JP3129814U - Magnetized air supply type fumigation equipment - Google Patents

Magnetized air supply type fumigation equipment Download PDF

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JP3129814U
JP3129814U JP2006010043U JP2006010043U JP3129814U JP 3129814 U JP3129814 U JP 3129814U JP 2006010043 U JP2006010043 U JP 2006010043U JP 2006010043 U JP2006010043 U JP 2006010043U JP 3129814 U JP3129814 U JP 3129814U
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fumigation
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guide plate
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健司 下山
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テクノシナジー株式会社
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Abstract

【課題】含水処理物でも効果に焼却処理可能とし、ダイオキシンの発生を抑制する。
【解決手段】処理筐体は、頂部に開閉蓋付きの処理物投入口を、内壁と間に循環路を形成して内設され、上下に連通する処理物蓄積空間の形成された矩形筒体を備え、一方の下部対抗側面に固定された傾斜案内板の表面内側に燻蒸処理空間を形成すると共に傾斜案内板裏面と筐体壁面の間に三角形状の貯気室を形成し、他方の下部対抗側面に扉14付きの灰取出し口を有し、処理筐体1の底面に前記貯記室に連通する給気配管及び該給気配管に配設の磁化手段、流量調整弁及び傾斜案内板から燻蒸処理室に水平上で対抗して複数配設される給気パイプを含む磁化給気装置を備え、処理筐体1の上部に燻蒸煙の消煙・脱臭処理用の水タンクを備え、前記傾斜案内板の周縁に処理物の水分を燻蒸処理室下面へ導く通口が形成されている。
【選択図】図1
An object of the present invention is to effectively incinerate even a water-containing treated product and suppress the generation of dioxins.
A processing case has a rectangular cylindrical body in which a processing object inlet with an open / close lid is formed at the top, a circulation path is formed between the inner wall and a processing object accumulation space communicating vertically is formed. A fumigation treatment space is formed inside the front surface of the inclined guide plate fixed to one lower opposing side surface, and a triangular storage chamber is formed between the rear surface of the inclined guide plate and the wall of the housing, and the other lower portion There is an ash outlet port with a door 14 on the opposite side, an air supply pipe communicating with the storage chamber on the bottom surface of the processing housing 1, magnetizing means disposed in the air supply pipe, a flow rate adjusting valve, and an inclined guide plate A magnetizing air supply device including a plurality of air supply pipes arranged horizontally against the fumigation processing chamber, and a water tank for fumigation smoke deodorizing and deodorizing treatment at the upper part of the processing housing 1; A through hole is formed at the peripheral edge of the inclined guide plate to guide the moisture of the processed material to the lower surface of the fumigation chamber.
[Selection] Figure 1

Description

この出願の考案は、金属、ガラス・石類等無機質以外の廃棄物を含む各種処理物を薫蒸処理する燻蒸処理装置であって、薫蒸処理に際して、燻蒸に必要な給気を、予め強力な磁気装置を通過させることにより磁気イオン化して磁化給気し、低温度(例えば370℃前後の温度)で熱処理でありながら、ダイオキシンの発生を効果的に低下抑制する燻蒸処理を可能とする磁化給気式燻蒸処理装置に関する。 The device of this application is a fumigation processing apparatus for fumigating various processed materials including non-inorganic waste such as metal, glass, stones, and the like. Magnetization that allows magnetic ionization by passing through a magnetic device and magnetization supply, and enables fumigation treatment that effectively reduces the generation of dioxins while performing heat treatment at a low temperature (for example, a temperature around 370 ° C.). The present invention relates to an air supply type fumigation apparatus.

従来の焼却炉は、灰とゴミの環境を網で隔てているロストルが必要であり、着火するバーナーを備え、また、ダイオキシン生成の原因が、不完全燃焼による酸素の滞留及び処理温度が<400℃〜800℃>範囲での処理であるとされており、このため、800℃以上の高温での処理を義務付けられ、煙突から出てくる煙は燃やすための二次燃焼機を必要とするものであった。 Conventional incinerators require a rooster that separates the ash and trash environment with a net, is equipped with an igniting burner, and the cause of dioxin generation is oxygen retention and processing temperature <400 due to incomplete combustion. It is said that it is processing in the range of ℃ ~ 800 ℃> , therefore, processing at a high temperature of 800 ℃ or more is obligatory, and the smoke coming out of the chimney requires a secondary combustor to burn Met.

従来、廃棄物処理は、燃焼炉による燃焼処理装置において、ダイオキシンを分解して無害化するため、800℃以上の高温で処理する高温焼却炉を必要とするものであり、この場合、高温焼却であるため必然的に炉の耐久性に課題を残し、メンテナンスの必要から維持経費を含めたトータルコストが嵩むものであった(特開平11−230528)。   Conventionally, waste treatment requires a high-temperature incinerator that treats at a high temperature of 800 ° C. or higher in order to decompose and detoxify dioxins in a combustion treatment apparatus using a combustion furnace. For this reason, there is inevitably a problem in the durability of the furnace, and the total cost including the maintenance cost increases due to the necessity of maintenance (Japanese Patent Laid-Open No. 11-230528).

また、ダイオキシンの発生なく廃棄物を乾留炭化処理する乾留炭化処理装置が存在し、励起した燃焼用空気を処理室に導入するに際して、処理室の周囲の複数の空気導入口から、供給するようにし、廃棄物の低温乾留処理を安定的にする装置が提案されている(特開2005−29600)。   In addition, there is a carbonization carbonization apparatus that performs carbonization of waste without the generation of dioxins, and when the excited combustion air is introduced into the processing chamber, it is supplied from a plurality of air inlets around the processing chamber. An apparatus for stabilizing the low-temperature carbonization treatment of waste has been proposed (Japanese Patent Laid-Open No. 2005-29600).

