitrogen oxides, sulfur oxides, hydrogen chloride, and carbon dioxide gas are generated. This is disadvantageous in terms of cost.

【0003】また、重油等の助燃材を用いないで廃棄物
を完全燃焼させ、悪臭や有害な燃焼ガスの発生を極力抑
制した装置として、廃棄物を減圧マイクロ波加熱により
乾燥し、水分を除去した廃棄物を燃焼室に送って酸素焼
却を行うという焼却装置が、特開平7−233931号
公報に開示されている。この装置は、燃焼室の前段に置
かれた乾燥室において、マイクロ波加熱により水分を含
んだ廃棄物を内部から加熱して乾燥させた後、乾燥室か
ら燃焼室に移送して焼却しようとするものであり、マイ
クロ波加熱を乾燥手段として用いることは、たとえば木
材の乾燥等において従来から用いられているものであ
る。
Further, as a device for completely burning waste without using a combustion aid such as heavy oil and suppressing generation of offensive odor and harmful combustion gas, the waste is dried by microwave heating under reduced pressure to remove moisture. An incinerator in which waste waste is sent to a combustion chamber for oxygen incineration is disclosed in Japanese Patent Application Laid-Open No. Hei 7-233931. In this drying apparatus, waste containing water is heated and dried from the inside by microwave heating in a drying chamber placed in front of the combustion chamber, and then transferred from the drying chamber to the combustion chamber for incineration. The use of microwave heating as a drying means has been conventionally used for drying wood, for example.

【0004】また特開昭59−109131号公報に
は、このようなマイクロ波加熱を用いた回転キルン型の
乾燥炉による茶葉の乾燥装置が提唱されている。これら
の装置における加熱原理は、高周波電流による誘導作用
を利用して、被加熱物を内部から加熱するというもので
あり、被加熱物を(表面のみでなく)内部まで均一に乾
燥することができるという特徴がある。
Japanese Patent Laid-Open Publication No. Sho 59-109131 proposes a device for drying tea leaves using a rotary kiln type drying furnace using microwave heating. The heating principle in these devices is to heat an object to be heated from the inside by using an induction action by a high-frequency current, and the object to be heated can be uniformly dried to the inside (not only the surface). There is a feature.

【0005】[0005]

【発明が解決しようとする課題】この発明は、廃棄物を
乾燥するとともにより高温に加熱して、悪臭や有害ガス
を発生させることなく炭化・還元することができる装置
を得ることを課題としており、高周波を用いて廃棄物を
より効率良く炭化・還元温度にまで加熱することができ
る加熱手段を備えた廃棄物の炭化・還元装置を得ること
を課題としている。
SUMMARY OF THE INVENTION It is an object of the present invention to provide an apparatus which can dry and heat a waste material to a higher temperature and carbonize and reduce it without generating a bad odor or a harmful gas. It is another object of the present invention to provide a waste carbonization / reduction apparatus provided with a heating means capable of heating waste to a carbonization / reduction temperature more efficiently using high frequency.

【0006】[0006]

【課題を解決するための手段】請求項1記載の廃棄物の
炭化・還元装置は、水平軸から若干傾斜して支持した回
転胴2と、この回転胴の両端を閉鎖する固定の流入側隔
壁3及び流出側隔壁4と、流入側隔壁3を貫通して回転
胴2内に廃棄物を供給するフィーダ28と、流出側隔壁
4の底部に開口する排出口33に連通する排出コンベア
34と、流入側隔壁3及び流出側隔壁4を貫通して当該
両隔壁3、4で支持された円柱ないし多角柱状の加熱装
置5と、流入側隔壁3及び流出側隔壁4の少なくともい
ずれか一方に設けられた不燃ガス供給口35及び還元ガ
ス排気筒31とを備え、加熱装置5は金属殻筒23とこ
の金属殻筒の内面に若干間隔を隔てて配置された中空素
線からなる高周波コイル25と、この高周波コイルを所
定位置に保持する絶縁性断熱材26とを備え、前記コイ
ル25には高周波電流が印加されるとともに、その中空
孔に冷却水が通水されることを特徴とするものである。
According to a first aspect of the present invention, there is provided an apparatus for carbonizing and reducing waste, comprising: a rotating drum 2 supported at a slight inclination from a horizontal axis; and a fixed inflow-side partition for closing both ends of the rotating drum. A feeder 28 that feeds waste into the rotating drum 2 through the inlet-side partition 3 and a discharge conveyor 34 that communicates with a discharge port 33 that opens at the bottom of the outlet-side partition 4; A cylindrical or polygonal heating device 5 that penetrates the inflow-side partition wall 3 and the outflow-side partition wall 4 and is supported by the partition walls 3 and 4 is provided on at least one of the inflow-side partition wall 3 and the outflow-side partition wall 4. The heating device 5 comprises a metal shell 23 and a high-frequency coil 25 composed of a hollow wire arranged at a slight distance from the inner surface of the metal shell, Hold this high frequency coil in place And a rim of the heat insulating material 26, together with the high-frequency current is applied to the coil 25, in the hollow hole cooling water is characterized in being passed through.

