JP2010137214A - Garbage carbonization processing machine - Google Patents

Garbage carbonization processing machine Download PDF

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JP2010137214A
JP2010137214A JP2009003830A JP2009003830A JP2010137214A JP 2010137214 A JP2010137214 A JP 2010137214A JP 2009003830 A JP2009003830 A JP 2009003830A JP 2009003830 A JP2009003830 A JP 2009003830A JP 2010137214 A JP2010137214 A JP 2010137214A
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carbonization
garbage
pipe
combustion chamber
induction
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Deung Hyun Yun
登顯 尹
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • 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

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Drying Of Solid Materials (AREA)
  • Coke Industry (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a garbage carbonizing device for treating a large quantity of the garbage to be discharged from public restaurants, etc. <P>SOLUTION: A garbage carbonization processing machine is provided with: a body 10 having an insulation layer 11 formed on the inside surface thereof and a fire-retardant layer 12 formed on the inside surface of the insulation layer 11; a carbonization guide path 20' which is arranged in the internal space of the fire-retardant layer 12, and is divided into an upper-side heating furnace 30 and a lower-side combustion chamber 40 to have a downward-facing hemispherical shape in the cross section thereof; a cover arranged on the body 10 in order to open the heating furnace 30 selectively; a mixing screw arranged in the carbonization guide path 20' to be rotated by a driving motor 53 arranged on the outside of the body 10; a first burner and a second burner arranged separately in the combustion chamber 40; an exhaust pipe 43 one end of which is arranged at the bottom of the combustion chamber 40 and the other end of which is erected inside the combustion chamber 40 so as to penetrate the ceiling of the body 10; and a gas transfer pipe 44 arranged in the combustion chamber 40 so as to communicate the heating furnace 30 and the combustion chamber 40 with each other. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、大衆飲食店などから排出される多量の生ゴミを処理するための炭化装置に関する。より詳細には、本発明は、本体の内部空間を上下に区画して加熱炉と燃焼室を形成し、この加熱炉には所定の傾斜角を有する攪拌スクリューを並べて配設し、燃焼室にはバーナーと排気管を設け、加熱炉と燃焼室はガス移送管により連通させることによって、投入蓋を通じて加熱炉の内部に供給した生ゴミは加熱炉の熱気により熱分解され、この時生じた乾溜や有害ガスはガス移送管を通じて移送され、燃焼室では加熱炉の間接加熱と同時に乾溜や有害ガスを燃焼させて大気中に排出すると共に、攪拌スクリューにより移送される生ゴミは熱分解を通じて完全乾燥した状態の炭化物として排出させる、生ゴミ用炭化処理機に関するものである。   The present invention relates to a carbonization apparatus for processing a large amount of garbage discharged from a popular restaurant or the like. More specifically, the present invention forms a heating furnace and a combustion chamber by dividing the internal space of the main body into upper and lower portions, and a stirring screw having a predetermined inclination angle is arranged in the heating furnace. Is provided with a burner and an exhaust pipe, and the heating furnace and the combustion chamber are communicated with each other by a gas transfer pipe, so that the garbage supplied to the inside of the heating furnace through the charging lid is thermally decomposed by the hot air of the heating furnace, And harmful gases are transferred through gas transfer pipes, and in the combustion chamber, dry distillation and harmful gases are combusted simultaneously with indirect heating of the heating furnace and discharged into the atmosphere, and the garbage transferred by the stirring screw is completely dried through thermal decomposition. It is related with the carbonization processing machine for garbage which is discharged | emitted as the carbide | carbonized_material of the state which carried out.

最近、外食産業とサービス産業が発達するに伴って、一般家庭や大衆飲食店などから排出される生ゴミの発生及び排出量が増加している趨勢である。このような生ゴミは、規定されたシステムと関係法令によって、一定の経路を通じて回収して安全に処理されている。このような生ゴミの処理方法としては、大部分を地中に埋め込み又は焼却することが普遍的な方法であり、場合によっては多様な処理過程を経て動物用飼料や堆肥などに再加工される。   Recently, with the development of the restaurant and service industries, the generation and discharge of raw garbage from ordinary households and popular restaurants are increasing. Such garbage is collected and processed safely through a predetermined route according to a prescribed system and related laws and regulations. As a method for treating such garbage, it is a universal method that most of it is buried or incinerated in the ground, and in some cases, it is reprocessed into animal feed or compost through various treatment processes. .

しかし、埋め込みによる生ゴミの処理方法には広い埋立地が必要であり、衛生的な側面と環境的な側面においても不利な結果を招くため、地方自治体と住民の反対がある場合がある。また、動物の副産物の場合には、関係法令によって飼料を作ることが求められ、又はこれを埋め込んで処理することが禁止され若しくは厳格に制限される場合がある。   However, there are cases where there is opposition between local governments and residents because the disposal method of garbage by embedding requires a large landfill site, which also has adverse consequences in terms of hygiene and environmental aspects. In addition, in the case of animal by-products, it may be required to make feed according to relevant laws or regulations, and it may be prohibited or strictly limited to embed and process it.

すなわち、承認された既存の埋立地の場合、生ゴミの受け入れが飽和状態となって新しい埋立地の指定が不可避であるにも関わらず、当該地域の住民は勿論、地方自治体の反対が深刻であるため、新しい埋立地を指定することにおいて多くの困難を経験している。また、環境的な側面においても、埋め込み過程で発生する悪臭や浸出水による土壌の汚染、又は有害ガスによる深刻な大気汚染が発生すると報告されているため、生ゴミに対する好ましい処理方法としては不適合である。   In other words, in the case of existing landfills that have been approved, the acceptance of raw garbage has become saturated and the designation of new landfills is inevitable. As such, it has experienced many difficulties in designating new landfills. Also, in terms of environmental aspects, it has been reported that bad odor generated during the embedding process, soil contamination due to leachate, or serious air pollution due to harmful gases will occur. is there.