この先行装置においては、積重ねられた廃棄物は処理室内で先ず乾留され、次いで炭化されるので、炭化された廃棄物は磁界により励起された燃焼用空気の導入により、高温となっている乾留炭化物が励起された燃焼用空気に触れることで燃焼せずに炭化されて微粒化される乾留炭化処理が連続的に進行する。その際、低温乾留が90℃〜120℃以下の低温で効率よく乾留処理できる。その後、処理室からの排ガスは水プール上を循環する煙道Pを通過させ、排ガス中の煤やガス成分の一部をトラップし、更に黒鉛ヒーターからなる加熱装置により当該排ガスを800〜1200℃に加熱し、異臭発生源と煤を燃焼し、排ガスを無害化・無色化するものある。しかし、この装置の場合、廃棄物が、湿気又は水分の多く含んだ含水性の廃棄物の場合には、乾留炭化処理する乾留炭化処理装置としての使用することはできず、使用できる廃棄物に制約を受け、使用上の制約があることで問題を有するものであり、また、排ガスを無害化・無色化のために水プール以外に加熱装置など別途装置を付設しなければならず、追加装置が必要であり、乾留炭化処理装置自体が複雑となり、高価になるという問題があった。 In this prior apparatus, the stacked waste is first carbonized in the processing chamber and then carbonized, so that the carbonized waste is heated to a high temperature by introducing combustion air excited by a magnetic field. The carbonization process of carbonization without carbonization and atomization proceeds continuously by touching the combustion air excited by. At that time, low-temperature carbonization can be efficiently carbonized at a low temperature of 90 ° C. to 120 ° C. or less. Thereafter, the exhaust gas from the treatment chamber passes through the flue P circulating on the water pool, traps some of the soot and gas components in the exhaust gas, and further, the exhaust gas is 800-1200 ° C. by a heating device comprising a graphite heater. It is heated to burn the off-flavor source and soot, making the exhaust gas harmless and colorless. However, in the case of this device, if the waste is a water-containing waste containing a lot of moisture or moisture, it cannot be used as a dry distillation carbonization device for carbonizing carbonization, and it can be used as a usable waste. There are problems due to restrictions and restrictions on use. In addition to the water pool, a separate device such as a heating device must be added to make the exhaust gas harmless and colorless. However, there is a problem that the carbonization apparatus itself is complicated and expensive.

先行技術として、反応容器の外部に対向配した複数の磁石により、反応容器内に外部磁場を導入し磁波振動を形成し、これにより内部の有機物分子を励起、活性化させ、有機物分子を分解、反応を促進し、無機物、炭酸ガス、水、無水硫酸ガスを形成しながら炭化、灰化する有機物分解装置も存在する。この装置によれば、石油やガスなどの燃焼エネルギーを不要とし、ダイオキシンなどの有害化合物の発生を伴うことなく、有機廃棄物を効果的に分解する(特開2006−150295)。
しかしこの装置の場合も、廃棄物が湿気又は水分の多く含んだ含水性の廃棄物の場合には、有機物分解装置としての使用上制約を受け、使用上、利用できる廃棄物の適用範囲に制約を受けるので問題を残すものであった。
As a prior art, an external magnetic field is introduced into the reaction vessel by a plurality of magnets opposed to the outside of the reaction vessel to form a magnetic wave vibration, thereby exciting and activating the internal organic molecules, decomposing the organic molecules, There is also an organic matter decomposing apparatus that accelerates the reaction and carbonizes and incinerates while forming an inorganic substance, carbon dioxide gas, water, and anhydrous sulfuric acid gas. According to this apparatus, combustion energy such as oil and gas is unnecessary, and organic waste is effectively decomposed without generation of harmful compounds such as dioxin (Japanese Patent Laid-Open No. 2006-150295).
However, even in the case of this device, if the waste is a water-containing waste containing a lot of moisture or moisture, there is a restriction on the use as an organic matter decomposition device, and the application range of the waste that can be used is restricted. The problem was left.

さらに、先行技術として、各種廃棄物を、ダイオキシンを発生しない低温度(例えば400℃未満の温度)で熱処理して灰にすることを目的とするとした低温熱処理炉が存在する。
低温熱処理炉によれば、要するに、水平方向供気パイプ突設の下部熱処理室、間隙を保って内設の上部熱処理室、蓋付きの廃棄物等の投入口、煙筒・煙突付散水式浄煙槽、給気パイプに連通の空気室に連結される磁化空気の給送手段を備えるものであるとする。そして、基本的に水分の多い廃棄物(水分70%以上)、水分の少ない廃棄物(水分30%以下)を一緒に処理する場合に好ましいとある(特開2006−2612)。
しかし、低温熱処理炉において、実用上種々の課題を残しており、特に、追加処理物が水分の多い廃棄物(水分70%以上)である場合はもちろん、水分70%以下でも水が高温灰、火芯玉へと接近して滲み出す量が多い場合には、廃棄物に含まれた水分は、殆んど全て下部熱処理空間に流入して、却って消火の要因となり、下部熱処理室への水分の流入を防止できる工夫なく、このため、高温灰、火芯玉の維持が困難になり、実用上問題があり、低温熱処理炉として問題を残す結果となるものであった。
Furthermore, as a prior art, there is a low-temperature heat treatment furnace aimed at heat-treating various wastes at a low temperature (for example, a temperature of less than 400 ° C.) that does not generate dioxin to make ash.
In short, according to the low-temperature heat treatment furnace, the lower heat treatment chamber with a horizontal air supply pipe projecting, the upper heat treatment chamber with a gap inside, the waste inlet with a lid, etc., the sprinkler type smoke purification with a chimney / chimney Suppose that it has a supply means of magnetized air connected to a tank and an air chamber connected to an air supply pipe. Basically, it is preferable when wastes with a high water content (water content of 70% or more) and wastes with a low water content (water content of 30% or less) are treated together (Japanese Patent Laid-Open No. 2006-2612).
However, in the low-temperature heat treatment furnace, there are still various problems in practical use. Especially, when the additional processed material is waste with a high water content (moisture of 70% or more), the water is high-temperature ash even when the water content is 70% or less. If there is a large amount of leaching when approaching the fireball, almost all of the moisture contained in the waste flows into the lower heat treatment space, causing fire extinguishing, and the moisture in the lower heat treatment chamber. Therefore, it was difficult to maintain the high-temperature ash and the fireball, which had practical problems and left the problem as a low-temperature heat treatment furnace.

