JP2002012875A - Apparatus for carbonizing and reducing scrap wood - Google Patents

Apparatus for carbonizing and reducing scrap wood

Info

Publication number
JP2002012875A
JP2002012875A JP2000195047A JP2000195047A JP2002012875A JP 2002012875 A JP2002012875 A JP 2002012875A JP 2000195047 A JP2000195047 A JP 2000195047A JP 2000195047 A JP2000195047 A JP 2000195047A JP 2002012875 A JP2002012875 A JP 2002012875A
Authority
JP
Japan
Prior art keywords
reducing
combustion
waste wood
discharge
rotating drum
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
JP2000195047A
Other languages
Japanese (ja)
Inventor
Yuji Mizukoshi
裕治 水越
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.)
KANAHARA KAIHATSU KK
RYOSHIN SANGYO KK
ACTREE Corp
Original Assignee
KANAHARA KAIHATSU KK
RYOSHIN SANGYO KK
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 KANAHARA KAIHATSU KK, RYOSHIN SANGYO KK, ACTREE Corp filed Critical KANAHARA KAIHATSU KK
Priority to JP2000195047A priority Critical patent/JP2002012875A/en
Publication of JP2002012875A publication Critical patent/JP2002012875A/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
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/145Feedstock the feedstock being materials of biological origin
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Coke Industry (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an apparatus for efficiently carbonizing scrap wood at a low cost capable of reducing combustion air and gaseous carbon dioxide and providing a by-product from the scrap wood in relation to an incineration device for the scrap wood. SOLUTION: This apparatus for carbonizing and reducing the scrap wood is equipped with a crusher for crushing the scrap wood and feeding the crushed scrap wood, a feed hopper, a circular cylindrical or a prismatic radiant heating cylinder supported parallel to a rotating drum, a heating peripheral chamber surrounding the outer periphery of the rotating drum, a combustion chamber receiving the feeding of a reducing gas from an exhaust pipe, a combustion gas duct for passing the combustion gas discharged from the combustion chamber in series to the heating peripheral chamber and radiant heating cylinder and a weighing and bagging device for the discharged carbonized material and capable of carrying out the carbonization and reduction of the scrap wood under a high-temperature reducing atmosphere by complete indirect heating with radiation and thermal conduction in the apparatus for carbonizing and reducing the scrap wood provided with the rotating drum and the exhaust pipe for the reducing gas in the rotating drum.

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、木造家屋の解体
時に生ずる廃材に代表される廃木材の焼却装置に関する
もので、特に廃木材を乾燥及び炭化させると共にダイオ
キシン等の有害物を還元雰囲気で分解させるのに好適な
加熱手段を備えた上記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 an incinerator for waste wood typified by waste wood generated when a wooden house is dismantled, and more particularly to drying and carbonizing waste wood and decomposing harmful substances such as dioxin in a reducing atmosphere. The present invention relates to the above-mentioned device provided with a heating means suitable for performing the heating.

【0002】[0002]

【従来の技術】廃木材は安定型処分場に埋立処理される
か焼却処理される場合が殆どであるが、埋立場の確保が
困難で廃棄場周辺の環境破壊が問題にされている実情に
おいては、埋立て処理は問題が大きい。また通常の焼却
処理では大量の燃焼空気を必要とし(空気中の酸素が2
1%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が大量に発生し、温暖化
の原因となる炭酸ガスが大量に発生するほか、有害な副
生成物が発生して、これを除去するための排気ガス処理
装置も複雑になり、コスト的にも不利になる。
2. Description of the Related Art Waste wood is mostly landfilled or incinerated in a stable disposal site. However, it is difficult to secure a landfill site and environmental destruction around the disposal site is a problem. In landfill, the problem is big. In addition, ordinary incineration requires a large amount of combustion air (oxygen in the air is 2%).
1% and an excess air ratio of about 1.8 times), which generates a large amount of combustion exhaust gas, generates a large amount of carbon dioxide gas that causes global warming, and generates harmful secondary gases. A product is generated, and an exhaust gas treatment device for removing the product is complicated, which is disadvantageous in cost.