このような実情から、前述したような生ゴミに対する効果的な処理方法として、焼却及び炭化方法が台頭している。この方法によれば、一定水準の設備を備えた状態で生ゴミを高温で焼却させてこれを処理し、又は乾燥と炭化過程を経て含水率が極めて低い炭化物の状態で排出させることによって、炭化物を堆肥や埋立土用途に活用することができる。   From such a situation, incineration and carbonization methods have emerged as an effective treatment method for raw garbage as described above. According to this method, the garbage is incinerated at a high temperature in a state equipped with a certain level of equipment and treated, or discharged through a drying and carbonization process in the form of a carbide having a very low moisture content. Can be used for compost and landfill applications.

しかしながら、焼却及び炭化方法による生ゴミの処理方法では多量の有害ガスや浸出水が発生するが、現在は埋め込み以外の最も効果的な処理方法として知られているので、過度な運営費や施設費の負担にも拘わらず、不可避的に運営している実情である。   However, a large amount of harmful gas and leachate is generated in the method of treating garbage by incineration and carbonization, but since it is currently known as the most effective treatment method other than embedding, excessive operating costs and facility costs In spite of the burden of, it is the fact that it is inevitably operated.

また、このような焼却及び炭化方法は回収した生ゴミを破砕させた状態で、これを乾燥させた後、焼却または炭化させるものであり、乾燥過程と焼却または炭化過程で多量のエネルギーを消費する。   In addition, such incineration and carbonization methods are such that the collected garbage is crushed, dried, then incinerated or carbonized, and a large amount of energy is consumed in the drying and incineration or carbonization processes. .

また、前述したような一般的な生ゴミの処理方法は、生ゴミの貯蔵段階と生ゴミの破砕段階、脱水段階、乾燥段階及び炭化段階で多量の浸出水及び廃水が発生する。このような浸出水と廃水は2次処理処置を通じて浄化しなければならないため、2重の処理費用が必要である問題点がある。   Further, in the general garbage disposal method as described above, a large amount of leachate and wastewater is generated in the garbage storage stage, the garbage crushing stage, the dewatering stage, the drying stage, and the carbonization stage. Since such leachate and wastewater must be purified through secondary treatment, there is a problem that double treatment costs are required.

これを詳細に説明すると、一般的な生ゴミの焼却処理過程において、大型貯蔵タンク内に回収したゴミを、破砕機を利用して細かく破砕した後、これに対する含水率を低下するために脱水過程を行い、脱水した生ゴミは含水率をより低下させるために乾燥過程を経ると共に、乾燥した状態の生ゴミは焼却または炭化過程を経て処理する。   This will be explained in detail. In a general garbage incineration process, the garbage collected in the large storage tank is finely crushed using a crusher and then dehydrated to reduce the moisture content. The dehydrated garbage undergoes a drying process in order to further reduce the moisture content, and the dried garbage is treated through an incineration or carbonization process.

一方、前述したような処理過程においては、廃水と有害ガス及び粉塵と炭化物が最終的に排出される。この時、廃水は貯蔵庫から発生する大量の浸出水と破砕及び脱水、乾燥過程で発生する廃水を全て集めて別の浄化槽に回収し、浄化槽内の廃水は化学処理を通じて海洋に投棄する方法で処理される。しかし、ロンドン協約によれば、2012年からは生ゴミを含んだ有機性廃棄物に対する浸出水や廃水に対する浄化水の海洋投棄が全面的に禁止される。そのため、廃水処理施設に対する拡充や廃水処理に対する所要費用が大きく増大することが予想される。   On the other hand, in the treatment process as described above, waste water, harmful gas, dust and carbide are finally discharged. At this time, waste water is collected by collecting a large amount of leachate generated from the storage, waste water generated during crushing, dehydration, and drying and collecting it in a separate septic tank. Is done. However, according to the London Agreement, from 2012, ocean dumping of leachate for organic waste containing raw garbage and purified water for wastewater will be completely prohibited. Therefore, it is expected that the required cost for expansion and wastewater treatment for wastewater treatment facilities will increase greatly.

また、前述したような処理過程で発生する有害ガスには多量の粉塵が含まれているため、一次的に高温で有害ガスに対する燃焼を進行させた後、燃焼ガス及び粉塵を最終的に湿式粉塵除去装置を経て大気中に排出させる。ところが、前述したような焼却処理過程で発生するダイオキシンのような多量の有害ガスは公害と環境汚染を深刻に誘発するものと知られている。   In addition, since the harmful gas generated in the treatment process as described above contains a large amount of dust, after the combustion with respect to the harmful gas is primarily advanced at a high temperature, the combustion gas and dust are finally wet dust. It is discharged into the atmosphere through a removal device. However, a large amount of harmful gas such as dioxin generated in the incineration process as described above is known to cause serious pollution and environmental pollution.

さらに、前述したような湿式粉塵除去装置で使用する処理用水は多量の粉塵を含んでいるため、このような処理用水もやはり浸出水及び廃水の処理過程と同一な経路を経て浄化された後、海洋に投棄される。結局、海洋投棄による環境と費用的な側面で改善及び解決しなければならない問題が加重される原因になる。   Furthermore, since the treatment water used in the wet dust removal apparatus as described above contains a large amount of dust, such treatment water is also purified through the same process as the leachate and wastewater treatment process, Dumped into the ocean. In the end, the problem of having to be improved and solved in terms of environmental and cost aspects due to ocean dumping is weighted.

