JP4772213B2 - Continuous carbonization equipment for organic waste - Google Patents

Continuous carbonization equipment for organic waste Download PDF

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Publication number
JP4772213B2
JP4772213B2 JP2001169619A JP2001169619A JP4772213B2 JP 4772213 B2 JP4772213 B2 JP 4772213B2 JP 2001169619 A JP2001169619 A JP 2001169619A JP 2001169619 A JP2001169619 A JP 2001169619A JP 4772213 B2 JP4772213 B2 JP 4772213B2
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Prior art keywords
continuous carbonization
opening plate
organic waste
upper opening
carbonization
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JP2002361297A (en
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昌洋 難波
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株式会社まさなみ鉄工
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Description

【0001】
【発明の属する技術分野】
本発明は、し尿処理汚泥、食品製造業や畜産廃棄物等の汚水処理施設で生じる活性汚泥、そば殻、コーヒー抽出かすなど主として有機質に富む廃棄物の連続炭化処理装置に関するものである。
【0002】
【従来の技術】
下水処理施設、し尿処理施設や各種汚水処理施設の規模は益々大きくなっており、それにつれて発生する汚泥の量も増大し、その処理が問題となっている。固形化して有用な建築素材等にするには有機質が主体で強度が得られなかったり、臭いの問題もある。肥料化する試みがなされているが(特開平11-116367号)、製造される肥料の量が多く、過剰生産となっているのが現状である。下水処理汚泥、し尿処理施設や各種汚水処理施設で発生する汚泥は、有効利用することも一手段であるが、焼却処分することも廃棄物処理手段として選択肢の一つである。しかし、焼却に際してはダイオキシンの発生の対策が必要となってくるし、加熱源も必要となる。
【0003】
そこで、本発明者は下水処理施設等で大量に発生する汚泥を連続して炭化処理することが可能な下水処理等の汚泥の連続処理方法及び装置について検討し、先に特許第3131176号、特開2000-246289号、特開2000-288595号等で提案している。特許第3131176号では有機廃棄物の還元炭化が実施可能な装置を提案している。また、特開2000-246289号では、有機質を含む汚泥又は有機廃棄物の被炭化処理対象物に炭素含有炭化助剤を添加して炭化処理する方法を提案しており、更に、特開2000-288595号ではその炭化処理方法を実施するシステムを提案している。
【0004】
前記特開2000-246289号、特開2000-288595号では、連続炭化部の下部に格子を設けただけの装置では格子が目詰まりして連続処理に支障を生じるので、還元雰囲気での連続炭化処理が円滑に行われるように、炭化物の下方への移動を可能とするために連続炭化部へ複数の通過穴を有する上開口板と下開口板を設けている。上開口板を移動させることによって、上下の通過穴が一致した時(垂直方向に見た時同位置)炭化物の落下を可能としている。加えて、上開口板の底面に下向きの掻出し板を設けている。
【0005】
【発明が解決しようとする課題】