特開平11−230528JP-A-11-230528 特開2005−29600JP 2005-29600 A 特開2006−150295JP 2006-150295 A 実開2006−2612Opening 2006-2612

この出願の考案は、追加処理物が水分の多い廃棄物(水分70%以上)である場合でも、廃棄物に含まれた水分は、下部燻蒸処理空間内の高温灰、火芯玉に影響を与えないようにドレーン室Dに流出できるような工夫を施し、燻蒸処理を一層確実に維持できるようにし、各種廃棄物を、ダイオキシンを発生しない低温度(例えば400℃未満の温度)で燻蒸処理し灰化するまで処理可能にすることである。   The idea of this application is that even if the additional processed material is waste with a lot of moisture (more than 70% moisture), the moisture contained in the waste affects the high-temperature ash and fireball in the lower fumigation treatment space. In order not to give it to the drain chamber D, the device is designed so that the fumigation process can be maintained more reliably, and various wastes are fumigated at a low temperature (eg, less than 400 ° C.) that does not generate dioxins. It is to be able to process until ashing.

以上から、本願考案は上記課題を解決するものとして、水分の多い廃棄物(水分70%以上)場合にあっても、廃棄物・その他の処理物の低温熱処理が可能であって、ダイオキシンの発生を抑えた(又は無害化した)廃棄物・その他の処理物の処理が可能である磁化給気式燻蒸処理装置を提供するものである。   From the above, the present invention is designed to solve the above-mentioned problems. Even in the case of waste with a lot of water (moisture of 70% or more), low-temperature heat treatment of waste and other processed materials is possible, and dioxins are generated. It is an object of the present invention to provide a magnetized supply type fumigation processing apparatus capable of processing waste and other processed products that are suppressed (or detoxified).

この考案は、第1には、処理筐体は、その頂部に備える処理物投入口及びこれを施蓋する開閉蓋と、その周壁内側に間隔を置いて循環路Sを形成して配設され、その内側を上下に連通し処理物蓄積空間を形成する矩形筒体と、さらに処理物蓄積空間下方で、処理筐体の一方の対抗する側面下部に各設置の傾斜案内板により傾斜案内板の内側に形成される燻蒸処理空間及び傾斜案内板と筐体内壁間に形成される三角形状の貯気室と、処理筐体1の他方の対抗する側面の各側面下部に備える灰取出し口及びこれを開閉する扉と、処理筐体の裏面に給気磁化手段及び流量調整弁を介し配設され、前記貯気室に連通する給気配管及び前記傾斜案内板より燻蒸処理空間へ向けて突設される給気パイプを含み、給気パイプが各傾斜案内板より燻蒸処理空間へ向けて相対抗するよう水平状に複数配設され、給気配管から貯気室及び給気パイプを通じて燻蒸処理箇所へ空気を磁化し供給する複数の磁化給気装置と、処理筐体の上部に連結管を介して接続され、燻蒸処理空間から発生の燻蒸煙の消煙及び脱臭処理をする水タンクを備え、処理筐体内壁に接合される傾斜案内板の周縁は処理物の水分を下方へ導く通口が形成され、ドレーン室を通じ処理筐体の底面から排水可能に構成されていることを特徴とする磁化給気式燻蒸処理装置を提供する。   In this device, firstly, the processing housing is disposed by forming a circulation path S with a space inside the peripheral wall and an opening / closing lid for covering the processing object at the top thereof. A rectangular cylinder that forms a processed material storage space that communicates with the inside of the processing chamber, and a lower portion of one side of the processing housing that faces the lower side of the processing housing. A fumigation treatment space formed on the inside, a triangular air storage chamber formed between the inclined guide plate and the inner wall of the housing, and an ash take-out port provided at each side lower portion of the opposite side surface of the treatment housing 1 and the same A door that opens and closes, and an air supply magnetizing means and a flow rate adjusting valve disposed on the back surface of the processing housing, and protrudes toward the fumigation processing space from the air supply pipe communicating with the air storage chamber and the inclined guide plate The air supply pipe is fumigated from each inclined guide plate. A plurality of horizontal air supply devices that are opposed to each other and magnetized to supply air from the supply pipe to the fumigation processing point through the storage chamber and the supply pipe, and an upper part of the processing housing It is connected via a connecting pipe and has a water tank that smokes and deodorizes the fumigation smoke generated from the fumigation treatment space. There is provided a magnetization supply type fumigation processing apparatus characterized in that a through hole is formed and drained from a bottom surface of a processing casing through a drain chamber.

この考案は、第2には、前記給気磁化手段が永久磁石であることを特徴とする磁化給気式燻蒸処理装置を提供する。   The present invention secondly provides a magnetization supply type fumigation processing apparatus, wherein the supply air magnetization means is a permanent magnet.

この考案は、第3には、前記水平対向的に複数配設される給気パイプは、給気パイプの各先端を傾斜壁面に略並行する面内に位置させる共に給気パイプ相互を千鳥状に多段に配置し、給気パイプの先端を下方側に向く下側傾斜給気口としたことを特徴とする磁化給気式燻蒸処理装置を提供する。   Thirdly, according to the present invention, the plurality of air supply pipes arranged horizontally opposed to each other are arranged such that the tips of the air supply pipes are positioned in a plane substantially parallel to the inclined wall surface, and the air supply pipes are staggered. A magnetized air supply type fumigation apparatus is provided, which is arranged in multiple stages and has a lower inclined air supply port with the front end of the air supply pipe facing downward.