【0003】[0003]

【発明が解決しようとする課題】この発明は、廃木材を
乾燥すると共に、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・還元して、燃焼空気及び炭
酸ガスの減少を図ると共に、廃木材から副生成物を得る
ことができる装置を得ることを課題としており、炭化時
に発生する可燃性還元ガスを燃焼させて間接加熱するこ
とにより、効率良くかつ低コストで炭化・還元温度にま
で廃木材を加熱することができる加熱手段を備えた廃木
材の炭化・還元装置を得ることを課題としている。
SUMMARY OF THE INVENTION The present invention is intended to reduce waste air and carbon dioxide by drying waste wood, heating it to a higher temperature, and carbonizing and reducing it without generating odor or harmful gas. The goal is to obtain a device that can obtain by-products from waste wood. By combusting combustible reducing gas generated during carbonization and indirect heating, carbonization and reduction can be performed efficiently and at low cost. It is an object of the present invention to obtain an apparatus for carbonizing and reducing waste wood provided with a heating means capable of heating waste wood to a temperature.

【0004】[0004]

【課題を解決するための手段】請求項1記載の廃木材の
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供給側隔
壁3及び排出側隔壁4と、還元ガスの排気筒31と、供
給側隔壁3を貫通して回転胴2内に廃木材を供給するフ
ィーダ28と、排出側隔壁4の底部に開口する排出口3
3に連通する排出コンベア34とを備えた廃木材の炭化
・還元装置において、廃木材を破砕してフィーダ28に
供給する破砕機48及び供給ホッパ50と、供給側隔壁
3及び排出側隔壁4を貫通して当該両隔壁3、4で回転
胴2と平行に支持された円柱ないし多角柱状の輻射加熱
筒5と、回転胴2の外周を囲む加熱周室10と、前記排
気筒から還元ガスの供給を受ける燃焼室15と、この燃
焼室に設けた助燃バーナー44と、当該燃焼室から排出
される燃焼ガスを前記加熱周室及び輻射加熱筒を直列に
通過させる燃焼ガスダクト11、25と、排出コンベア
34から排出された炭化物の計量袋詰め装置55、56
とを備え、輻射と熱伝導との完全な間接加熱による高温
還元雰囲気下で廃木材の炭化・還元を行なうことを特徴
とするものである。
According to the first aspect of the present invention, there is provided an apparatus for carbonizing and reducing waste wood, comprising a rotating drum 2 supported at a slight inclination from a horizontal axis, and a fixed supply-side partition for closing both ends of the rotating drum. 3 and a discharge-side partition 4, an exhaust pipe 31 for reducing gas, a feeder 28 that passes through the supply-side partition 3 and supplies waste wood into the rotary drum 2, and a discharge port 3 that opens at the bottom of the discharge-side partition 4.
In a carbonization and reduction device for waste wood provided with a discharge conveyor 34 communicating with the feeder 3, a crusher 48 and a supply hopper 50 for crushing waste wood and supplying it to the feeder 28, and a supply-side partition 3 and a discharge-side partition 4 are provided. A cylindrical or polygonal radiant heating cylinder 5 that penetrates and is supported by the partition walls 3 and 4 in parallel with the rotary drum 2, a heating peripheral chamber 10 surrounding the outer circumference of the rotary drum 2, A combustion chamber 15 to be supplied, an auxiliary burner 44 provided in the combustion chamber, combustion gas ducts 11 and 25 for passing combustion gas discharged from the combustion chamber through the heating peripheral chamber and the radiant heating cylinder in series, Measuring bagging device 55, 56 for carbide discharged from conveyor 34
And carbonizing and reducing waste wood in a high-temperature reducing atmosphere by complete indirect heating of radiation and heat conduction.

【0005】請求項2記載の発明は、請求項1記載の廃
木材の炭化・還元装置において、加熱周室10が当該周
室と輻射加熱筒5とを連結する燃焼ガスダクト11の上
流側に位置してい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 wood carbonizing and reducing apparatus according to the first aspect, the heating peripheral chamber 10 is located upstream of the combustion gas duct 11 connecting the peripheral chamber and the radiation heating cylinder 5. It is characterized by doing.

【0006】また請求項3記載の発明は、請求項1又は
2記載の廃木材の炭化・還元装置において、還元ガスの
排気筒31から排出された還元ガスが木酢液抽出装置4
1を経て燃焼室15へ供給されることを特徴とするもの
である。
According to a third aspect of the present invention, in the apparatus for carbonizing and reducing waste wood according to the first or second aspect, the reducing gas discharged from the exhaust gas exhaust pipe 31 is a wood vinegar extractor 4.
1 and is supplied to the combustion chamber 15.