特に、焼却及び炭化過程と燃焼過程で消費する大部分の燃料として、石油エネルギーや電気エネルギーが使用されるため、大量の生ゴミを連続して処理するためには莫大な量のエネルギーが必要である。このように、使用するエネルギー消費量の増大により、生ゴミの埋め込み方法に比べて過度な処理費用が発生するため、長期的な側面で過度なエネルギー使用により競争力が低下すると共に、財源の確保にも相当な困難を経験している。   In particular, petroleum energy and electrical energy are used as the majority of fuel consumed in incineration and carbonization and combustion processes, so a huge amount of energy is required to continuously process a large amount of garbage. is there. In this way, an increase in energy consumption to be used results in excessive processing costs compared to the method of embedding garbage, so that in the long-term aspect, excessive energy use reduces competitiveness and secures financial resources. Also experienced considerable difficulties.

そこで、本発明は、最小の消費燃料だけでも比較的多量の生ゴミを効果的に炭化させることができ、従来の生ゴミに対する回収費用及び処理費用を大きく節減できると共に、環境的な側面においても環境親和的であって、従来の生ゴミ処理システムが有する上述した諸般の問題点を効果的に克服することのできる、生ゴミ用炭化処理機を提供することを目的とする。   Accordingly, the present invention can effectively carbonize a relatively large amount of garbage with only a minimum amount of fuel consumed, and can greatly reduce the collection cost and processing cost of conventional garbage, and also from an environmental aspect. An object of the present invention is to provide a carbonization processor for garbage which is environmentally friendly and can effectively overcome the above-mentioned various problems of conventional garbage disposal systems.

前述した目的を達成するために、本発明に係る生ゴミ用炭化処理機は、内面に断熱層が形成され、前記断熱層の内面には耐火層が形成される本体と、前記耐火層の内部空間に設けられて上側の加熱炉と下側の燃焼室に分割し、下半球状の断面形状を有する連続の炭化誘導管と、前記加熱炉を選択的に開放するため前記本体に開閉可能に設けられる投入蓋と、前記本体の外部に配設された駆動モーターにより回転されるように炭化誘導管の内に設けられる攪拌スクリューと、前記燃焼室に離間して設けられる第1バーナー及び第2バーナーと、一端は前記燃焼室の底に配設し、他端は前記本体の天頂に貫設されるように前記燃焼室の内部に立設される排気管と、前記加熱炉と燃焼室を互いに連通するように前記燃焼室の内に設けられるガス移送管と、を含み、前記第1バーナー及び第2バーナーは、加熱炉内部の炭化誘導管に投入された生ゴミを高熱により熱分解し、前記ガス移送管は、熱分解過程で生じた乾溜や有害ガスを燃焼室の内部へ運搬させて燃焼除去させ、前記炭化誘導管は、熱分解された生ゴミを本体の外部に排出可能なように構成されることを特徴とする。   In order to achieve the above-described object, the garbage carbonization apparatus according to the present invention includes a main body in which a heat insulating layer is formed on an inner surface, and a fire resistant layer is formed on the inner surface of the heat insulating layer, and an inner portion of the fire resistant layer. A space is divided into an upper heating furnace and a lower combustion chamber, and a continuous carbonization induction pipe having a lower hemispherical cross-sectional shape and the main body can be opened and closed to selectively open the heating furnace. A charging lid provided, a stirring screw provided in the carbonization induction tube so as to be rotated by a drive motor provided outside the main body, a first burner and a second provided separately in the combustion chamber A burner, one end is disposed at the bottom of the combustion chamber, and the other end includes an exhaust pipe standing inside the combustion chamber so as to penetrate the zenith of the main body, the heating furnace, and the combustion chamber. Gas transfer provided in the combustion chamber so as to communicate with each other The first burner and the second burner pyrolyze the raw garbage put into the carbonization induction pipe inside the heating furnace with high heat, and the gas transfer pipe is used for dry distillation and harmful generated in the pyrolysis process. The gas is transported to the inside of the combustion chamber to be burned and removed, and the carbonization induction pipe is configured to be able to discharge the pyrolyzed raw garbage to the outside of the main body.

本発明に係る生ゴミ用炭化処理機によれば、少なくとも30〜40Kgの生ゴミを一度に投入し、これを炭化処理できることは勿論、処理機の24時間フル稼働が可能であり、一般大衆飲食店などで発生する生ゴミを全て処理することができる。また、間接熱による生ゴミの熱分解過程で発生する乾溜ガスを回収し、回収した乾溜ガスの燃焼過程で発生する廃熱は投入した生ゴミの分解熱として作用するため、消費エネルギーの減少により経済性が向上する。また、加熱室内部の高熱により熱分解過程で発生する悪臭やガスなどが分解除去され排出されることにより、環境親和性も向上する。   According to the carbonization processing machine for garbage according to the present invention, at least 30 to 40 kg of garbage can be charged at a time and this can be carbonized, and the processing machine can be fully operated for 24 hours. All garbage generated in stores can be processed. In addition, the waste gas generated during the pyrolysis process of garbage due to indirect heat is recovered, and the waste heat generated during the combustion process of the collected dry distillation gas acts as the decomposition heat of the input garbage. Economic efficiency improves. Moreover, the environmental affinity is also improved by decomposing and removing malodors and gases generated in the thermal decomposition process due to high heat in the heating chamber.