移動する上開口板と下開口板を連続炭化部に設けると、上下の通過穴が垂直方向に同位置となった時に炭化中の被炭化処理対象物が通過し、通過穴が垂直方向に異なる位置では閉鎖された状態となり、いずれの場合にも空気の通過をほとんど許さないので還元雰囲気を保つことができる。被炭化処理対象物は適度に下方へ移動しながら炭化されるのである。ところが、炭化中の被炭化処理対象物は通常600〜650℃程度の高温となり、上開口板も下開口板も、また、連続炭化部周囲の壁面も高温に曝され、運転条件によっては構成部材に変形が生じる場合があった。上開口板も下開口板も熱で反ったり変形すると被炭化処理対象物の落下が不充分となるし、移動が困難となって、連続炭化が不可能となる。上開口板の底面に下向きの掻出し板を設けている場合にはかえって移動が困難となるケースもみられた。そこで、連続炭化を円滑に行うことができることを目的として、上開口板、下開口板に検討を加え、かつ、掻出しの機能を良好に保持できる構成について検討した。
【0006】
【課題を解決するための手段】
上記課題を検討した結果、有機質を含む汚泥又は有機廃棄物の被処理対象物を連続炭化処理するための装置であって、還元雰囲気の連続炭化部上部に被処理対象物の供給部を設け、該供給部下方の連続炭化部中に設けられた少なくとも一方が移動する上開口板と下開口板のそれぞれに設けた通過穴の一致によって被処理対象物を降下させながら連続炭化する装置において、上開口板又は下開口板に冷却用ジャケットを設けたことを特徴とする有機質廃棄物の連続炭化処理装置とした。
【0007】
そして本発明では、上開口板の下方に通過穴を残して突出した冷却用ジャケットを設け、上開口板の移動時に冷却用ジャケットの干渉(接触)により被処理対象物の落下を促すようにした。また、連続炭化部の周囲にも冷却用ジャケットを設けた有機質廃棄物の連続炭化処理装置としたのである。
【0008】
また、このような有機質廃棄物の連続炭化処理装置の連続炭化部下部の炭化物取出し口と被処理対象物の供給部との間に炭化物のフィードバック手段を設け、該炭化物を被処理対象物と混合するようにした。前記特開2000-246289号、特開2000-288595号と同様に、炭素含有助剤の供給手段として前記処理によって得られた炭化物をフィードバックする手段を連続炭化部の被処理対象物供給部と下部の炭化物取出し口との間に設け、下水処理汚泥からの炭化物を連続炭化部へフィードバックさせて、下水処理汚泥を連続処理するのである。
【0009】
更に、下水処理汚泥と炭化物とを混合する混合機と、下水処理汚泥を燃焼し易くするための造粒部と、上部に被処理対象物供給部を有する密閉連続炭化部とからなる炭化処理装置において、連続炭化部が前記いずれかに記載のジャケットを有している有機質廃棄物の連続炭化処理装置としたのである。
【0010】
【発明の実施の形態】
以下本発明を図面に基づいて詳細に説明する。
図1は本発明の有機質廃棄物の連続炭化処理装置の工程系統図である。この装置は連続炭化部4の上部に被処理対象物供給部5を有しており、必要に応じて連続炭化部4の上部右方において下水処理汚泥等に炭素含有助剤を添加して、この連続炭化部4で連続炭化処理するのである。この装置の概要については先に提案した特開2000-246289号でも紹介している。被処理対象物供給部5へ供給するために下水処理汚泥等を燃焼し易くするための造粒部19と乾燥部20を設けている。造粒部19は詳細な図示を省略するが、多孔ノズルから押し出された麺線状の汚泥等を粒状にカットするようになっている。この実施例の装置では炭素含有助剤の供給手段として、連続炭化部4で得られた炭化物のほぼ全量をフィードバックするようになっており、フィードバック手段18は連続炭化部の炭化物取出し口6から下水処理汚泥等と炭化物とを混合する混合機21まで運ぶようになっている。混合機21から造粒部19までコンベアで送られる。下水処理汚泥からの炭化物を連続炭化部へフィードバックさせて使用し、下水処理汚泥を連続処理するのである。
【0011】
図2は本発明の有機質廃棄物の連続炭化処理装置における連続炭化部の実施例の縦断面図である。この装置における連続炭化部においては、機台1上に円筒状のケーシング2を有しており、その内部に内筒3Aと外筒3Bを有する連続炭化部4を設けている。その上部が被処理対象物供給部5である。連続炭化部4の下部は下方が狭いテーパ状の炭化物取出し口6となっている。連続炭化部4の下部に有機ガス捕集部7の吸引ダクト8が設けられている。この吸引ダクト8は排気ファン9につながっている。炭化物取出し口6から排出される炭化物は前記被処理対象物供給部5間に設けられたコンベア等のフィードバック手段18(一点鎖線表示)によってフィードバックして炭素含有助剤として再使用されるようになっている。
【0012】