この考案は、第4には、前記水タンクは水槽を天井から前後に仕切る1枚のゲートと、前方の空間を複数に仕切る複数のゲート及び後方の空間を複数に仕切る複数のゲートと、水タンクに給水する注水管、水タンクから排水するドレーン及び水タンクの水位を所定のレベルに維持する溢水管とを備え、燻蒸処理空間から排出の燻蒸煙を前方空間及びこれに続いて後方空間を上下ジグザグ状に屈曲流動できるように、前後に仕切る1枚のゲートの後流部に流路を形成したことを特徴とする磁化給気式燻蒸処理装置を提供する。   According to a fourth aspect of the present invention, the water tank includes a single gate that divides the water tank forward and backward from the ceiling, a plurality of gates that divide the front space into a plurality of spaces, a plurality of gates that divide the rear space into a plurality of spaces, A water injection pipe that supplies water to the tank, a drain that drains from the water tank, and an overflow pipe that maintains the water level of the water tank at a predetermined level.The fumigation smoke discharged from the fumigation treatment space is passed through the front space and the rear space. Provided is a magnetization supply type fumigation processing device, characterized in that a flow path is formed in the wake portion of one gate divided forward and backward so as to bend and flow in a zigzag shape.

この考案は、第5には、処理筐体1の4側面に熱防護ネットを付設したことを特徴とする磁化給気式燻蒸処理装置を提供する。 Fifthly, the present invention provides a magnetization supply type fumigation processing apparatus characterized in that a thermal protection net is attached to four side surfaces of the processing casing 1.

この考案は、第6には、磁化給気式燻蒸処理装置の周辺に隣接して設置され、高所での投入物の投入作業に供する鋼製ステップ台と鋼製梯子を備え、ステップは上部に水平な金網の足場を有する脚付き台座に孔を有し、梯子は、その先端に形成した折り曲げたフック状の係止突起を有し、前記台座の孔と梯子のフック状突起を嵌合係止可能としたことを特徴とする磁化給気式燻蒸処理装置を提供する。   Sixth, this device is provided adjacent to the periphery of the magnetized air supply type fumigation processing equipment, and includes a steel step base and a steel ladder for the input work at a high place, and the step is an upper part. There is a hole in the legged pedestal with a horizontal wire mesh scaffolding, and the ladder has a bent hook-shaped locking projection formed at the tip, and the hole in the pedestal and the hook-shaped projection on the ladder are fitted A magnetized air supply type fumigation apparatus characterized by being able to be locked is provided.

本考案は、永久磁石、好ましくは4000乃至4500ガウスの永久磁石を用いた磁界を通して処理室への給気を実行し、燻蒸処理により炭化ないし灰化処理するもので、300〜400℃以下、好ましくは370前後の低温処理でありながら、ダイオキシンなどの有害物質の排出を1/3以下に抑えることができ、先行の燃焼処理とは異なる薫蒸処理の採用により有機物処理可能とした低公害処理装置であって、従来の焼却炉のようなロストル、着火バーナー、二次燃焼機を不要として構造の簡素化を図ることができる磁化給気式燻蒸処理装置を提供することができる。   The present invention performs supply of air to a processing chamber through a magnetic field using a permanent magnet, preferably 4000 to 4500 gauss permanent magnet, and carbonizes or incinerates by fumigation, and is preferably 300 to 400 ° C. or less. Is a low-temperature treatment around 370, but can reduce the discharge of harmful substances such as dioxins to 1/3 or less, and can be treated with organic substances by adopting fumigation treatment different from the previous combustion treatment. Thus, it is possible to provide a magnetization supply type fumigation processing apparatus that can simplify the structure without using a rooster, an ignition burner, and a secondary combustor as in a conventional incinerator.

この考案の装置によれば、紙くず(紙おむつ、紙パック、新聞紙、雑誌など)、生ゴミ(家庭生ゴミ、飲食品店廃棄飲食品)、木材、ビニール類、ナイロン、ウレタン、布、タイヤなど、金属・ガラス・鉱物以外の処理物を、励起空気の制限通気によって、焼却炉の場合の高温焼却温度以下とする低温域で、低温薫蒸処理させて灰にすることができながら、ダイオキシンの発生を極めて少量(基準内)に抑えた中で、各種廃棄物を含む処理物をより確実に、かつ効率よく処理できる。   According to the device of the present invention, waste paper (paper diapers, paper packs, newspapers, magazines, etc.), garbage (household garbage, food and beverages from food and beverage stores), wood, vinyl, nylon, urethane, cloth, tires, etc. Dioxins are generated while processing materials other than metal, glass, and mineral can be converted to ash by low-temperature fumigation at a low temperature range below the high-temperature incineration temperature of an incinerator by restricting ventilation of excited air. Can be treated more reliably and efficiently, while keeping the amount of waste in a very small amount (within the standard).

また本願考案の磁化給気式燻蒸処理によれば、各種廃棄物を、低温薫蒸処理によって灰にまで処理することができるので、最終的に投入された廃棄物の1/300 の容量となり、きわめて少量の残渣として残るだけであるので、以後の廃棄物等の処分作業を著しく軽減することができる。   In addition, according to the magnetized air supply type fumigation process of the present invention, various wastes can be processed to ash by low-temperature fumigation process. Since it remains only as a very small amount of residue, it is possible to remarkably reduce subsequent disposal work of wastes and the like.