【0007】請求項2記載の発明は、請求項1記載の廃
棄物の炭化・還元装置において、フィーダ28及び排出
コンベア34がスクリューフィーダ及びスクリューコン
ベアであることを特徴とするものである。
According to a second aspect of the present invention, in the waste carbonizing and reducing apparatus according to the first aspect, the feeder 28 and the discharge conveyor 34 are a screw feeder and a screw conveyor.

【0008】[0008]

【作用】軸線が傾斜した回転胴2の回転により、フィー
ダ28によって回転胴2内に供給された廃棄物36は、
撹拌されながら流出側へゆっくりと移送される。高周波
コイル25に高周波電流を通電することにより、誘導加
熱作用で金属殻筒23が加熱される。廃棄物36は回転
胴2内の上流側部分を移動する間に、金属殻筒23から
の主として輻射熱によって加熱され、外表面から水分が
蒸散して乾燥していく。外表面が乾燥した廃棄物は、金
属殻筒23からの輻射熱によってさらに加熱され、炭化
・還元する。炭化・還元によって生ずる還元ガスは、金
属殻筒23とともに廃棄物36の乾燥と炭化・還元とを
助長する。またこの炭化・還元に伴い廃棄物の内部の水
も蒸散して炭化・還元が進み、回転胴2の回転に伴って
撹拌されながら流出側へゆっくりと移送され、残った炭
化材が排出口33を通って排出コンベア34により搬出
される。この排出コンベア34による搬出過程で、炭化
材が冷却される。また、通電抵抗によって生ずる高周波
コイル25の素線の発熱は、中空孔を流れる水によって
冷却される。
The waste 36 supplied into the rotary drum 2 by the feeder 28 due to the rotation of the rotary drum 2 whose axis is inclined,
It is slowly transferred to the outflow side while being stirred. When a high-frequency current is applied to the high-frequency coil 25, the metal shell 23 is heated by the induction heating action. The waste 36 is heated mainly by the radiant heat from the metal shell 23 while moving on the upstream side portion in the rotary drum 2, and the moisture evaporates from the outer surface and dries. The waste whose outer surface is dried is further heated by radiant heat from the metal shell 23 and carbonized and reduced. The reducing gas generated by the carbonization / reduction together with the metal shell 23 promotes the drying of the waste 36 and the carbonization / reduction. In addition, the water inside the waste evaporates due to the carbonization and reduction, and the carbonization and reduction proceeds. The carbonized material is slowly transferred to the outflow side while being stirred with the rotation of the rotary drum 2, and the remaining carbonized material is discharged to the outlet 33 Through the discharge conveyor 34. During the unloading process by the discharge conveyor 34, the carbonized material is cooled. Further, the heat generated by the wires of the high-frequency coil 25 caused by the current-carrying resistance is cooled by the water flowing through the hollow holes.