図3及び図4は図2中A部拡大図である。連続炭化部4では上方から被処理対象物を供給し、空気の供給が殆どない状態で還元雰囲気の炭化を行いながら下方へ移動させる。そのために、連続炭化部4中に上開口板11と下開口板12を設けている。いずれも炭化中の被処理対象物が通過するための複数の通過穴(開口溝)を有した構造であって、図5に下開口板12の断面を示す。上開口板11もほぼ同様な構造であるが、下開口板12が装置ケーシング2側へ固定されているのに対し、上開口板11は水平方向に移動可能である。そのために上開口板11は、吊り杆13によって連続炭化部4内に吊ると共に、装置ケーシング2の側面に設けたシリンダ15へ連結している。移動する上開口板11と固定した下開口板12のそれぞれに設けた通過穴11a,12aが、図3のように異なる垂直位置に存在した場合には被処理対象物が通過できない。図4のように垂直方向で一致すると、被処理対象物は降下することができる。
【0013】
炭化中の被炭化処理対象物は通常600〜650℃の高温となり、上開口板11も下開口板12も変形が生じ易い。また、連続炭化部周囲の内筒3Aの壁面も高温に曝される。上開口板11も下開口板12も熱で反る等の変形が生じると、被炭化処理対象物の落下が不充分となるし、移動が困難となって、連続炭化が不可能となる。上開口板11の底面に下向きの掻出し板を設けている場合にはかえって移動が困難となる場合もある。そこで、本発明では上開口板11と下開口板12に冷却用ジャケット10A,10Bを設けている。この冷却用ジャケットの構造を図5に下開口板12の例によって示す。被処理対象物の複数の通過穴12aの周囲に冷媒の液体が冷媒入口12bから迂回しながら冷媒出口方向へと移動する。冷媒の液体としては、水が安価かつ供給し易いので適している。
【0014】
一方、上開口板11は、図3のように通過穴11a,12aが異なる位置に存在した場合には、被処理対象物が落下しないで下開口板12の上へ載った状態となる。上開口板の下方に通過穴を残して突出した状態に冷却用ジャケット10Aを設けている。このことによって、上開口板が移動する度に冷却用ジャケット10Aが被処理対象物の落下を促すよう被処理対象物に干渉するのである。揺動手段14を吊り杆13と共に構成するシリンダ15により定期的に上開口板11を左右に動かすと被処理対象物又は炭化物を下方へ落下させることができる。
【0015】
本発明の有機質廃棄物の連続炭化処理装置では、更に連続炭化部4の周囲にも冷却用ジャケット10Cを設けている。これによって、内筒3Aの熱変形や熱分解を防ぐことができる。
【0016】
有機質廃棄物の被処理対象物は連続炭化部4中に入れて、初期の炭化が安定するまでの間、連続炭化部4中にバーナー炎を作用させて着火させる。空気の供給が殆どない状態で還元雰囲気の炭化を行い、揺動手段14により定期的に上開口板11を左右に動かしながら、炭化物を下方へ落下させる。このとき、排気ファン9を回して吸引ダクト8から炭化の結果生じた木酢等の有機ガスを強制的に吸引除去させ、燃焼炉16で燃焼させる。木酢等の有機ガスは、また、途中がU字状に曲がって冷却水槽中を通っている捕集管によって捕集するようにしてもよい。
【0017】
【発明の効果】
本発明によって、上開口板の移動が円滑に行われるので、有機質廃棄物の被処理対象物が炭化の過程で停滞することなく連続炭化が可能となる。常に安定した状態で還元が行われ、均質な炭化物が得られる。上開口板、下開口板、内筒、ケーシング等が高温に曝されることがないので、装置が破損し難く、かつ耐久性が向上した。
【図面の簡単な説明】
【図1】本発明の有機質廃棄物の連続炭化処理装置の工程系統図である。
【図2】本発明の有機質廃棄物の連続炭化処理装置における連続炭化部の縦断面図である。
【図3】通過穴が異なる垂直位置に存在した時の図2中A部拡大図である。
【図4】通過穴が垂直方向で一致した時の図3相当図である。
【図5】下開口板の断面図である。
【符号の説明】
1 機台
2 ケーシング
3A 内筒
3B 外筒
4 連続炭化部
5 被処理対象物供給部
6 炭化物取出し口
7 有機ガス捕集部
8 吸引ダクト
9 排気ファン
10A 冷却用ジャケット
10B 冷却用ジャケット
10C 冷却用ジャケット
11 上開口板
11a 通過穴
12 下開口板
12a 通過穴
13 吊り杆
14 揺動手段
15 シリンダ
16 燃焼炉
18 フィードバック手段
19 造粒部
20 乾燥部
21 混合機
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a continuous carbonization apparatus for wastes mainly rich in organic matter such as human waste processing sludge, activated sludge generated in sewage treatment facilities such as food manufacturing industry and livestock waste, buckwheat husk, and coffee grounds.