なお、本願考案の磁化給気式燻蒸処理装置において、処理室への給気に際して、容量の大きな貯気室を介し、傾斜案内板の斜面に、面内に上下ジグザグ状に多段に配設した複数の給気パイプを通じて給気するので、励起空気は処理室内全体にほぼ均一に送り込まれ、斑のない安定した燻蒸処理が発現できる。ここで、給気パイプ群の各パイプは、それらの先端が傾斜案内板の傾斜面に略平行な面に位置し、給気パイプ自体は水平に配設され、また個々の給気パイプ先端は切口を図面下側が下向き斜めにして切断され,下側傾斜給気口を有している。これは、投入された廃棄物が給気パイプの給気口を直接塞ぐことがないように給気口の上部で遮蔽部を形成するものであり、また廃棄物の重量を分散的に支持するものでもあり、所期の燻蒸処理を一層円滑に実現するための工夫である。このように、傾斜案内板、傾斜案内板に上下ジグザグ状多段傾斜面内配設の給気パイプ群、各給気パイプ先端斜下面切斜切口により、給気配管からの励起空気の給気は妨げられることなく、安定した給気を可能とし、燻蒸処理の円滑な実現が可能となる。   In addition, in the magnetization supply type fumigation processing apparatus of the present invention, when supplying air to the processing chamber, it is arranged in multiple stages in a vertical zigzag manner in the plane on the inclined surface of the inclined guide plate through a large-capacity storage chamber. Since air is supplied through a plurality of air supply pipes, the excited air is sent almost uniformly into the entire processing chamber, and stable fumigation processing without spots can be realized. Here, each pipe of the air supply pipe group has its tip positioned on a plane substantially parallel to the inclined surface of the inclined guide plate, the air supply pipe itself is disposed horizontally, and each air supply pipe tip is The cut is cut with the lower side of the drawing inclined downward, and has a lower inclined air supply port. This is to form a shielding part at the upper part of the air supply port so that the input waste does not directly block the air supply port of the air supply pipe, and supports the weight of the waste in a distributed manner. It is also a device for realizing the intended fumigation process more smoothly. In this way, the supply of excitation air from the supply air pipe is made possible by the inclined guide plate, the inclined guide plate, the air supply pipe group arranged in the upper and lower zigzag multi-step inclined surface, and the inclined cut surface of the front end of each air supply pipe. A stable air supply is possible without being obstructed, and a smooth fumigation process can be realized.

この考案において、処理筐体内面に固接して貯気室を形成する傾斜案内板は、その接続端縁に、貯気室と通じる通口が形成されている。これにより、再度の処理物投入の際、最初に正常に燻蒸処理されている処理物の上部の処理待ち処理物に、処理物蓄積空間内で追加投入される処理物が水分の多い処理物であった場合、その処理物は燻蒸処理室内の温度で徐々に乾燥されつつ火心玉(コア)へと降下接近しつつ徐々に燻蒸されるものではあるが、処理物から水分が蒸発乾燥によってもなお蒸発しきれず滲出し流下したとしても、その水分は燻蒸処理室の傾斜案内板周縁の通口を通じて貯気室、さらにドレーン室へと流下可能となっている。
したがって、水分を多量に含んだ処理物が投入のときには、処理物からの水分は、薫蒸処理装置内の内壁、傾斜案内面を伝って流下し、滴となって、前記傾斜案内板3端縁の通口を通じて貯気室へと流入し、また、前記水分は、傾斜案内板に対し接続端縁に通口を有して固接された灰床板のその通口を通じても、この灰床板より二重底として形成されたドレーン室へと流出する。上述のように、燻蒸処理空間を避けるようにして徐々に流下させることができ、したがって、高温灰や、火芯玉(コア)への影響を最小限に抑えることができ、燻蒸処理のへの悪影響を回避して、燻蒸処理の正常な処理を維持することができる。
なお、このドレーン室の底には排水パイプが接続され、この排水パイプを通じてドレーン室に集積されたドレーンを排出することができ、或はさらにドレーンタンク(図示省略)に貯留することもできる。
In the present invention, the inclined guide plate that forms a gas storage chamber in solid contact with the inner surface of the processing casing has a communication port that communicates with the gas storage chamber at the connecting edge. As a result, when the processed material is re-introduced, the processed material additionally added in the processed material accumulation space to the processing-waiting processed material at the top of the processed material that has been normally fumigated first is a processed material with a lot of moisture. In such a case, the processed product is gradually dried at the temperature in the fumigation chamber and gradually fumigated while descending and approaching the core ball (core). Even if it cannot evaporate and exudes and flows down, the moisture can flow down to the air storage chamber and further to the drain chamber through the opening at the periphery of the inclined guide plate of the fumigation processing chamber.
Therefore, when a processed material containing a large amount of water is charged, the water from the processed material flows down along the inner wall and the inclined guide surface in the fumigation processing apparatus, forming droplets, and the end of the inclined guide plate 3 The ash floor plate also flows into the air storage chamber through the edge through-hole, and the moisture also flows through the through-hole of the ash floor plate that is fixedly connected to the inclined guide plate with a through-hole at the connection edge. It flows out into a drain chamber formed as a double bottom. As mentioned above, it can be made to gradually flow down to avoid the fumigation treatment space, and thus the influence on the high-temperature ash and fireball (core) can be minimized, and the fumigation treatment It is possible to avoid the adverse effects and maintain the normal processing of the fumigation process.
A drain pipe is connected to the bottom of the drain chamber, and the drain accumulated in the drain chamber can be discharged through the drain pipe, or can be stored in a drain tank (not shown).