【0009】この発明の装置では、高周波電流の誘導加
熱作用すなわち高周波コイル25に高周波電流を流すこ
とによって、導体である金属殻筒23内に生ずる渦電流
の電気抵抗によって金属殻筒23が高温に加熱されるこ
とを利用して、廃棄物36の乾燥と炭化・還元とを行っ
ており、廃棄物を効率良く炭化・還元に必要な高温度に
加熱することが可能である。また回転胴2の回転による
撹拌作用で、均一な乾燥及び燃焼が可能であるととも
に、炉内温度に応じて高周波コイル25への通電量を制
御することにより、炭化・還元温度を所望温度に正確に
維持することができる。
In the apparatus according to the present invention, the induction heating action of the high-frequency current, that is, the flow of the high-frequency current through the high-frequency coil 25 causes the electric resistance of the eddy current generated in the metal shell 23 as a conductor to raise the temperature of the metal shell 23 to a high temperature. By utilizing the heating, the waste 36 is dried and carbonized / reduced, and the waste can be efficiently heated to a high temperature required for carbonization / reduction. In addition, uniform drying and combustion can be performed by the stirring action by the rotation of the rotating drum 2, and the amount of electricity supplied to the high-frequency coil 25 is controlled according to the furnace temperature, so that the carbonization / reduction temperature can be accurately adjusted to a desired temperature. Can be maintained.

【0010】回転胴2内の廃棄物36は、回転胴2内に
この回転胴とほぼ平行に配置された円柱ないし多角柱状
の加熱装置5で加熱されるので、外部への熱の放散が少
なく、熱効率が向上する。高周波コイル25を絶縁性断
熱材26で保持することにより、金属殻筒23の内側へ
の放熱も抑制することができる。
The waste 36 in the rotary drum 2 is heated by the cylindrical or polygonal column heating device 5 disposed in the rotary drum 2 substantially in parallel with the rotary drum, so that heat is less radiated to the outside. , Improve thermal efficiency. By holding the high-frequency coil 25 with the insulating heat insulating material 26, heat radiation to the inside of the metal shell 23 can also be suppressed.

【0011】フィーダ28及び排出コンベア34として
スクリューフィーダ及びスクリューコンベアを用いたも
のは、廃棄物及び灰がコンベア内を充満して搬送される
ことにより、特別な密封装置を用いることなくフィーダ
や排出コンベアの空間を通って回転胴内に空気が流入す
るのを防止できる。なお、炭化・還元中においては、空
気の流入を防ぐために、炉内は若干正圧に維持される。
In the case where a screw feeder and a screw conveyor are used as the feeder 28 and the discharge conveyor 34, waste and ash are filled and conveyed inside the conveyor, so that the feeder and the discharge conveyor can be used without using a special sealing device. Air can be prevented from flowing into the rotating drum through the space. During the carbonization and reduction, the inside of the furnace is maintained at a slightly positive pressure in order to prevent the inflow of air.

【0012】[0012]

【発明の実施の形態】以下図面に示す実施例を参照して
この発明の実施の形態を説明する。図1は回転炉の断面
図、図2は図1のA部断面図、図3は装置全体の側面
図、図4は同平面図である。
Embodiments of the present invention will be described below with reference to embodiments shown in the drawings. 1 is a sectional view of a rotary furnace, FIG. 2 is a sectional view of a part A in FIG. 1, FIG. 3 is a side view of the entire apparatus, and FIG.

【0013】回転炉1は回転胴2と流入側及び流出側隔
壁3、4と加熱装置5とで構成される。回転胴2は両側
に肉厚の鍔6を有しており、この鍔6を架台7に設けた
ローラ8(8a,8b)で支持することにより、回転自
在に支持されている。ローラ8は上流側のもの8aが若
干高い位置にあり、従って回転胴2は上流側から下流側
へと若干低くなるように傾斜している。回転胴2にはま
たスプロケット9が固着されており、架台7に装着した
電動機10の出力軸とこのスプロケットとをチェーンで
連結することにより、回転胴2が回転駆動される。
The rotary furnace 1 comprises a rotary drum 2, inflow and outflow partition walls 3 and 4, and a heating device 5. The rotating drum 2 has thick flanges 6 on both sides, and is supported rotatably by supporting the flanges 6 with rollers 8 (8a, 8b) provided on a gantry 7. The roller 8 is slightly higher than the roller 8a on the upstream side, so that the rotary drum 2 is inclined so as to be slightly lower from the upstream side to the downstream side. A sprocket 9 is also fixed to the rotating drum 2, and the rotating drum 2 is rotationally driven by connecting an output shaft of an electric motor 10 mounted on the gantry 7 and the sprocket with a chain.