[0002]
[Prior art]
The scales of sewage treatment facilities, human waste treatment facilities and various sewage treatment facilities are increasing, and the amount of sludge generated is increasing accordingly. In order to solidify it into a useful building material or the like, there is a problem that the organic substance is mainly used and the strength cannot be obtained or the smell is bad. Attempts to use fertilizer have been made (Japanese Patent Laid-Open No. 11-116367), but the amount of fertilizer produced is large and the production is excessive. Effective utilization of sludge generated in sewage treatment sludge, human waste treatment facilities and various sewage treatment facilities is one means, but incineration is also an option as a waste treatment means. However, incineration requires countermeasures against dioxin generation and a heating source.
[0003]
In view of this, the present inventor examined a sludge continuous treatment method and apparatus, such as sewage treatment, capable of continuously carbonizing sludge generated in large quantities at a sewage treatment facility. This is proposed in Kai 2000-246289, JP-A 2000-288595, and the like. Japanese Patent No. 3131176 proposes an apparatus capable of reducing carbonization of organic waste. Japanese Patent Laid-Open No. 2000-246289 proposes a method of carbonization treatment by adding a carbon-containing carbonization aid to an object to be carbonized of sludge containing organic matter or organic waste. 288595 proposes a system that implements the carbonization method.
[0004]
In the above-mentioned JP-A-2000-246289 and JP-A-2000-288595, an apparatus in which a grid is simply provided at the lower part of the continuous carbonization section clogs the grid and hinders continuous processing. In order to allow the processing to be performed smoothly, an upper opening plate and a lower opening plate having a plurality of passage holes are provided in the continuous carbonization portion in order to allow the carbide to move downward. By moving the upper aperture plate, the carbide can be dropped when the upper and lower passage holes are coincident (same position when viewed in the vertical direction). In addition, a downward scraping plate is provided on the bottom surface of the upper opening plate.
[0005]
[Problems to be solved by the invention]
When the upper opening plate and the lower opening plate that move are provided in the continuous carbonization section, the carbonized object to be carbonized passes when the upper and lower passage holes are in the same position in the vertical direction, and the passage holes are different in the vertical direction. The position is closed, and in any case, almost no air is allowed to pass through, so that a reducing atmosphere can be maintained. The object to be carbonized is carbonized while moving downward appropriately. However, the object to be carbonized during carbonization usually becomes a high temperature of about 600 to 650 ° C., and the upper opening plate, the lower opening plate, and the wall surface around the continuous carbonization part are exposed to a high temperature. In some cases, deformation occurred. If the upper aperture plate and the lower aperture plate are warped or deformed by heat, the object to be carbonized is insufficiently dropped, becomes difficult to move, and cannot be continuously carbonized. In some cases, when a downward scraping plate was provided on the bottom surface of the upper opening plate, it was difficult to move. In view of this, for the purpose of smoothly performing continuous carbonization, the upper opening plate and the lower opening plate were studied, and a configuration capable of satisfactorily retaining the scraping function was studied.
[0006]
[Means for Solving the Problems]
As a result of examining the above problems, it is an apparatus for continuously carbonizing an object to be treated of sludge containing organic matter or organic waste, and a supply part for the object to be treated is provided on the continuous carbonization part in a reducing atmosphere, In the apparatus for continuously carbonizing while lowering the object to be processed by matching the through holes provided in each of the upper opening plate and the lower opening plate in which at least one of the continuous carbonization units provided below the supply unit moves, A continuous carbonization treatment apparatus for organic waste, characterized in that a cooling jacket is provided on the aperture plate or the lower aperture plate.
[0007]
In the present invention, a cooling jacket that protrudes leaving a through hole is provided below the upper opening plate, and the object to be processed is urged to drop by interference (contact) of the cooling jacket when the upper opening plate is moved . . In addition, a continuous carbonization treatment apparatus for organic waste provided with a cooling jacket around the continuous carbonization portion.