【0007】[0007]

【作用】この発明の廃木材の炭化・還元装置によれば、
木造建築物の解体などにより生じた廃材の処理から副生
成物の生産までを一貫して行なうことが可能であり、最
小限の燃焼によって燃焼空気量の減少、炭酸ガス排出量
の減少が図れ、高温燃焼により有害物質の生成が防止さ
れる。そして、炭化・還元前の破砕により、効率の良い
炭化・還元処理が可能になり、得られる副生成物の粒度
が一定し、燃料、調湿材、土壌改良剤などとして用いる
品質の良い副生成物が得られる。
According to the waste wood carbonizing and reducing apparatus of the present invention,
It is possible to consistently carry out the processing from waste material generated by demolition of wooden buildings to the production of by-products, and by minimizing combustion, it is possible to reduce the amount of combustion air and carbon dioxide emissions, High-temperature combustion prevents generation of harmful substances. By crushing before carbonization and reduction, efficient carbonization and reduction treatment is possible, the particle size of the obtained by-products is constant, and high-quality by-products used as fuel, humidity control material, soil conditioner, etc. Things are obtained.

【0008】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内に供給された廃木材36
は、撹拌されながら排出側へゆっくりと移送される。運
転の開始時には、燃焼室に付属されている助燃バーナー
44によって加熱用の燃焼ガスを発生させ、廃木材が炭
化されて還元ガスが発生した時点で助燃バーナーを徐々
に絞り、還元ガスを燃焼させて回転胴2を加熱する。
The waste wood 36 supplied into the rotary drum 2 by the feeder 28 by the rotation of the rotary drum 2 whose axis is inclined.
Is slowly transferred to the discharge side while being stirred. At the start of operation, a combustion gas for heating is generated by an auxiliary burner 44 attached to the combustion chamber, and when the waste wood is carbonized to generate a reducing gas, the auxiliary combustion burner is gradually squeezed to burn the reducing gas. To heat the rotating drum 2.

【0009】廃木材36は、回転胴2内の上流側部分を
移動する間に主として加熱周室10からの熱伝導と輻射
により加熱され、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木材は、主として輻射加熱筒5
からの輻射熱によってさらに加熱され、炭化・還元され
る。
The waste wood 36 is heated mainly by heat conduction and radiation from the heating peripheral chamber 10 while moving in the upstream portion in the rotary drum 2, and water evaporates from the outer surface and dries. Waste wood whose outer surface has dried is mainly
And further carbonized and reduced by the radiant heat from

【0010】炭化・還元によって生ずる還元ガスは、燃
焼室15に供給されて完全燃焼され、その燃焼ガスが廃
木材36の乾燥と炭化・還元に利用される。またこの炭
化・還元に伴い廃木材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排出側
へゆっくりと移送され、残った炭化物が排出口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、炭化物が冷却される。
The reducing gas generated by the carbonization / reduction is supplied to the combustion chamber 15 and completely burned, and the combustion gas is used for drying and carbonizing / reducing the waste wood 36. In addition, the water inside the waste wood evaporates due to the carbonization and reduction, and the carbonization and reduction proceeds, and the water is slowly transferred to the discharge side while being stirred with the rotation of the rotary drum 2, and the remaining carbide is discharged through the discharge port 33. It is carried out by the discharge conveyer 34. During the carry-out process by the discharge conveyor 34, the carbide is cooled.

【0011】この発明の装置では、炭化・還元時に発生
する還元ガスを燃焼して、その高温の燃焼ガスにより回
転胴の外側から廃木材を熱伝導と輻射により加熱し、更
に回転胴の内側に設置した輻射加熱筒からの輻射熱によ
ってを内側から加熱するという、回転胴の内外両面から
間接加温により、炭化・還元時の熱効率を高めている。
加熱筒から排出された燃焼ガスは、サイクロン集塵機1
9等で集塵された後、排ガスファン14を経て煙突24
から大気放出される。
In the apparatus of the present invention, the reducing gas generated during carbonization and reduction is burned, and the waste wood is heated by heat conduction and radiation from the outside of the rotating body by the high-temperature combustion gas. The thermal efficiency at the time of carbonization and reduction is increased by indirect heating from both inside and outside of the rotating drum, in which the radiant heat from the installed radiant heating tube is heated from the inside.
The combustion gas discharged from the heating cylinder is supplied to the cyclone dust collector 1
9 and the like, and then the exhaust gas fan 14 passes through the chimney 24
Emitted from the atmosphere.