【0014】回転胴2は主要な強度部材である円筒状の
鉄板11の内面に、断熱材層12と耐火材層13を設け
た三層構造をしており、さらに鉄板11の外側の前記鍔
6及びスプロケット9の装着しないところには、断熱材
14が装着されている。回転胴2の内側には廃棄物を掻
き上げるための軸方向に細長い掻上羽根15が装着され
ている。
The rotary drum 2 has a three-layer structure in which a heat insulating material layer 12 and a refractory material layer 13 are provided on the inner surface of a cylindrical iron plate 11 which is a main strength member. A heat insulating material 14 is mounted where no sprocket 6 and sprocket 9 are mounted. An axially elongated scraping blade 15 for scraping up waste is mounted inside the rotating drum 2.

【0015】回転胴2の両端を閉鎖する流入側隔壁3及
び流出側隔壁4は、架台7に固定的に設けられている。
流入側隔壁3及び流出側隔壁4と回転胴2との間には、
回転シール16及び17が設けられて炉内からのガスの
漏出を防止している。回転シール16及び17は、耐熱
性の紐状のシール材を巻回したもので、押え板18及び
19で軸方向に挟み込んで回転シール16、17を保持
している。
The inflow-side partition wall 3 and the outflow-side partition wall 4 that close both ends of the rotary drum 2 are fixedly provided on a gantry 7.
Between the inflow-side bulkhead 3 and the outflow-side bulkhead 4 and the rotary drum 2,
Rotary seals 16 and 17 are provided to prevent gas leakage from inside the furnace. The rotary seals 16 and 17 are formed by winding a heat-resistant string-like seal material, and are held between the pressing plates 18 and 19 in the axial direction to hold the rotary seals 16 and 17.

【0016】加熱装置5は円柱状でその両端を流入側隔
壁3及び流出側隔壁4に設けたヒータ装着孔20、21
を貫通した状態で支持されている。この円柱状の加熱装
置5は流入側隔壁3側で軸方向に固定され、点検等をす
るときは流出側隔壁4側に引き抜くことができるように
なっており、そのために流出側隔壁4のヒータ装着孔2
1は若干径大で、その隙間から炉内ガスが漏れるのを防
止するために、流出側隔壁4と回転胴2との間に設けた
と同様な回転シール22が設けられている。
The heating device 5 has a cylindrical shape and has both ends provided on the inflow-side partition 3 and the outflow-side partition 4 with heater mounting holes 20 and 21.
Is supported in a state where it passes through. The cylindrical heating device 5 is fixed in the axial direction on the inflow side partition 3 side, and can be pulled out to the outflow side partition 4 side for inspection or the like. Mounting hole 2
1 has a slightly larger diameter, and is provided with a rotary seal 22 similar to that provided between the outflow-side partition 4 and the rotary drum 2 in order to prevent the gas in the furnace from leaking from the gap.

【0017】加熱装置5は円柱状の金属殻筒23の内側
に当該金属殻筒と若干間隙24aを隔てて銅パイプを巻
回した高周波コイル25を配置し、このコイルの内側及
び前記金属殻筒との間の間隙24、24aにセラミック
ファイバー製の断熱材26を充填した構造である。高周
波コイル25には高周波発振器から高周波電流が印加さ
れ、また銅パイプの中空孔には冷却水が供給されるよう
になっている。
The heating device 5 has a high-frequency coil 25 around which a copper pipe is wound with a slight gap 24a disposed between the metal shell tube 23 and the inside of the cylindrical metal shell tube 23. Is filled with a heat insulating material 26 made of ceramic fiber. A high-frequency current is applied to the high-frequency coil 25 from a high-frequency oscillator, and cooling water is supplied to the hollow hole of the copper pipe.