[0008]
In addition, a carbide feedback means is provided between the carbide outlet at the bottom of the continuous carbonization section of such a continuous carbonization treatment apparatus for organic waste and the supply section of the object to be processed, and the carbide is mixed with the object to be processed. I tried to do it. Similar to the above-mentioned JP-A-2000-246289 and JP-A-2000-288595, means for feeding back the carbide obtained by the above process as a means for supplying a carbon-containing auxiliary agent is provided with the object supply part and the lower part of the continuous carbonization part. The sewage treatment sludge is continuously treated by feeding back the carbide from the sewage treatment sludge to the continuous carbonization section.
[0009]
Furthermore, the carbonization processing apparatus which consists of the mixer which mixes a sewage-treatment sludge and a carbide | carbonized_material, the granulation part for making a sewage-treatment sludge easy to burn, and the closed continuous carbonization part which has a to-be-processed object supply part in the upper part. In the above, the continuous carbonization portion is a continuous carbonization processing apparatus for organic waste having the jacket described above.
[0010]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail with reference to the drawings.
FIG. 1 is a process flow diagram of an apparatus for continuous carbonization of organic waste according to the present invention. This apparatus has the to-be-processed object supply part 5 in the upper part of the continuous carbonization part 4, and adds a carbon containing adjuvant to sewage treatment sludge etc. in the upper right part of the continuous carbonization part 4 as needed, This continuous carbonization part 4 performs continuous carbonization. An outline of this apparatus is also introduced in the previously proposed Japanese Patent Laid-Open No. 2000-246289. A granulation unit 19 and a drying unit 20 are provided for facilitating combustion of sewage treatment sludge and the like for supply to the object supply unit 5. Although the detailed illustration is omitted, the granulating portion 19 is configured to cut the noodle-like sludge extruded from the porous nozzle into a granular shape. In the apparatus of this embodiment, almost the entire amount of carbide obtained in the continuous carbonization section 4 is fed back as means for supplying the carbon-containing auxiliary agent, and the feedback means 18 is sewage from the carbide outlet 6 of the continuous carbonization section. It is transported to a mixer 21 for mixing treated sludge and carbides. It is sent from the mixer 21 to the granulation unit 19 by a conveyor. Carbide from the sewage treatment sludge is fed back to the continuous carbonization section and used to continuously treat the sewage treatment sludge.
[0011]
FIG. 2 is a longitudinal sectional view of an embodiment of a continuous carbonization portion in the continuous carbonization processing apparatus for organic waste according to the present invention. In the continuous carbonization part in this apparatus, it has the cylindrical casing 2 on the machine base 1, and the continuous carbonization part 4 which has the inner cylinder 3A and the outer cylinder 3B is provided in the inside. The upper part is the processing object supply part 5. The lower part of the continuous carbonization part 4 is a tapered carbide outlet 6 having a narrow bottom. A suction duct 8 for the organic gas collection unit 7 is provided below the continuous carbonization unit 4. The suction duct 8 is connected to the exhaust fan 9. The carbide discharged from the carbide outlet 6 is fed back by a feedback means 18 (indicated by a one-dot chain line) such as a conveyor provided between the object supply parts 5 to be reused as a carbon-containing auxiliary agent. ing.
[0012]
3 and 4 are enlarged views of part A in FIG. In the continuous carbonization unit 4, the object to be treated is supplied from above, and is moved downward while carbonizing the reducing atmosphere in a state where there is almost no supply of air. For this purpose, an upper opening plate 11 and a lower opening plate 12 are provided in the continuous carbonization portion 4. Each has a structure having a plurality of through holes (opening grooves) through which an object to be treated during carbonization passes, and FIG. 5 shows a cross section of the lower opening plate 12. The upper opening plate 11 has substantially the same structure, but the lower opening plate 12 is fixed to the apparatus casing 2 side, whereas the upper opening plate 11 is movable in the horizontal direction. For this purpose, the upper opening plate 11 is suspended in the continuous carbonization part 4 by a suspension rod 13 and is connected to a cylinder 15 provided on the side surface of the apparatus casing 2. When the through holes 11a and 12a provided in the moving upper opening plate 11 and the fixed lower opening plate 12 exist at different vertical positions as shown in FIG. 3, the object to be processed cannot pass. If they match in the vertical direction as shown in FIG. 4, the object to be processed can be lowered.