本発明の一実施形態に係る炭化処理機の全体外形を示す正面図である。It is a front view which shows the whole external shape of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機の横断面図である。It is a cross-sectional view of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機のもう一つの横断面図である。It is another cross-sectional view of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機の攪拌スクリュー駆動部を示す側面図である。It is a side view which shows the stirring screw drive part of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機の側断面拡大図である。It is a side section enlarged view of the carbonization processing machine concerning one embodiment of the present invention. 本発明の一実施形態に係る炭化処理機のもう一つの側断面拡大図である。It is another side cross-sectional enlarged view of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機の攪拌移送部を示す平面拡大図である。It is a plane enlarged view which shows the stirring transfer part of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機の攪拌移送部を示す斜視図である。It is a perspective view which shows the stirring transfer part of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機の排出部の密閉状態を示す概略図である。It is the schematic which shows the sealing state of the discharge part of the carbonization processing machine which concerns on one Embodiment of this invention. 本発明の一実施形態に係る炭化処理機の排出部の開放状態を示す概略図である。It is the schematic which shows the open state of the discharge part of the carbonization processing machine which concerns on one Embodiment of this invention.

以下に添付図面を参照しながら、本発明の好適な実施の形態について詳細に説明する。なお、本明細書及び図面において、実質的に同一の機能構成を有する構成要素については、同一の符号を付することにより重複説明を省略する。   Exemplary embodiments of the present invention will be described below in detail with reference to the accompanying drawings. In addition, in this specification and drawing, about the component which has the substantially same function structure, duplication description is abbreviate | omitted by attaching | subjecting the same code | symbol.

各図に示すように、本発明に係る炭化処理機は、外部ケースを構成する本体10を備えており、本体10の内面にはセラミックウールでなった断熱層11を形成する。また断熱層11の内面には不定形耐火材であるキャスタブルでなった耐火層12が形成される。この断熱層11は本体内部の高温の熱気が外部に伝えられることを防止する役割をし、耐火層12は高温の熱気によって断熱層11が損傷されることを防止すると共に、高温の熱気が外部に伝わって損失されることを遮断する役割を果たす。   As shown in each figure, the carbonization processing machine according to the present invention includes a main body 10 constituting an outer case, and a heat insulating layer 11 made of ceramic wool is formed on the inner surface of the main body 10. In addition, a castable refractory layer 12 which is an amorphous refractory material is formed on the inner surface of the heat insulating layer 11. The heat insulating layer 11 serves to prevent high temperature hot air inside the main body from being transmitted to the outside, and the fireproof layer 12 prevents the heat insulating layer 11 from being damaged by the high temperature hot air, and the high temperature hot air is It plays a role in blocking the loss of being transmitted.

このような本体10の内部空間には下半球状の断面を有する炭化誘導管20、20′が並べて配設され、炭化誘導管20、20′により上側には加熱炉30が形成され、炭化誘導管20、20′の下側には燃焼室40が形成される。   In the internal space of the main body 10, carbonization induction pipes 20 and 20 ′ having a lower hemispherical cross section are arranged side by side, and a heating furnace 30 is formed on the upper side by the carbonization induction pipes 20 and 20 ′. A combustion chamber 40 is formed below the tubes 20, 20 '.

ここで、加熱炉30には本体10の外部から生ゴミを投入する投入蓋31が設けられており、投入蓋31は一般的な開閉手段を通じて開放され、及び密閉されることが可能な構造を有する。燃焼室30には本体10の外部から内部に向かって挿設された第1バーナー41と第2バーナー42が装着されている。   Here, the heating furnace 30 is provided with a charging lid 31 for charging garbage from the outside of the main body 10, and the charging lid 31 has a structure that can be opened and sealed through a general opening / closing means. Have. The combustion chamber 30 is provided with a first burner 41 and a second burner 42 inserted from the outside of the main body 10 toward the inside.

また、燃焼室30には排気管43が垂直に装着されており、先端は本体10の外部に露出している。燃焼室30の内部から垂直に立設されるガス移送管44は加熱炉30の内部空間に先端が露出するように形成されている。   Further, an exhaust pipe 43 is vertically installed in the combustion chamber 30, and the tip is exposed to the outside of the main body 10. The gas transfer pipe 44 erected vertically from the inside of the combustion chamber 30 is formed so that the tip is exposed in the internal space of the heating furnace 30.

また、第2バーナー42には燃焼室30の内部に延設された燃焼管42aが設けられており、燃焼管42aにはガス移送管44の下段が連通するように結合されている。   The second burner 42 is provided with a combustion pipe 42a extending inside the combustion chamber 30, and is connected to the combustion pipe 42a so that the lower stage of the gas transfer pipe 44 communicates therewith.

特に、炭化誘導管20、20′は一定の傾斜角を持って形成されており、2個の炭化誘導管20、20′は反対の傾斜角で互いに離間して配設されるので、これらの2個の炭化誘導管20、20′には端部に一定水準の段差が形成される。このような段差は生ゴミの自然的な落下移送を助けるためのものとして、炭化誘導管20、20′の端部には段差に対応する傾斜角を有する移送管20aを配設されている。   In particular, the carbonization induction pipes 20 and 20 'are formed with a certain inclination angle, and the two carbonization induction pipes 20 and 20' are disposed apart from each other with opposite inclination angles. The two carbonization induction pipes 20, 20 'are formed with a certain level of step at the end. Such a step is used to assist the natural fall transfer of garbage, and a transfer tube 20a having an inclination angle corresponding to the step is provided at the end of the carbonization induction tubes 20 and 20 '.

また、炭化誘導管20、20′の上部内側には投入した生ゴミを移送させるための攪拌スクリュー50、50′が各々内蔵されている。攪拌スクリュー50、50′は本体10に装着した別の駆動モーター53から伝えられる動力により自由回転が可能な状態で軸結合されている。これらの攪拌スクリュー50、50′は炭化誘導管20、20′の傾斜角と同一な傾斜角を有するように形成されて生ゴミの円滑な移送を助ける。   In addition, agitation screws 50 and 50 'for transferring the thrown-in garbage are incorporated in the upper inner sides of the carbonization induction tubes 20 and 20', respectively. The stirring screws 50 and 50 ′ are shaft-coupled in a state where they can be freely rotated by power transmitted from another drive motor 53 mounted on the main body 10. These agitating screws 50 and 50 'are formed to have the same inclination angle as that of the carbonization induction tubes 20 and 20' to facilitate smooth transfer of garbage.