【0012】廃木材自体を一切燃焼させないので歩留ま
りがよく、燃焼室の助燃バーナー44を制御することに
より、回転胴内を炭化・還元に必要な高温度に加熱する
ことができると共に、炭化・還元に温度を所望温度に正
確に維持することができる。また、回転胴2の回転によ
る撹拌作用で、均一な乾燥及び炭化・還元が可能であ
る。
Since the waste wood itself is not burned at all, the yield is good. By controlling the auxiliary burner 44 in the combustion chamber, the inside of the rotary drum can be heated to a high temperature required for carbonization and reduction, and the carbonization and reduction can be performed. Temperature can be accurately maintained at the desired temperature. In addition, uniform drying and carbonization / reduction can be performed by the stirring action of the rotation of the rotary drum 2.

【0013】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れ
ば、廃木材及び炭化物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。
If a screw feeder and a screw conveyor are used as the feeder 28 and the discharge conveyor 34, waste wood and carbides are filled and conveyed inside the conveyor, so that the space of the feeder and the discharge conveyor can be used without using a special sealing device. The air can be prevented from flowing into the rotary drum through the rotary drum. During carbonization and reduction,
In order to prevent the inflow of air, the inside of the furnace is maintained at a slightly positive pressure.

【0014】[0014]

【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
一実施例を示す断面図、図2は木質廃木材のための装置
の一実施例を示すブロック図、図3は図1の回転炉を含
む図2の装置のより具体的な形状を示す平面図である。
Embodiments of the present invention will be described below with reference to embodiments shown in the drawings. 1 is a cross-sectional view showing one embodiment of a rotary furnace, FIG. 2 is a block diagram showing one embodiment of an apparatus for woody waste wood, and FIG. 3 is a more specific view of the apparatus of FIG. 2 including the rotary furnace of FIG. It is a top view which shows a general shape.

【0015】回転炉1は回転胴2と供給側及び排出側隔
壁3、4と、回転胴の周壁を囲んでいる加熱周室10
と、輻射加熱筒5と、加熱周室10と輻射加熱筒5とを
連結する燃焼ガスダクト11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、廃材供給側の
もの8aが若干高い位置にあり、従って、回転胴2は供
給側から排出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が固定されており、架
台7に装着した図示しない電動機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, a supply-side and discharge-side partition walls 3, 4, and a heating peripheral chamber 10 surrounding the peripheral wall of the rotary drum.
And a radiant heating cylinder 5, and a combustion gas duct 11 connecting the heating peripheral chamber 10 and the radiant heating cylinder 5. Rotating body 2
Has thick flanges 6 on both sides. By supporting the flanges 6 with rollers 8 (8a, 8b) provided on a gantry 7,
It is rotatably supported. The roller 8 has a slightly higher position on the waste material supply side 8a, and therefore the rotating drum 2 is inclined so as to be slightly lower from the supply side to the discharge side.
A sprocket 9 is also fixed to the rotary drum 2, and the rotary drum 2 is rotationally driven by connecting a sprocket with an electric motor (not shown) mounted on the gantry 7 by a chain.

【0016】回転胴2の両端を閉鎖する供給側隔壁3及
び排出側隔壁4は、架台7に固定的に設けられている。
供給側隔壁3及び排出側隔壁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。回転胴2の内面には、廃木材を
掻き上げるための軸方向に細長い掻上羽根が装着されて
いる。
The supply-side partition wall 3 and the discharge-side partition wall 4 for closing both ends of the rotary drum 2 are fixedly provided on a gantry 7.
Between the supply-side partition 3 and the discharge-side partition 4 and the rotary drum 2,
Rotary seals 16 and 17 are provided to prevent gas leakage from the furnace. An axially elongated scraping blade for scraping waste wood is mounted on the inner surface of the rotating drum 2.

【0017】回転胴2のローラ8で支持された鍔6の間
の部分は、回転胴との間に筒状の加熱周室10を形成し
ている断熱壁12で囲まれている。加熱周室10内は、
図2で説明する排ガスファン14の吸引により僅かに負
圧となっており、断熱壁12の両端と回転胴2との摺接
部には、大気の流入を防ぐ回転シール16及び17が設
けられている。加熱周室10の廃材供給側の端部は、燃
焼ガス供給ダクト25により図3に示す燃焼室15に連
結されている。
The portion of the rotary drum 2 between the flanges 6 supported by the rollers 8 is surrounded by a heat insulating wall 12 which forms a cylindrical heating peripheral chamber 10 between itself and the rotary drum. In the heating peripheral chamber 10,
Rotation seals 16 and 17 for preventing the inflow of the atmosphere are provided at the sliding contact between both ends of the heat insulating wall 12 and the rotary drum 2 due to a slight negative pressure due to the suction of the exhaust gas fan 14 described in FIG. ing. The end of the heating peripheral chamber 10 on the waste material supply side is connected to the combustion chamber 15 shown in FIG.