上記において、追加投入された水分の多い処理物の水分は、先に投入されている積載された高温の処理物内に徐々に浸透吸収されていき、前記傾斜案内板端縁の通口を通じて貯気室へと流入されるので、燻蒸処理されている箇所における火芯玉(コア)へと浸透していく水分量は燻蒸処理に影響を与えることの無いほどに減少されたものとなる。
したがって、処理しようとする廃棄物等の処理物に含まれる水分が従来より多い場合であっても、廃棄物に含まれる水分は、火芯玉(コア)の存在する燻蒸処理箇所の系外に確実に排出することができ、この場合処理時間は通常より時間は掛かるが薫蒸処理は可能である。処理しようとする処理物の含水割合が、特に水分の多い廃棄物(水分70%以上)の場合は、水分の少ない廃棄物(水分30%以下)の上に追加投入することにより処理することが好ましい。
ただし、最初は、乾燥有機物の燻蒸処理によって高温灰(例えば300℃以上の灰)を早期に溜めて高温灰を創生しておくことが必要であり、高温灰を創生してから、水分のない処理物、水分の少ない処理物、水分を含んだ廃棄物と、水分の少ない廃棄物から順に投入し蓄積収容した後、燻蒸処理することが好ましい。この方が、円滑な処理ができることは勿論である。
なお、本考案装置において処理しようとする処理物に、特に制限はなく、家庭廃棄物及び産業廃棄物の何れでも処理できる。
In the above, the moisture of the additional processed material with a high amount of water is gradually permeated and absorbed into the previously loaded high-temperature processed material and stored through the opening at the edge of the inclined guide plate. Since it flows into the air chamber, the amount of water penetrating into the fireball (core) in the fumigated portion has been reduced to such an extent that it does not affect the fumigation treatment.
Therefore, even if the amount of moisture contained in the treated material such as the waste to be treated is higher than in the past, the moisture contained in the waste is outside the fumigation treatment location where the fireball (core) exists. In this case, the processing time is longer than usual, but fumigation is possible. If the water content of the processed material to be treated is a waste with a high moisture content (moisture of 70% or more), it can be treated by additionally charging it on a waste with a low moisture content (moisture of 30% or less). preferable.
However, at first, it is necessary to create high-temperature ash by quickly storing high-temperature ash (for example, ash of 300 ° C. or higher) by fumigation of dry organic matter. It is preferable to perform the fumigation treatment after sequentially putting in and storing the processed product having no moisture, the processed product having a low water content, the waste material containing the water content, and the waste material having a low water content. Of course, smoother processing can be achieved.
In addition, there is no restriction | limiting in particular in the processed material processed in this invention apparatus, Any of household waste and industrial waste can be processed.

この考案の磁化給気式燻蒸処理装置Aは、給送空気を給気磁化手段によって励起し、給気中に含まれた酸素を活性化するので、廃棄物等の処理物を低温(400℃未満)でも、燻蒸により効率よく熱処理させることができ、この温度でも薫蒸処理の場合にはダイオキシン発生を抑制することができた。
磁化給気式燻蒸処理の原理について概説すれば、4500ガウスの永久磁石を使用した磁力が炉内にプラズマ状態を作り出すと同時に、反応性の高い酸素を作り出すことにより酸化還元力との相乗効果で有機物を燻蒸処理するもので、有機物はこの燻蒸処理で磁気を帯びた真っ白な灰を作り出す。
The magnetization supply type fumigation processing apparatus A of this device excites the supply air by the supply air magnetization means and activates the oxygen contained in the supply air. However, even at this temperature, dioxin generation could be suppressed in the case of fumigation.
The outline of the principle of fumigation with magnetized air supply can be summarized as follows: the magnetic force using a permanent magnet of 4500 gauss creates a plasma state in the furnace, and at the same time, synergistic effects with the redox power by creating highly reactive oxygen. Organic matter is fumigated, and organic matter produces white ash with magnetism by this fumigation treatment.

給送空気を励起し、給気中に含まれる酸素を活性化し、燻蒸処理室へその活性化された酸素を含む空気を給気する磁化給気装置6は、給気配管、この給気配管に配備される給気磁化手段及び流量調整弁、貯気室及び給気パイプを含み、処理筐体1の裏面に左右前後に複数各独立して配設されている。   A magnetized air supply device 6 that excites the supply air, activates oxygen contained in the supply air, and supplies the activated oxygen to the fumigation processing chamber includes an air supply pipe, and this air supply pipe. A plurality of air supply magnetizing means, a flow rate adjusting valve, an air storage chamber, and an air supply pipe are provided on the rear surface of the processing housing 1 and arranged independently on the right and left sides.