[0013]
The object to be carbonized during carbonization usually has a high temperature of 600 to 650 ° C., and the upper opening plate 11 and the lower opening plate 12 are likely to be deformed. Further, the wall surface of the inner cylinder 3A around the continuous carbonization portion is also exposed to high temperature. If the upper opening plate 11 and the lower opening plate 12 are deformed such as warping due to heat, the object to be carbonized is insufficiently dropped, becomes difficult to move, and continuous carbonization becomes impossible. If a downward scraping plate is provided on the bottom surface of the upper opening plate 11, the movement may be difficult. Therefore, in the present invention, the upper opening plate 11 and the lower opening plate 12 are provided with cooling jackets 10A and 10B. The structure of the cooling jacket is shown in FIG. The refrigerant liquid moves in the direction of the refrigerant outlet while bypassing the refrigerant inlet 12b around the plurality of passage holes 12a of the object to be processed. As the refrigerant liquid, water is suitable because it is inexpensive and easy to supply.
[0014]
On the other hand, when the passage holes 11a and 12a are present at different positions as shown in FIG. 3, the upper opening plate 11 is placed on the lower opening plate 12 without dropping the object to be processed. The cooling jacket 10A is provided so as to protrude below the upper opening plate leaving a passage hole. Thus, every time the upper opening plate moves, the cooling jacket 10A interferes with the object to be processed so as to encourage the object to be processed to fall. When the upper opening plate 11 is periodically moved to the left and right by the cylinder 15 that constitutes the swing means 14 together with the suspension rod 13, the object to be processed or the carbide can be dropped downward.
[0015]
In the continuous carbonization treatment apparatus for organic waste according to the present invention, a cooling jacket 10C is also provided around the continuous carbonization section 4. Thereby, thermal deformation and thermal decomposition of the inner cylinder 3A can be prevented.
[0016]
The object to be treated of the organic waste is put in the continuous carbonization part 4 and is ignited by applying a burner flame in the continuous carbonization part 4 until the initial carbonization is stabilized. The reducing atmosphere is carbonized in a state where there is almost no supply of air, and the carbide is dropped downward while the upper opening plate 11 is periodically moved left and right by the swinging means 14. At this time, the exhaust fan 9 is turned to forcibly remove organic gas such as pyroligneous acid produced as a result of carbonization from the suction duct 8 and burn it in the combustion furnace 16. Organic gas such as wood vinegar may also be collected by a collection tube that is bent in a U shape and passes through the cooling water tank.
[0017]
【The invention's effect】
According to the present invention, the upper aperture plate is smoothly moved, so that the object to be treated of organic waste can be continuously carbonized without stagnation in the process of carbonization. Reduction is always performed in a stable state, and a homogeneous carbide is obtained. Since the upper opening plate, the lower opening plate, the inner cylinder, the casing, and the like are not exposed to high temperatures, the apparatus is hardly damaged and the durability is improved.
[Brief description of the drawings]
FIG. 1 is a process flow diagram of an organic waste continuous carbonization treatment apparatus of the present invention.
FIG. 2 is a longitudinal sectional view of a continuous carbonization portion in the organic waste continuous carbonization processing apparatus of the present invention.
FIG. 3 is an enlarged view of a portion A in FIG. 2 when the passage holes exist at different vertical positions.
FIG. 4 is a view corresponding to FIG. 3 when the passage holes are aligned in the vertical direction.
FIG. 5 is a cross-sectional view of a lower opening plate.