この時、攪拌スクリュー50、50′には図8に示すように、四方に連続して突出した支持棒51、51′が形成されており、支持棒51、51′には傾斜角を有する移送翼52、52′が各々形成されている。したがって、攪拌スクリュー50、50′が回転すると、移送翼52、52′は炭化誘導管20、20′の内にある生ゴミを移送翼52、52′の傾斜方向に沿って一側から他側に移送させる。   At this time, as shown in FIG. 8, the stirring screws 50 and 50 'are formed with support rods 51 and 51' protruding continuously in four directions, and the support rods 51 and 51 'are transported with an inclination angle. Wings 52 and 52 'are respectively formed. Therefore, when the agitating screws 50 and 50 'rotate, the transfer blades 52 and 52' cause the garbage in the carbonization induction tubes 20 and 20 'to move from one side to the other along the inclined direction of the transfer blades 52 and 52'. To be transported.

特に、炭化誘導管20、20′において、一側の炭化誘導管20′の側端下部には排出管21が下方に突出しており、排出管21の下段には排出案内管22が連通されて横設される。排出案内管22の内部には、別の排出モーター23から伝えられる動力により回転が可能な状態で無軸スクリュー24が装着される。   In particular, in the carbonization induction pipes 20 and 20 ′, a discharge pipe 21 protrudes downward from a lower side end of the carbonization induction pipe 20 ′ on one side, and a discharge guide pipe 22 communicates with the lower stage of the discharge pipe 21. Horizontally installed. Inside the discharge guide tube 22, a non-axial screw 24 is mounted in a state where it can be rotated by power transmitted from another discharge motor 23.

また、排出管21には図9に示すように、排出管21を密閉させ及び開放させることができる開閉板60が装着される。本実施形態に係る生ゴミ炭化処理機は、ブラケットにより排出管21に装着される開閉モーター63と、この開閉モーター63のねじ軸64に螺合されるナット体62と、一端は開閉板60の底面にヒンジ結合され、他端はナット体62にヒンジ結合される回転リンク61と、をさらに含む。したがって、図10に示すように、開閉モーター63の作動によりねじ軸64が回転すると、これに螺合されたナット体62が摺動することによって、回転リンク61を介して開閉板60を上下に回動できる。   Further, as shown in FIG. 9, an opening / closing plate 60 capable of sealing and opening the discharge pipe 21 is attached to the discharge pipe 21. The garbage carbonization processing machine according to the present embodiment includes an opening / closing motor 63 attached to the discharge pipe 21 by a bracket, a nut body 62 screwed to the screw shaft 64 of the opening / closing motor 63, and one end of the opening / closing plate 60. A rotation link 61 is further included that is hinged to the bottom surface and hinged to the nut body 62 at the other end. Therefore, as shown in FIG. 10, when the screw shaft 64 is rotated by the operation of the opening / closing motor 63, the nut body 62 screwed on the sliding slides to move the opening / closing plate 60 up and down via the rotation link 61. Can rotate.

このような構造を有する本発明の生ゴミ炭化処理機の全体的な作動及び作用関係について順次説明する。   The overall operation and operational relationship of the garbage carbonization processor of the present invention having such a structure will be described in order.

まず、ユーザーは本体10の外面に露出した投入蓋31を開放して第1炭化誘導管20の内部に例えば30〜40Kgの生ゴミを投入する。この時、燃焼室40に位置した第1バーナー41を点火させると、火炎による燃焼室40内部の熱気が金属材でなった炭化誘導管20、20′を通じて伝渡されながら加熱炉30の内部温度が上昇するようになる。   First, the user opens the charging lid 31 exposed on the outer surface of the main body 10 and loads, for example, 30 to 40 kg of garbage into the first carbonization induction tube 20. At this time, when the first burner 41 located in the combustion chamber 40 is ignited, the internal temperature of the heating furnace 30 is transferred while the hot air inside the combustion chamber 40 due to the flame is transferred through the carbonization induction tubes 20 and 20 'made of a metal material. Will rise.

この時の燃焼室40の内部温度は、例えば約900℃程度が理想的であり、燃焼室40の熱気が伝渡される加熱炉30の内部温度は例えば500〜550℃が理想的である。   The internal temperature of the combustion chamber 40 at this time is ideally about 900 ° C., for example, and the internal temperature of the heating furnace 30 to which the hot air in the combustion chamber 40 is transferred is ideally 500 to 550 ° C., for example.

次に、前述のように設定した温度に到達すると、駆動モーター53を作動させて2個の攪拌スクリュー50、50′が同時に回転を開始する。この時、第1炭化誘導管20の内部に投入した生ゴミは、当該攪拌スクリュー50が回転することによって一側から他側に混合攪拌されながら移送するようになる。続いて、第1炭化誘導管20の端部に至った生ゴミは移送管20aを通じて他側の炭化誘導管20′の内部に自由落下しながら移送される。第2攪拌スクリュー50′は第2炭化誘導管20′の内部に供給された生ゴミを一側から他側に移送する。   Next, when the temperature set as described above is reached, the drive motor 53 is operated, and the two stirring screws 50 and 50 'start to rotate simultaneously. At this time, the garbage thrown into the inside of the first carbonization induction tube 20 is transferred while being mixed and stirred from one side to the other side as the stirring screw 50 rotates. Subsequently, the garbage that has reached the end of the first carbonization induction pipe 20 is transferred to the inside of the other carbonization induction pipe 20 'through the transfer pipe 20a while freely falling. The second agitating screw 50 'transfers the garbage supplied into the second carbonization induction tube 20' from one side to the other side.