【0018】回転炉1の上流側の架台7a上には、基端
にホッパ27を設けたスクリューフィーダ28が設けら
れており、このフィーダの先端は、回転炉の上流側隔壁
3を貫通して回転胴2内に開口している。このスクリュ
ーフィーダ28の配置スペースを確保するため、加熱装
置5は図2に示すように回転炉1の中心から若干偏倚し
ている。ホッパ27の側方(図3の紙面手前側)には、
作業台29とこの作業台に上がるための梯子30が設け
られている。流入側隔壁3の上方部には、回転炉内に連
通する還元ガス排気筒31が設けられている。
A screw feeder 28 provided with a hopper 27 at a base end is provided on a pedestal 7a on the upstream side of the rotary furnace 1, and a tip of the screw feeder penetrates the upstream partition 3 of the rotary furnace. It is open in the rotating drum 2. In order to secure an arrangement space for the screw feeder 28, the heating device 5 is slightly offset from the center of the rotary furnace 1 as shown in FIG. On the side of the hopper 27 (on the front side of FIG. 3),
A work table 29 and a ladder 30 for ascending the work table are provided. Above the inflow-side partition 3, a reducing gas exhaust pipe 31 communicating with the inside of the rotary furnace is provided.

【0019】流出側隔壁4は壁面に回転胴2に設けたと
同様な断熱材層12及び耐火材層13を設けた空室32
を有しており、回転胴2の流出側端部は、この空室に若
干差し込まれた状態で支持されている。空室32の下端
には排出口33が設けられ、この排出口に排出用スクリ
ューコンベア34が連接されている。排出用スクリュー
コンベア34は斜め上方に向かって延びており、排出口
33から落下する炭化材を斜め上方に持ち上げるように
して排出する。また流出側隔壁4には炉内に連通する不
燃ガス供給口35が設けられている。
The outflow-side partition 4 has a vacant space 32 in which a heat insulating material layer 12 and a refractory material layer 13 similar to those provided on the rotary drum 2 are provided on the wall surface.
The outflow-side end of the rotary drum 2 is supported in a state where it is slightly inserted into the empty space. A discharge port 33 is provided at the lower end of the empty room 32, and a discharge screw conveyor 34 is connected to this discharge port. The discharge screw conveyor 34 extends obliquely upward, and discharges the carbon material falling from the discharge port 33 so as to lift diagonally upward. The outlet side partition wall 4 is provided with a non-combustible gas supply port 35 communicating with the inside of the furnace.

【0020】炭化・還元しようとする廃棄物はホッパ2
7に投入され、スクリューフィーダ28によって回転胴
2内に送られる。回転胴2は電動機10により図2で左
回りにゆっくりと回転駆動される。不燃ガス供給口35
からは、不燃ガスが炉内に供給され、加熱装置5の高周
波コイルには、高周波電流が印加され、かつその銅パイ
プの中空孔に冷却水が通水される。加熱装置の金属殻筒
23は高周波コイル25を流れる高周波の作用により誘
導加熱され、金属殻筒23の熱が主として輻射及び対流
により回転胴2内の廃棄物に伝熱され、廃棄物を炭化・
還元する。炭化・還元温度は高周波コイル25に流す電
流値により制御する。回転胴2の回転により回転胴内の
廃棄物は底部のものが上層へ掻き上げられるように撹拌
され、均一に炭化・還元される。非酸化性雰囲気中での
加熱により、廃棄物36が炭化・還元される。
The waste to be carbonized and reduced is hopper 2
7 and fed into the rotary drum 2 by the screw feeder 28. The rotating drum 2 is slowly driven to rotate counterclockwise in FIG. Incombustible gas supply port 35
After that, a non-combustible gas is supplied into the furnace, a high-frequency current is applied to the high-frequency coil of the heating device 5, and cooling water flows through the hollow hole of the copper pipe. The metal shell 23 of the heating device is induction-heated by the action of the high frequency current flowing through the high-frequency coil 25, and the heat of the metal shell 23 is transferred to the waste in the rotary drum 2 mainly by radiation and convection to carbonize the waste.
To reduce. The carbonization / reduction temperature is controlled by a current value flowing through the high-frequency coil 25. By the rotation of the rotary drum 2, the waste in the rotary drum is stirred such that the bottom is scraped up to the upper layer, and is uniformly carbonized and reduced. By heating in the non-oxidizing atmosphere, the waste 36 is carbonized and reduced.