そこで給送空気の給気は、処理筐体1の裏面に配設の磁化給気装置6により、活性化された酸素を含む空気がそれら各流量調整弁63により調節され、貯気室S2を介し、給気パイプ64を通じて、薫蒸処理空間へと給気可能となっている。燻蒸処理の際、給気量は、燻蒸処理に伴って上昇気流となって発生する燻蒸煙が、薫蒸処理室内で矩形筒体の内側外側空間を通じて循環流が形成され、さらに後述の水タンク8を経て排気されるなか、これを補いながら、薫蒸処理に必要な最小限の空気量として求められる。
上記の流量調整弁は、好ましくはゲート弁が適用され、ゲート弁により給気量の調整は一層容易になる。なお、ここで、流量調整弁63はゲート弁63aに限定されることはない。通常、適正な燻蒸処理中の火心玉(コア)は略中央位置であることが望ましく、したがって、燻蒸処理における高温火灰の位置が偏ったときには、前記各流量調整弁の絞り度を手動によって調整することによって、適正な中央位置に修正移動させることができる。この場合に熟練を要する。また、処理室に積層された廃棄物の燻蒸状態によって、偏った位置での燻蒸状態であったときには、いつでも中央で燻蒸処理が実行されるように、自動的に燻蒸処理位置を修正制御することも可能となる。
なお、この場合、燻蒸処理が正常な中央位置で処理実行されているか、偏った位置で処理実行されているかは、燻蒸処理装置の外壁で温度検知可能とし、4箇所の外壁面の各温度を比較により判別することができることは勿論である。
Therefore, the supply air is supplied by the magnetizing air supply device 6 disposed on the back surface of the processing housing 1 so that the air containing the activated oxygen is adjusted by the flow rate adjusting valves 63 and the storage chamber S2 is supplied. Therefore, air can be supplied to the fumigation processing space through the air supply pipe 64. During the fumigation process, the amount of air supplied is the fumigation smoke generated as an updraft with the fumigation process, and a circulation flow is formed through the inner and outer space of the rectangular cylinder in the fumigation process chamber. While being exhausted through No. 8, it is calculated as the minimum amount of air necessary for fumigation while supplementing this.
A gate valve is preferably used as the flow rate adjusting valve, and the adjustment of the air supply amount is further facilitated by the gate valve. Here, the flow rate adjusting valve 63 is not limited to the gate valve 63a. Normally, it is desirable that the fireball (core) during proper fumigation processing is at a substantially central position. Therefore, when the position of the high-temperature fire ash in the fumigation processing is biased, the throttling degree of each flow rate adjusting valve is manually adjusted. By adjusting, it can be corrected and moved to an appropriate center position. In this case, skill is required. In addition, when the fumigation state of the waste stacked in the processing chamber is fumigated at an uneven position, the fumigation processing position is automatically corrected and controlled so that the fumigation process is executed at the center anytime. Is also possible.
In this case, whether the fumigation process is being performed at a normal central position or at a biased position can be detected at the outer wall of the fumigation apparatus, and the temperatures of the four outer wall surfaces are determined. Of course, it can be determined by comparison.

この考案の磁化給気式燻蒸処理装置Aによれば、処理対象処理物に対応して、励起した酸素の給気量を調整し、また励起した酸素の給気量により薫蒸処理温度を制御することが可能であるので、給気量の関係を正確に保つことにより、適正な燻蒸処理の火心玉(コア)の位置において、適正な薫蒸処理温度範囲内での制御を達成することができる。実際、薫蒸処理温度は、300〜400℃以下、好ましくは370℃前後に加熱されるように、励起した酸素の給気量を調節し、これによって有機物を気化させ、炭その他を灰化することができた。
燻蒸処理空間における燻蒸処理温度の管理は、燻蒸処理空間内に設置される温度感知器と装置に設置された温度計により制御管理される。
According to the magnetization supply type fumigation processing apparatus A of the present invention, the supply amount of excited oxygen is adjusted corresponding to the processing object, and the fumigation processing temperature is controlled by the supply amount of excited oxygen. It is possible to achieve control within the proper fumigation temperature range at the position of the proper fumigation core (core) by keeping the relationship of the air supply amount accurate. Can do. In fact, the fumigation temperature is adjusted to 300-400 ° C. or less, preferably around 370 ° C., and the amount of excited oxygen supplied is adjusted, thereby vaporizing organic matter and ashing charcoal and the like. I was able to.
Management of the fumigation temperature in the fumigation space is controlled and managed by a temperature sensor installed in the fumigation space and a thermometer installed in the device.

処理筐体1内へ投入形態については、投入口11から処理物を投入する場合、隙間ができないようにできるだけ詰めて投入する。また、その際、偏った処理物の投入を行なうと、処理に時間が掛かる場合があるため、バランスのよい投入が好ましい。   As for the input form into the processing housing 1, when the processing object is input from the input port 11, it is input as close as possible so that there is no gap. At that time, if an unevenly processed material is input, it may take a long time for the processing, and therefore, a balanced input is preferable.

この出願の考案によれば、鉄・石・ガラス類を除く有機物の処理が可能である。
例えば、一般ゴミとして、含水量の少ないプラスチック類(プラスチック・発泡スチロール・塩化ビニール・ペットボトル・ポリエステル・ビニールなど)、ゴム製品(タイヤ、合成ゴム)・木材・紙(段ボールなども含む)・繊維類(布団なども含む)などである。
また、生ゴミ・汚泥(糞尿・食品汚泥、など)の場合、水分が底辺部に落ちない程度の含水量であれば時間は掛かかるが処理はできる。ただし、含水量が60%を越すと処理が難しくなる。この場合、含水量が60%を越す有機物の処理に当たっては、予め脱水の前処理により、含水量を30〜50%までに落とすことが好ましく、乾燥機、圧縮(圧搾)機、或は遠心分離機により脱水処理をする。
生ゴミの場合、圧縮できるので、量として型式により異なるが、圧縮した生ゴミの投入により一層大量の生ゴミが処理可能となる。その場合、段ボールやビニールなどを一緒に混入して処理しても差し支えない。生ゴミの圧縮処理に際して、ポリ袋などに生ゴミを入れてきっちりと結んで圧縮機に掛けると処理しづらいので、ポリ袋から出すか、ポリ袋に穴を開けることで対処が可能である。
According to the device of this application, it is possible to treat organic matter excluding iron, stone and glass.
For example, as general garbage, plastics with low water content (plastic, foamed polystyrene, vinyl chloride, PET bottles, polyester, vinyl, etc.), rubber products (tires, synthetic rubber), wood, paper (including cardboard, etc.), fibers (Including futons).
In the case of raw garbage / sludge (such as manure, food sludge, etc.), if the water content is such that moisture does not fall to the bottom, it takes time, but can be processed. However, if the water content exceeds 60%, the treatment becomes difficult. In this case, it is preferable to reduce the water content to 30 to 50% by pretreatment of dehydration in advance for the treatment of organic substances having a water content exceeding 60%, such as a dryer, a compression (squeezing) machine, or a centrifugal separator. Dehydrated by machine.
In the case of raw garbage, since it can be compressed, the amount varies depending on the model, but a larger amount of raw garbage can be processed by introducing compressed raw garbage. In that case, cardboard or vinyl may be mixed and processed together. When the garbage is compressed, it is difficult to put the garbage in a plastic bag or the like and tie it tightly and hang it on the compressor, so it can be dealt with by removing it from the plastic bag or making a hole in the plastic bag.