このような生ゴミの移送過程において、生ゴミは移送翼52、52′により混合と攪拌及び粉砕が繰り返して持続的に行われながら移送される。したがって、高温の熱気に十分に露出しながら、無酸素状態の熱分解が進行される。   In the process of transferring raw garbage, the raw garbage is transferred by the transfer blades 52 and 52 'while being continuously mixed and stirred and pulverized. Accordingly, oxygen-free thermal decomposition proceeds while sufficiently exposed to high-temperature hot air.

この時、前述したような熱分解過程において、生ゴミから水蒸気と乾溜ガスや有害ガスが排出される。このような水蒸気と乾溜や有害ガスは加熱炉30の内部圧力を上昇させる作用をするため、結局ガス移送管44を通じて燃焼室40に排出される過程が進行する。燃焼室40は排気管43により外気と同一の圧力になっているので、前述したように加熱炉30内部での圧力を上昇させる水蒸気と乾溜や有害ガスは自然にガス移送管44を通じて燃焼室40の内部に排出される。   At this time, in the pyrolysis process as described above, water vapor, dry distillation gas and harmful gas are discharged from the garbage. Since such steam, dry distillation, and harmful gas act to increase the internal pressure of the heating furnace 30, the process of exhausting to the combustion chamber 40 through the gas transfer pipe 44 eventually proceeds. Since the combustion chamber 40 is at the same pressure as the outside air by the exhaust pipe 43, as described above, the steam, dry distillation, and harmful gas that increase the pressure in the heating furnace 30 naturally pass through the gas transfer pipe 44 through the combustion chamber 40. It is discharged into the inside.

これによって、前述したように水蒸気と乾溜や有害ガスの発生が開始すると、第1バーナー41の稼動を中断させて第2バーナー42を稼動させる。第2バーナー42の稼動によって発生する火炎は水蒸気と乾溜や有害ガスを蒸発及び燃焼させる役割をすると共に、燃焼が可能な乾溜ガスは第2バーナー42の火炎を増大させる役割をする。したがって、乾溜ガスの追加によって第1バーナー41より弱い火炎で第2バーナー42を稼動させても乾溜ガスが燃焼しながら、燃焼室40の内部温度は一定の水準に維持される。   Accordingly, as described above, when the generation of water vapor, dry distillation, or harmful gas starts, the operation of the first burner 41 is interrupted and the second burner 42 is operated. The flame generated by the operation of the second burner 42 plays a role of evaporating and burning water vapor, dry distillation, and harmful gas, and the dry distillation gas capable of combustion plays a role of increasing the flame of the second burner 42. Therefore, even if the second burner 42 is operated with a flame weaker than the first burner 41 by adding the dry distillation gas, the internal temperature of the combustion chamber 40 is maintained at a constant level while the dry distillation gas is combusted.

したがって、生ゴミの熱分解過程で発生する乾溜ガスを回収して熱源として使用することによって、生ゴミの炭化に必要な消耗エネルギー量を大きく低減することができる。   Therefore, the amount of consumed energy required for carbonization of garbage can be greatly reduced by collecting the dry distillation gas generated during the pyrolysis process of garbage and using it as a heat source.

また、前述したような炭化過程が約3〜4時間程度進行すると、生ゴミは完全に乾燥した状態の炭化物に変わる。この時にはバーナーの稼動を中断させて排出管21を開放して炭化誘導管20、20′の内部にある炭化物を外部に排出させる。   Further, when the carbonization process as described above proceeds for about 3 to 4 hours, the garbage is changed to a completely dried carbide. At this time, the operation of the burner is interrupted, the discharge pipe 21 is opened, and the carbides inside the carbonization induction pipes 20 and 20 'are discharged to the outside.

すなわち、排出管21に位置した開閉板60を下方に開放した状態で攪拌スクリュー50、50′を回転させると、移送翼52、52′の回転傾斜角により炭化誘導管20、20′の内部にある炭化物が移送されながら、開放状態の排出管21に落下する。続いて、排出管21の下段に横設された排出案内管22に炭化物が落下すると、排出モーター23を回転させて無軸スクリュー24により炭化物が本体10の外部に排出されるようになる。   That is, when the stirring screws 50 and 50 'are rotated with the opening and closing plate 60 positioned in the discharge pipe 21 opened downward, the carbonization induction pipes 20 and 20' are brought into the inside of the carbonization induction pipes 20 and 20 'by the rotation inclination angles of the transfer blades 52 and 52'. While a certain carbide is transferred, it falls to the discharge pipe 21 in an open state. Subsequently, when the carbide falls on the discharge guide tube 22 provided in the lower stage of the discharge pipe 21, the discharge motor 23 is rotated and the carbide is discharged to the outside of the main body 10 by the non-axial screw 24.

以上、添付図面を参照しながら本発明の好適な実施形態について詳細に説明したが、本発明はかかる例に限定されない。本発明の属する技術の分野における通常の知識を有する者であれば、特許請求の範囲に記載された技術的思想の範疇内において、各種の変更例または修正例に想到し得ることは明らかであり、これらについても、当然に本発明の技術的範囲に属するものと了解される。   The preferred embodiments of the present invention have been described in detail above with reference to the accompanying drawings, but the present invention is not limited to such examples. It is obvious that a person having ordinary knowledge in the technical field to which the present invention pertains can come up with various changes or modifications within the scope of the technical idea described in the claims. Of course, it is understood that these also belong to the technical scope of the present invention.

以上のように、本発明に係る生ゴミ炭化処理機は、比較的簡単な構成だけでも多量の生ゴミを炭化処理できると共に、回収した乾溜ガスの燃焼廃熱を活用するので、炭化に必要なエネルギー消費量を大きく減らすことができ経済性を向上させる。   As described above, the garbage carbonization processor according to the present invention can carbonize a large amount of garbage even with a relatively simple configuration and utilizes the combustion waste heat of the collected dry distillation gas. Energy consumption can be greatly reduced, improving economy.