【0018】回転胴2の内部には、その軸線と平行な円
筒状の輻射加熱筒5が設けられている。輻射加熱筒5
は、その両端を供給側隔壁3及び排出側隔壁4に設けた
加熱筒装着孔20、21を貫通した状態で支持されてい
る。この輻射加熱筒5の廃材排出側の端部は、燃焼ガス
ダクト11により、前記加熱周室10の廃材排出側の端
部に連結されており、廃材供給側の端部は、排ガスダク
ト18により、図2のサイクロン集塵機19に連結され
ている。
A cylindrical radiant heating cylinder 5 is provided inside the rotary drum 2 in parallel with its axis. Radiation heating tube 5
Are supported in a state where both ends thereof pass through heating cylinder mounting holes 20 and 21 provided in the supply-side partition 3 and the discharge-side partition 4. The end of the radiant heating cylinder 5 on the waste material discharge side is connected to the end of the heating peripheral chamber 10 on the waste material discharge side by a combustion gas duct 11, and the end on the waste material supply side is connected by an exhaust gas duct 18. It is connected to the cyclone dust collector 19 of FIG.

【0019】回転炉1の供給側の架台7上には、基端に
撹拌ホッパ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、回転炉の供給側隔
壁3を貫通して回転胴2内に開口している。撹拌ホッパ
27には、回転撹拌羽根29が設けられて、回転炉1に
供給される廃木材を撹拌しており、均一化された廃木材
が連続的に回転炉に供給されるようにしている。また、
スクリューフィーダ28の中間部には、加熱により廃木
材から発生する水蒸気を逃がすための水蒸気出口30が
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、加熱筒5は図2、3に示すように
回転胴2の中心から若干偏倚している。
A screw feeder 28 provided with a stirring hopper 27 at the base end is provided on the gantry 7 on the supply side of the rotary furnace 1, and the tip of the feeder penetrates the supply side partition 3 of the rotary furnace. Opening in the rotating drum 2. The stirring hopper 27 is provided with a rotary stirring blade 29 for stirring waste wood supplied to the rotary furnace 1 so that uniform waste wood is continuously supplied to the rotary furnace. . Also,
At an intermediate portion of the screw feeder 28, a steam outlet 30 for opening steam generated from waste wood by heating is opened. In order to secure an arrangement space for the screw feeder 28, the heating cylinder 5 is slightly deviated from the center of the rotary drum 2 as shown in FIGS.

【0020】供給側隔壁3は、上方部に回転炉内に連通
する還元ガス排気筒31を備えている。排出側隔壁4
は、壁面に耐火材層13を設けた空室32を有してお
り、回転胴2の排出側端部は、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3
4は、排出口33から落下する炭化物を排出する。また
排出側隔壁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 supply-side partition 3 is provided with a reducing gas exhaust pipe 31 communicating with the inside of the rotary furnace at the upper part. Discharge side bulkhead 4
Has a vacant space 32 in which a refractory material layer 13 is provided on a wall surface, and a discharge-side end of the rotary drum 2 is supported while being slightly inserted into the vacant 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. Screw conveyor 3 for discharge
4 discharges the carbide falling from the discharge port 33. The discharge-side partition 4 is provided with a non-combustible gas supply port 35 communicating with the inside of the furnace.

【0021】次に図2、3を参照して、回転炉1の周辺
の機器について説明する。廃木材の供給用スクリューフ
ィーダ28及び炭化物の排出用スクリューコンベア34
にはウォータジャケット38、39が設けられて、この
ウォータジャケットに通水することにより、冷却を行な
っている。
Next, the peripheral devices of the rotary furnace 1 will be described with reference to FIGS. Screw feeder 28 for supplying waste wood and screw conveyor 34 for discharging carbide
Are provided with water jackets 38 and 39, and cooling is performed by passing water through the water jackets.