[Explanation of symbols]
1 Machine 2 Casing
3A inner cylinder
3B Outer cylinder 4 Continuous carbonization part 5 Processed object supply part 6 Carbide outlet 7 Organic gas collection part 8 Suction duct 9 Exhaust fan
10A cooling jacket
10B Cooling jacket
10C cooling jacket
11 Upper aperture plate
11a Through hole
12 Lower aperture plate
12a Through hole
13 Hanging rod
14 Swing means
15 cylinders
16 Combustion furnace
18 Feedback means
19 Granulation section
20 Drying section
21 Mixer

Claims (3)

有機質を含む汚泥又は有機廃棄物の被処理対象物を連続炭化処理するための装置であって、還元雰囲気の連続炭化部上部に被処理対象物の供給部を設け、該供給部下方の連続炭化部中に設けられた少なくとも一方が移動する上開口板と下開口板のそれぞれに設けた通過穴の一致によって被処理対象物を降下させながら連続炭化する装置において、
上開口板又は下開口板に冷却用ジャケットを設け、
上開口板の下方に通過穴を残して突出した冷却用ジャケットを設け、
上開口板の移動時に冷却用ジャケットの干渉により被処理対象物の落下を促すようにしたことを特徴とする有機質廃棄物の連続炭化処理装置。
An apparatus for continuously carbonizing an object to be treated of sludge or organic waste containing organic matter, wherein a supply part for the object to be treated is provided above the continuous carbonization part in a reducing atmosphere, and continuous carbonization below the supply part In the apparatus for continuously carbonizing while lowering the object to be processed by matching the through holes provided in each of the upper opening plate and the lower opening plate in which at least one of the moving parts is moved,
A cooling jacket is provided on the upper opening plate or the lower opening plate,
A cooling jacket that protrudes leaving a passage hole below the upper opening plate is provided,
An apparatus for continuously carbonizing organic waste, wherein the object to be treated is urged to fall by interference of a cooling jacket when the upper opening plate is moved .
連続炭化部の周囲に冷却用ジャケットを設けた請求項1記載の有機質廃棄物の連続炭化処理装置。The continuous carbonization processing apparatus of the organic waste of Claim 1 which provided the jacket for cooling around the continuous carbonization part. 連続炭化部下部の炭化物取出し口と被処理対象物の供給部との間に炭化物のフィ−ドバック手段を設け、該炭化物を被処理対象物と混合するようにした請求項1記載の有機質廃棄物の連続炭化処理装置。Carbides Fi between outlet carbide continuous carbonization subordinates portion and the supply portion of the object to be processed - Dobakku a means, organic waste according to claim 1, wherein which is adapted to mix the object to be processed a carbon compound Equipment for continuous carbonization.
JP2001169619A 2001-06-05 2001-06-05 Continuous carbonization equipment for organic waste Expired - Fee Related JP4772213B2 (en)

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JP2001169619A JP4772213B2 (en) 2001-06-05 2001-06-05 Continuous carbonization equipment for organic waste
TW90123975A TW553905B (en) 2001-06-05 2001-09-27 An apparatus for processing organic waste into continuous carbonization

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Publication number Priority date Publication date Assignee Title
JPS588597A (en) * 1981-07-08 1983-01-18 Shinryo Air Conditioning Co Ltd Dry-distillation gasifier for sludge
JPH0691245A (en) * 1992-09-16 1994-04-05 Takenaka Komuten Co Ltd Treatment of waste
JP2952160B2 (en) * 1994-09-21 1999-09-20 プラント技販工業株式会社 Waste incineration method, grate, incinerator and incinerator
JP3333706B2 (en) * 1997-03-18 2002-10-15 強 ▲高▼原 Sewerage sludge carbonization method and sewerage sludge carbonization equipment
JPH11310782A (en) * 1998-04-30 1999-11-09 Hitachi Zosen Corp Carbonizing method for sludge
JP3682376B2 (en) * 1998-08-31 2005-08-10 株式会社まさなみ鉄工 Method for producing carbon-containing granular activated sludge fertilizer
JP2000169130A (en) * 1998-12-08 2000-06-20 Masanami Tekko:Kk Production of granular organic sludge carbon from activated sludge
JP3556852B2 (en) * 1999-02-01 2004-08-25 株式会社プランテック Sludge co-firing equipment
JP3199696B2 (en) * 1999-03-03 2001-08-20 株式会社まさなみ鉄工 Waste continuous carbonization method
JP3340083B2 (en) * 1999-04-06 2002-10-28 株式会社まさなみ鉄工 Continuous treatment equipment for sewage sludge

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