10 本体、11 断熱層、12 耐火層、20、20′ 炭化誘導管、20a 移送管、21 排出管、22 排出案内管、23 排出モーター、24 無軸スクリュー、30 加熱炉、31 投入蓋、40 燃焼室、41 第1バーナー、42 第2バーナー、42a 燃焼管、43 排気管、44 ガス移送管、50、50′ 攪拌スクリュー、51、51′ 支持棒、52、52′ 移送翼、53 駆動モーター、60 開閉板、61 回転リンク、62 ナット体、63 開閉モーター、64 ねじ軸
DESCRIPTION OF SYMBOLS 10 Main body, 11 Heat insulation layer, 12 Refractory layer, 20, 20 'Carbonization induction pipe, 20a Transfer pipe, 21 Discharge pipe, 22 Discharge guide pipe, 23 Discharge motor, 24 Non-axial screw, 30 Heating furnace, 31 Input lid, 40 Combustion chamber, 41 1st burner, 42 2nd burner, 42a Combustion tube, 43 Exhaust tube, 44 Gas transfer tube, 50, 50 'Stir screw, 51, 51' Support rod, 52, 52 'Transfer blade, 53 Drive motor , 60 Opening and closing plate, 61 Rotating link, 62 Nut body, 63 Opening and closing motor, 64 Screw shaft

Claims (10)