【0021】回転胴2の傾斜により、回転胴内の廃棄物
は撹拌されつつ流出側へと移動する。そして流出側隔壁
の空室32に移動してきた廃棄物は、排出口33を通っ
て落下し、排出用スクリューコンベア34によって排出
される。ホッパ27が上方に向かって開口しており、ま
た排出用スクリューコンベア34が上方に向けて炭化材
を送り出す関係上、スクリューフィーダ28及び排出用
スクリューコンベア34は、炭化材で充填された状態と
なり、炉内ガスがホッパ27及び排出用スクリューコン
ベア34から流出するのを抑制している。
Due to the inclination of the rotary drum 2, the waste in the rotary drum moves to the outflow side while being stirred. Then, the waste that has moved to the empty room 32 of the outflow side partition wall falls through the discharge port 33 and is discharged by the discharge screw conveyor 34. The hopper 27 is open upward, and the screw feeder 28 and the discharge screw conveyor 34 are in a state of being filled with the carbon material because the discharge screw conveyor 34 sends the carbon material upward. Furnace gas is prevented from flowing out of the hopper 27 and the discharge screw conveyor 34.

【0022】この発明の装置では、以上の実施例で述べ
たように、フィーダから連続的に供給される廃棄物を、
回転炉内で炭化・還元して排出コンベアにより連続的に
排出するものであり、廃棄物を均一に炭化・還元するこ
とができるとともに、炭化・還元温度の制御が容易であ
る。またこの発明の構造の加熱装置を採用することによ
り、高温加熱が可能であるとともに、炭化・還元の制御
を正確に行うことができ、かつ炉外への熱の漏洩が少な
くて熱効率を向上させることができる。
In the apparatus of the present invention, as described in the above embodiment, the waste continuously supplied from the feeder is
It is carbonized and reduced in a rotary furnace and is continuously discharged by a discharge conveyor, so that the waste can be uniformly carbonized and reduced and the control of the carbonization and reduction temperature is easy. In addition, by employing the heating device having the structure of the present invention, high-temperature heating is possible, carbonization and reduction can be accurately controlled, and heat leakage to the outside of the furnace is reduced, thereby improving thermal efficiency. be able to.

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

【図1】実施例の回転炉の断面図FIG. 1 is a sectional view of a rotary furnace according to an embodiment.

【図2】図1のA部断面図FIG. 2 is a sectional view of a portion A in FIG.

【図3】実施例装置の全体側面図FIG. 3 is an overall side view of the apparatus according to the embodiment.

【図4】実施例装置の全体平面図FIG. 4 is an overall plan view of the apparatus of the embodiment.

【符号の説明】[Explanation of symbols]

2 回転胴 3 流入側隔壁 4 流出側隔壁 5 燃焼装置 23 金属殻筒 25 高周波コイル 26 絶縁性断熱材 28 フィーダ 31 還元ガス排気筒 33 排出口 34 排出コンベア 35 不燃ガス供給口 2 Revolving drum 3 Inlet-side bulkhead 4 Outlet-side bulkhead 5 Combustion device 23 Metal shell 25 High-frequency coil 26 Insulating heat insulating material 28 Feeder 31 Reducing gas exhaust 33 Outlet 34 Exhaust conveyor 35 Incombustible gas supply