【0022】還元ガスの排気筒31は、還元ガスダクト
40により、木酢液抽出装置41を経て、燃焼室15に
連結されている。木酢液抽出装置41には給水パイプ4
2と排水パイプ43が連結されている。燃焼室15には
助燃バーナー44が設けられており、この助燃バーナー
には灯油タンク45から油ポンプ46で燃料が供給され
ている。燃焼室15の燃焼ガスは、燃焼ガスダクト25
で加熱周室10の廃材供給側の端部に導入されている。
The exhaust pipe 31 for the reducing gas is connected to the combustion chamber 15 via a wood vinegar liquid extracting device 41 by a reducing gas duct 40. The wood vinegar liquid extraction device 41 has a water supply pipe 4
2 and the drain pipe 43 are connected. An auxiliary burner 44 is provided in the combustion chamber 15, and fuel is supplied to the auxiliary burner from a kerosene tank 45 by an oil pump 46. The combustion gas in the combustion chamber 15 is supplied to a combustion gas duct 25.
At the end of the heating peripheral chamber 10 on the waste material supply side.

【0023】運転の立上り時においては、助燃バーナー
44に大量の灯油を供給して、その燃焼ガスで回転炉1
を加熱する。運転が定常状態に達したときは、廃木材か
ら生じた還元ガスを主たる燃料として回転炉を加熱し、
助燃バーナー44で不足熱量を補うとともに、助燃バー
ナー44の燃焼量を制御することによって、回転炉1の
温度を一定に維持する。
At the start of operation, a large amount of kerosene is supplied to the auxiliary combustion burner 44 and the combustion gas is used to rotate the rotary furnace 1.
Heat. When operation reaches a steady state, the rotary furnace is heated using reducing gas generated from waste wood as the main fuel,
The temperature of the rotary furnace 1 is maintained constant by supplementing the insufficient heat with the auxiliary burner 44 and controlling the amount of combustion of the auxiliary burner 44.

【0024】加熱周室10及び輻射加熱筒5を通った燃
焼ガスは、排ガスダクト18を経てサイクロン集塵機1
9に導かれ、ダンパ22を備えた外気吸入口23から吸
入される新鮮空気と混合されて、排ガスファン14で吸
引され、煙突24を通って大気放出される。
The combustion gas that has passed through the heating peripheral chamber 10 and the radiant heating cylinder 5 passes through an exhaust gas duct 18 so that the cyclone dust collector 1
9, is mixed with fresh air sucked from an outside air suction port 23 provided with a damper 22, is sucked by an exhaust gas fan 14, and is discharged to the atmosphere through a chimney 24.

【0025】攪拌ホッパ27の上流側には破砕機48、
破砕品コンベア49、受入れホッパ50及び供給コンベ
ア51が配置されている。木造家屋を解体したときに生
じる解体木屑は、破砕機48で所望の粒度に破砕された
後、破砕品コンベア49で受入れホッパ50に供給され
る。破砕木屑は、受入れホッパ50に一時的に貯留さ
れ、計量コンベア52で一定量ずつ供給コンベア51に
送り出して、攪拌ホッパ27へと搬送する。
At the upstream side of the stirring hopper 27, a crusher 48,
A crushed product conveyor 49, a receiving hopper 50, and a supply conveyor 51 are arranged. Demolition wood chips generated when the wooden house is dismantled are crushed to a desired particle size by a crusher 48, and then supplied to a receiving hopper 50 by a crushed product conveyor 49. The crushed wood chips are temporarily stored in the receiving hopper 50, sent out to the supply conveyor 51 by the metering conveyor 52 by a fixed amount, and conveyed to the stirring hopper 27.

【0026】排出コンベア34から排出された炭化物
は、ロータリーバルブ53を経て、製品コンベア58で
製品タンク54に貯留される。製品タンク54の下方に
は、計量機55、袋詰め機56及びシール機57が配置
されており、製品タンク54から落下する炭化物が計量
機55で所定量ずつ計量されて、袋詰め機56内に待機
している袋に投入され、シール機57で当該袋を封止す
ることにより、所定量ずつ袋詰めされた炭化物が得られ
る。
The carbide discharged from the discharge conveyor 34 is stored in a product tank 54 by a product conveyor 58 via a rotary valve 53. Below the product tank 54, a weighing machine 55, a bag stuffing machine 56, and a sealing machine 57 are arranged, and the carbide falling from the product tank 54 is measured by a predetermined amount by the weighing machine 55, and the inside of the bag stuffing machine 56 is measured. Is put into the waiting bag, and the bag is sealed by the sealing machine 57, so that a predetermined amount of packed carbide is obtained.