内面に断熱層11が形成され、前記断熱層11の内面には耐火層12が形成される本体10と、
前記耐火層12の内部空間に設けられて上側の加熱炉30と下側の燃焼室40に分割し、下半球状の断面形状を有する連続の炭化誘導管20、20′と、
前記加熱炉30を選択的に開放するため前記本体10に開閉可能に設けられる投入蓋31と、
前記本体10の外部に配設された駆動モーター53により回転されるように炭化誘導管20、20′の内に設けられる攪拌スクリュー50、50′と、
前記燃焼室40に離間して設けられる第1バーナー41及び第2バーナー42と、
一端は前記燃焼室40の底に配設し、他端は前記本体10の天頂に貫設されるように前記燃焼室40の内部に立設される排気管43と、
前記加熱炉30と燃焼室40を互いに連通するように前記燃焼室40の内に設けられるガス移送管44と、を含み、
前記第1バーナー41及び第2バーナー42は、加熱炉30内部の炭化誘導管20、20′に投入された生ゴミを高熱により熱分解し、
前記ガス移送管44は、熱分解過程で生じた乾溜や有害ガスを燃焼室40の内部へ運搬させて燃焼除去させ、
前記炭化誘導管20、20′は、熱分解された生ゴミを本体10の外部に排出可能なように構成されることを特徴とする、
生ゴミ用炭化処理機。
A main body 10 on which an insulating layer 11 is formed on the inner surface, and a refractory layer 12 is formed on the inner surface of the insulating layer 11;
A continuous carbonization induction tube 20, 20 ′ provided in the internal space of the refractory layer 12 and divided into an upper heating furnace 30 and a lower combustion chamber 40 and having a lower hemispherical cross-sectional shape;
A charging lid 31 that can be opened and closed on the main body 10 to selectively open the heating furnace 30;
Agitation screws 50, 50 'provided in the carbonization induction tubes 20, 20' so as to be rotated by a drive motor 53 disposed outside the main body 10;
A first burner 41 and a second burner 42 provided apart from the combustion chamber 40;
One end is disposed at the bottom of the combustion chamber 40, and the other end is an exhaust pipe 43 standing inside the combustion chamber 40 so as to penetrate the zenith of the main body 10.
A gas transfer pipe 44 provided in the combustion chamber 40 so that the heating furnace 30 and the combustion chamber 40 communicate with each other;
The first burner 41 and the second burner 42 thermally decompose raw garbage put into the carbonization induction tubes 20 and 20 'inside the heating furnace 30 with high heat,
The gas transfer pipe 44 carries dry combustion and harmful gas generated in the thermal decomposition process to the inside of the combustion chamber 40 for combustion removal,
The carbonization induction pipes 20 and 20 'are configured to discharge the thermally decomposed garbage to the outside of the main body 10.
Carbonization machine for garbage.
前記断熱層11は、セラミックウールにより形成されることを特徴とする、請求項1に記載の生ゴミ用炭化処理機。   The said heat insulation layer 11 is formed with ceramic wool, The carbonization processing machine for garbage of Claim 1 characterized by the above-mentioned. 前記耐火層12は、不定形耐火材であるキャスタブルで形成されることを特徴とする、請求項1に記載の生ゴミ用炭化処理機。   2. The garbage carbonization apparatus according to claim 1, wherein the refractory layer 12 is formed of a castable that is an irregular refractory material. 前記炭化誘導管20、20′は、反対の傾斜角を有して互いに離間して設けられ、
前記炭化誘導管20、20′の内部に装着される前記攪拌スクリュー50、50′は、前記炭化誘導管20、20′と同一の傾斜角を有するように形成され、
第1炭化誘導管20に投入された生ゴミを、第1攪拌スクリュー50の回転を通じて他端部に移送し、当該他端部において隣り合う炭化誘導管20、20′の高さの差により第1炭化誘導管20から第2炭化誘導管20′の内部に落下移送し、第2炭化誘導管20′の内部において第2攪拌スクリュー50′の回転により一側から他側に攪拌移送するように構成されることを特徴とする、
請求項1に記載の生ゴミ用炭化処理機。
The carbonization guide tubes 20 and 20 'are spaced apart from each other with opposite inclination angles;
The stirring screws 50 and 50 ′ mounted inside the carbonization induction tubes 20 and 20 ′ are formed to have the same inclination angle as the carbonization induction tubes 20 and 20 ′.
The garbage thrown into the first carbonization induction pipe 20 is transferred to the other end through the rotation of the first stirring screw 50, and the first carbonization induction pipe 20 and 20 'are adjacent to each other at the other end. The first carbonization induction pipe 20 is dropped and transferred into the second carbonization induction pipe 20 ', and the second carbonization induction pipe 20' is stirred and transferred from one side to the other side by the rotation of the second stirring screw 50 '. Is composed of,
The carbonization processing machine for garbage of Claim 1.
前記第1炭化誘導管20と前記第2炭化誘導管20′の端部は、所定の角度で傾斜して設けられた移送管20aにより互いに連結されて、前記第1炭化誘導管20から移送された生ゴミを前記移送管20aを通じて前記第2炭化誘導管20′の内部に落下移送するように構成されることを特徴とする、
請求項4に記載の生ゴミ用炭化処理機。
End portions of the first carbonization induction pipe 20 and the second carbonization induction pipe 20 ′ are connected to each other by a transfer pipe 20a provided to be inclined at a predetermined angle, and transferred from the first carbonization induction pipe 20. The raw garbage is configured to fall and transfer into the second carbonization induction pipe 20 ′ through the transfer pipe 20a.
The garbage carbonization processing machine according to claim 4.
前記第2バーナー42には、前記燃焼室40の内部に向かって延びた燃焼管42aが連設され、前記燃焼管42aには前記ガス移送管44の下段が連設されて、前記第2バーナー42の点火で生じた高熱により前記ガス移送管44を通じて排出される乾溜や有害ガスを燃焼及び除去するように構成されることを特徴とする、
請求項1に記載の生ゴミ用炭化処理機。
A combustion pipe 42a extending toward the inside of the combustion chamber 40 is connected to the second burner 42. A lower stage of the gas transfer pipe 44 is connected to the combustion pipe 42a, and the second burner is connected. It is configured to combust and remove dry distillation and harmful gas discharged through the gas transfer pipe 44 due to high heat generated by ignition of 42.
The carbonization processing machine for garbage of Claim 1.
前記攪拌スクリュー50、50′には、四方に突出する支持棒51、51′が連設され、前記支持棒51、51′には、当該支持棒51、51′の中心軸から所定の角度で傾斜した移送翼52、52′が設けられて、前記炭化誘導管20、20′の内にある生ゴミを前記攪拌スクリュー50、50′の回転時に前記移送翼52、52′により一側から他側に移送するように構成されることを特徴とする、
請求項1に記載の生ゴミ用炭化処理機。
Support rods 51 and 51 'projecting in four directions are connected to the stirring screws 50 and 50', and the support rods 51 and 51 'are arranged at a predetermined angle from the central axis of the support rods 51 and 51'. Inclined transfer blades 52 and 52 ′ are provided, and garbage inside the carbonization induction pipes 20 and 20 ′ is removed from one side by the transfer blades 52 and 52 ′ when the stirring screws 50 and 50 ′ are rotated. Characterized by being transported to the side,
The carbonization processing machine for garbage of Claim 1.
一側の前記炭化誘導管20′の端部には排出管21が連設され、前記排出管21には開閉板60が装着され、前記開閉板60の作動によって前記炭化誘導管20′の内にある炭化物を選択的に排出するように構成されることを特徴とする、
請求項1に記載の生ゴミ用炭化処理機。
A discharge pipe 21 is continuously connected to an end of the carbonization induction pipe 20 ′ on one side, and an opening / closing plate 60 is attached to the discharge pipe 21, and the inside of the carbonization induction pipe 20 ′ is operated by the operation of the opening / closing plate 60. Characterized in that it is configured to selectively discharge carbides in
The carbonization processing machine for garbage of Claim 1.
前記排出管21は、その下段に連絡される排出案内管22が横設され、前記排出案内管22の内部には排出モーター23に連結された無軸スクリュー24が内蔵されて、前記排出案内管22に供給される炭化物が前記無軸スクリュー24の回転により横方向に排出されるように構成されることを特徴とする、
請求項8に記載の生ゴミ用炭化処理機。
The discharge pipe 21 is provided with a discharge guide pipe 22 that communicates with the lower stage thereof, and a non-axial screw 24 that is connected to a discharge motor 23 is built in the discharge guide pipe 22. The carbide supplied to 22 is configured to be discharged laterally by the rotation of the non-axial screw 24,
The garbage carbonization processing machine according to claim 8.
ブラケットにより前記排出管21に装着される開閉モーター63と、当該開閉モーター63のねじ軸64に螺合されるナット体62と、一端は前記開閉板60の底面にヒンジ結合され、他端は前記ナット体62にヒンジ結合される回転リンク61と、をさらに含み、
前記開閉モーター63の作動により前記ねじ軸64が回転すると、前記ナット体62が摺動することによって、前記回転リンク61を介して前記開閉板60を上下に回動できるように構成されることを特徴とする、
請求項8に記載の生ゴミ用炭化処理機。
An opening / closing motor 63 mounted on the discharge pipe 21 by a bracket, a nut body 62 screwed to a screw shaft 64 of the opening / closing motor 63, one end hinged to the bottom surface of the opening / closing plate 60, and the other end A rotating link 61 hinged to the nut body 62;
When the screw shaft 64 is rotated by the operation of the opening / closing motor 63, the opening / closing plate 60 can be turned up and down via the rotating link 61 by sliding the nut body 62. Features
The garbage carbonization processing machine according to claim 8.
JP2009003830A 2008-12-15 2009-01-09 Garbage carbonization processing machine Pending JP2010137214A (en)

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