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 水平軸から若干傾斜して支持した回転胴
(2) と、この回転胴の両端を閉鎖する固定の流入側隔壁
(3) 及び流出側隔壁(4) と、流入側隔壁(3)を貫通して
回転胴(2) 内に廃棄物を供給するフィーダ(28)と、流出
側隔壁(4) の底部に開口する排出口(33)に連通する排出
コンベア(34)と、流入側隔壁(3) 及び流出側隔壁(4) を
貫通して当該両隔壁(3,4) で支持された円柱ないし多角
柱状の加熱装置(5) と、流入側隔壁(3) 及び流出側隔壁
(4) の少なくともいずれか一方に設けられた不燃ガス供
給口(35)及び還元ガス排気筒(31)とを備え、加熱装置
(5) は金属殻筒(23)とこの金属殻筒の内面に若干間隔を
隔てて配置された中空素線からなる高周波コイル(25)
と、この高周波コイルを所定位置に保持する絶縁性断熱
材(26)とを備え、前記コイル(25)には高周波電流が印加
されるとともに、その中空孔に冷却水が通水されること
を特徴とする、廃棄物の炭化・還元装置。
1. A rotary drum supported slightly inclined from a horizontal axis.
(2) and a fixed inflow-side bulkhead that closes both ends of this rotating body
(3) and the outlet bulkhead (4), the feeder (28) that penetrates the inlet bulkhead (3) and supplies waste into the rotating drum (2), and an opening at the bottom of the outlet bulkhead (4). The discharge conveyor (34) communicating with the discharge outlet (33), and the cylindrical or polygonal column supported by the partition walls (3, 4) through the inlet partition wall (3) and the outlet partition wall (4). Heating device (5), inlet bulkhead (3) and outlet bulkhead
(4) a non-combustible gas supply port (35) and a reducing gas exhaust pipe (31) provided in at least one of the
(5) is a high-frequency coil (25) consisting of a metal shell (23) and a hollow wire arranged at a slight distance on the inner surface of the metal shell.
And an insulating heat insulating material (26) for holding the high-frequency coil in a predetermined position, and a high-frequency current is applied to the coil (25), and cooling water is passed through the hollow hole. Characterized by a carbonization and reduction device for waste.
【請求項2】 フィーダ(28)及び排出コンベア(34)がス
クリューフィーダ及びスクリューコンベアであることを
特徴とする、請求項1記載の廃棄物の炭化・還元装置。
2. The waste carbonization / reduction apparatus according to claim 1, wherein the feeder (28) and the discharge conveyor (34) are a screw feeder and a screw conveyor.
JP11527697A 1997-04-16 1997-04-16 Waste carbonization and reduction equipment Expired - Fee Related JP3787216B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11527697A JP3787216B2 (en) 1997-04-16 1997-04-16 Waste carbonization and reduction equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11527697A JP3787216B2 (en) 1997-04-16 1997-04-16 Waste carbonization and reduction equipment

Publications (2)

Publication Number Publication Date
JPH10286544A true JPH10286544A (en) 1998-10-27
JP3787216B2 JP3787216B2 (en) 2006-06-21

Family

ID=14658660

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11527697A Expired - Fee Related JP3787216B2 (en) 1997-04-16 1997-04-16 Waste carbonization and reduction equipment

Country Status (1)

Country Link
JP (1) JP3787216B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005076959A (en) * 2003-08-29 2005-03-24 Murata Mfg Co Ltd Continuous heat treatment equipment
JP2005169301A (en) * 2003-12-12 2005-06-30 Hitachi Chem Co Ltd Apparatus for heating and/or supplying powder or granulate
CN104501580A (en) * 2014-12-01 2015-04-08 咸阳华光窑炉设备有限公司 Electric-heating ultrahigh-temperature internal heating type rotary kiln
JP2019089037A (en) * 2017-11-16 2019-06-13 太平洋セメント株式会社 Clothing recycling device and method
CN109945644A (en) * 2019-05-08 2019-06-28 扬州新达锌业有限公司 A kind of finishing stove of high-density zinc oxide

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005076959A (en) * 2003-08-29 2005-03-24 Murata Mfg Co Ltd Continuous heat treatment equipment
JP2005169301A (en) * 2003-12-12 2005-06-30 Hitachi Chem Co Ltd Apparatus for heating and/or supplying powder or granulate
JP4600721B2 (en) * 2003-12-12 2010-12-15 日立化成工業株式会社 Powder and granule heating and supply equipment
CN104501580A (en) * 2014-12-01 2015-04-08 咸阳华光窑炉设备有限公司 Electric-heating ultrahigh-temperature internal heating type rotary kiln
JP2019089037A (en) * 2017-11-16 2019-06-13 太平洋セメント株式会社 Clothing recycling device and method
CN109945644A (en) * 2019-05-08 2019-06-28 扬州新达锌业有限公司 A kind of finishing stove of high-density zinc oxide
CN109945644B (en) * 2019-05-08 2023-10-27 扬州新达再生资源科技有限公司 High density zinc oxide's processing stove

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