【0027】木造家屋の解体等により生じた木屑は、ま
ず破砕機48に投入されて所定粒度に破砕され、一定量
ずつ攪拌ホッパ27に投入され、スクリューフィーダ2
8によって回転胴2内に送られる。回転胴2はゆっくり
と回転駆動されている。回転胴2から排出される還元ガ
スは、燃焼室で完全燃焼され、これにより生ずる高温と
燃焼ガスにより、まず回転胴が外側より加熱され、更に
その燃焼ガスが回転胴内に設置されている輻射加熱筒を
通過する時に発生する輻射熱で回転胴2内の廃木材が加
熱されて、廃木材を炭化・還元する。炭化・還元温度は
燃焼室の助燃バーナーで制御する。回転胴2の回転によ
り回転胴内の廃木材は底部のものが上層へ掻き上げられ
るように撹拌され、非酸化性雰囲気中で均一に炭化・還
元される。
Wood chips generated by dismantling a wooden house or the like are first introduced into a crusher 48 to be crushed to a predetermined particle size, and then introduced into the stirring hopper 27 by a predetermined amount.
By 8, it is sent into the rotating drum 2. The rotary drum 2 is driven to rotate slowly. The reducing gas discharged from the rotating drum 2 is completely combusted in the combustion chamber, and the high temperature and the combustion gas generated thereby heat the rotating drum first from the outside, and further, the combustion gas is radiated in the rotating drum. The waste wood in the rotating drum 2 is heated by radiant heat generated when passing through the heating cylinder, and carbonizes and reduces the waste wood. The carbonization / reduction temperature is controlled by an auxiliary burner in the combustion chamber. By the rotation of the rotary drum 2, the waste wood in the rotary drum is stirred so that the bottom one is scraped up to the upper layer, and is uniformly carbonized and reduced in a non-oxidizing atmosphere.

【0028】回転胴2の傾斜により、回転胴内の廃木材
は撹拌されつつ排出側へと移動する。そして、排出側隔
壁の空室32に移動してきた廃木材は、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。
Due to the inclination of the rotary drum 2, the waste wood in the rotary drum moves to the discharge side while being stirred. Then, the waste wood that has moved into the empty room 32 of the discharge-side partition wall falls through the discharge port 33 and is discharged by the discharge screw conveyor 34.

【0029】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木材を、
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、廃木材を均一に炭化・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、かつ熱効率を向上させること
ができてランニングコストも低減できる。
According to the apparatus of the present invention, as described in the above embodiment, waste wood continuously supplied from the feeder is
It is carbonized and reduced in a rotary furnace, and is continuously discharged by a discharge conveyor. The waste wood can be uniformly carbonized and reduced, and the control of the carbonization and reduction temperature is easy. Further, by employing the heating device having the structure of the present invention, high-temperature heating can be performed, carbonization and reduction can be accurately controlled, thermal efficiency can be improved, and running costs can be reduced.

【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側面図FIG. 1 is a sectional side view of a rotary furnace according to an embodiment.

【図2】実施例装置全体を示すブロック図FIG. 2 is a block diagram showing the entire apparatus of the embodiment.

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

【符号の説明】[Explanation of symbols]

2 回転胴 3 供給側隔壁 4 排出側隔壁 5 輻射加熱筒 10 加熱周室 11 燃焼ガスダクト 15 燃焼室 25 燃焼ガスダクト 28 供給用スクリューフィーダ 31 還元ガス排気筒 33 炭化物排出口 34 排出用スクリューコンベア 41 木酢液抽出装置 44 助燃バーナー 48 破砕機 50 受入れホッパ 55 計量機 56 袋詰め機 2 Rotary barrel 3 Supply side partition 4 Discharge side partition 5 Radiant heating cylinder 10 Heating peripheral chamber 11 Combustion gas duct 15 Combustion chamber 25 Combustion gas duct 28 Supply screw feeder 31 Reducing gas exhaust cylinder 33 Carbide discharge port 34 Discharge screw conveyor 41 Wood vinegar Extractor 44 Burner burner 48 Crusher 50 Receiving hopper 55 Weighing machine 56 Bag filling machine

───────────────────────────────────────────────────── フロントページの続き (72)発明者 水越 裕治 石川県金沢市観音堂町ホ7番地 株式会社 アクトリームラタ内 Fターム(参考) 4D004 AA12 BA03 CA04 CA26 CA27 CA42 CB09 CB13 CB46 DA02 DA06 4H012 JA03 JA12  ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Yuji Mizukoshi 7 Kannondo-cho, Kanazawa City, Ishikawa Prefecture Actry Murata F-term (reference) 4D004 AA12 BA03 CA04 CA26 CA27 CA42 CB09 CB13 CB46 DA02 DA06 4H012 JA03 JA12

Claims (3)

【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供給側隔壁
(3)及び排出側隔壁(4)と、還元ガスの排気筒(31)と、供
給側隔壁(3)を貫通して回転胴(2)内に廃木材を供給する
フィーダ(28)と、排出側隔壁(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)とを備えた廃木材の
炭化・還元装置において、廃木材を破砕してフィーダ(2
8)に供給する破砕機(48)及び供給ホッパ(50)と、供給側
隔壁(3)及び排出側隔壁(4)を貫通して当該両隔壁(3,4)
で回転胴(2)と平行に支持された円柱ないし多角柱状の
輻射加熱筒(5)と、回転胴(2)の外周を囲む加熱周室(10)
と、前記排気筒から還元ガスの供給を受ける燃焼室(15)
と、この燃焼室に設けた助燃バーナー(44)と、当該燃焼
室から排出される燃焼ガスを前記加熱周室及び輻射加熱
筒を直列に通過させる燃焼ガスダクト(11,25)と、排出
コンベア(34)から排出された炭化物の計量袋詰め装置(5
5,56)とを備えている、廃木材の炭化・還元装置。
1. A rotary drum supported slightly inclined from a horizontal axis.
(2) and a fixed supply-side partition that closes both ends of this rotary drum
(3) and a discharge-side partition (4), an exhaust pipe (31) for reducing gas, and a feeder (28) for supplying waste wood into the rotating drum (2) through the supply-side partition (3), In a waste wood carbonization and reduction device provided with a discharge conveyor (34) communicating with a discharge port (33) opened at the bottom of the discharge side bulkhead (4), the waste wood is crushed and fed.
8) The crusher (48) and the supply hopper (50) to be supplied to the feeder bulkhead (3) and the discharge bulkhead (4) through the bulkheads (3, 4).
A cylindrical or polygonal radiant heating cylinder (5) supported in parallel with the rotating drum (2), and a heating chamber (10) surrounding the outer circumference of the rotating drum (2)
A combustion chamber (15) receiving a supply of reducing gas from the exhaust stack
A combustion burner (44) provided in the combustion chamber, a combustion gas duct (11, 25) for passing combustion gas discharged from the combustion chamber in series through the heating peripheral chamber and the radiant heating cylinder, and a discharge conveyor ( Weighing device (5)
5,56), a carbonization and reduction device for waste wood.
【請求項2】 加熱周室(10)が当該周室と輻射加熱筒
(5)とを連結する燃焼ガスダクト(11)の上流側に位置し
ていることを特徴とする、請求項1記載の廃木材の炭化
・還元装置。
2. The heating peripheral chamber (10) is composed of the peripheral chamber and a radiation heating cylinder.
The waste wood carbonizing / reducing device according to claim 1, wherein the device is located upstream of a combustion gas duct (11) connecting the waste gas to the waste gas.
【請求項3】 還元ガスの排気筒(31)から排出された還
元ガスが木酢液抽出装置(41)を経て燃焼室(15)へ供給さ
れることを特徴とする、請求項1又は2記載の廃木材の
炭化・還元装置。
3. The method according to claim 1, wherein the reducing gas discharged from the exhaust pipe of the reducing gas is supplied to the combustion chamber via the wood vinegar extractor. Waste wood carbonization and reduction equipment.
JP2000195047A 2000-06-28 2000-06-28 Apparatus for carbonizing and reducing scrap wood Pending JP2002012875A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000195047A JP2002012875A (en) 2000-06-28 2000-06-28 Apparatus for carbonizing and reducing scrap wood

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000195047A JP2002012875A (en) 2000-06-28 2000-06-28 Apparatus for carbonizing and reducing scrap wood

Publications (1)

Publication Number Publication Date
JP2002012875A true JP2002012875A (en) 2002-01-15

Family

ID=18693784

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000195047A Pending JP2002012875A (en) 2000-06-28 2000-06-28 Apparatus for carbonizing and reducing scrap wood

Country Status (1)

Country Link
JP (1) JP2002012875A (en)

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