この考案において、図1に示す処理筐体1の上部に搭載される水タンク8は、内部に蓄水したときその内部を前後の室に区切る左右長手方向のゲート81aと、前方室と後方室において各室を複数の区分室に隙間を通じて連通するように仕切るゲート81b、81cとを備える。水タンク8において、連結管7を通じて流入する燻蒸煙は、図4に詳細に示すように、水タンク8の前方室を上下ジグザグ状に、次いで後方室を上下ジグザグ状に流動し、燻蒸煙に含まれるダストが捕獲される。この過程で、燻蒸煙自体が蓄水に接触して吸着されながら、上部の排気筒85から排出される。   In this device, the water tank 8 mounted on the upper portion of the processing case 1 shown in FIG. 1 includes a gate 81a in the longitudinal direction that divides the interior into front and rear chambers when the water is stored therein, a front chamber, and a rear chamber. The gates 81b and 81c partition each chamber so as to communicate with a plurality of compartments through gaps. In the water tank 8, as shown in detail in FIG. 4, the fumigation smoke flowing in through the connecting pipe 7 flows in the upper and lower zigzags in the front chamber of the water tank 8 and then in the upper and lower zigzags in the rear chamber. Contained dust is captured. In this process, the fumigation smoke itself is discharged from the upper exhaust pipe 85 while being adsorbed in contact with the stored water.

水タンク8は燻蒸煙の上下ジグザグ状の流動が許容できるように水タンク8内部に蓄水するため、水タンク8の上部に給水のための給水口82、水タンク8の底部に排水のための排水口84、水タンク8内の水位Lを所定のレベルに維持させ、所定レベル以上の水をオーバーフローさせる溢水口83を備えている。したがって、前記した所定の煙道Pを形成するための給水、水位Lの調整は、各接続口に接続のライン(図示省略)に備える弁(図示省略)によって実行される。また、燻蒸煙を水タンク8通過させ、消煙・消臭処理後に排出する排気筒85は、水タンク8の上面以外に側面にも予備的に備えることができる。この使用法は、本考案の磁化給気式燻蒸処理装置Aを設置する際に、設置場所により排気方向に配慮する必要が生じたときに、不必要な排気筒85の口を閉鎖して使用する。   The water tank 8 stores water inside the water tank 8 so as to allow the upward and downward zigzag flow of fumigation smoke, so that a water supply port 82 for water supply is provided at the top of the water tank 8 and water is discharged at the bottom of the water tank 8. The water outlet 84 and the water level L in the water tank 8 are maintained at a predetermined level, and an overflow port 83 is provided for overflowing water above a predetermined level. Therefore, the water supply for forming the predetermined flue P and the adjustment of the water level L are executed by a valve (not shown) provided in a line (not shown) connected to each connection port. Further, the exhaust pipe 85 that allows the fumigation smoke to pass through the water tank 8 and discharges it after the smoke and odor eliminating treatment can be provided on the side surface in addition to the upper surface of the water tank 8. This method is used when the magnetized air supply type fumigation processing apparatus A of the present invention is installed, and it is necessary to close the unnecessary exhaust pipe 85 when it is necessary to consider the direction of the exhaust depending on the installation location. To do.

灰取出しは、処理筐体1の側壁に設けた灰出し口13を閉鎖している扉14を開放し、灰床板4上に蓄積された灰を、灰掻い出し具を用いて取り出す。灰出し口は処理筐体1の対抗する側壁の2箇所に設けてあるので、両側から作業する。磁化給気式燻蒸処理装置Aが大型になった場合に特に有利である。   In the ash removal, the door 14 that closes the ash outlet 13 provided on the side wall of the processing housing 1 is opened, and the ash accumulated on the ash floor plate 4 is taken out using an ash scraper. Since the ash outlets are provided at two locations on the opposite side wall of the processing housing 1, work is performed from both sides. This is particularly advantageous when the magnetization supply type fumigation processing apparatus A becomes large.

給気磁化手段62は、給気配管61に永久磁石を付設し、給気配管61内部の通過空気を磁化励起する。ここで使用の永久磁石は好ましくは4000乃至4500ガウスの永久磁石であり、この給気磁化手段62は、永久磁石に限定されず、電磁石を適用しても差し支えない。なお、この給気磁化手段62として、永久磁石の他に遠赤外線発生鉱物(例えば麦飯石、電気石など)を組み合わせて適用することにより、磁気処理と遠赤処理の両処理を行い、空気の活性化(励起、イオン化)を一層促進させることもできる。   The air supply magnetizing unit 62 attaches a permanent magnet to the air supply pipe 61 to excite magnetization of the air passing through the air supply pipe 61. The permanent magnet used here is preferably a permanent magnet of 4000 to 4500 gauss, and the air supply and magnetization means 62 is not limited to a permanent magnet, and an electromagnet may be applied. In addition, by applying a combination of a far-infrared ray generating mineral (for example, barley stone, tourmaline, etc.) in addition to a permanent magnet as the air supply magnetization means 62, both magnetic treatment and far-red treatment are performed, Activation (excitation, ionization) can be further promoted.

この考案では、図6(a)に示すように、設置された磁化給気式燻蒸処理装置Aにおいて、投入口11が高い場合には、その周囲に、高い位置の投入口11に運搬するための補助装置として鋼製のステップ台9を配置することができる。鋼製ステップ台9には鋼製梯子10がセットとして備える。
鋼製梯子10を鋼製ステップ台9に寄せ掛けるとき、単に、鋼製梯子10の梁部分上端を鋼製ステップ台9に寄せ掛けるだけでは、何らかの大きな負荷が梯子10に加えられたときに、鋼製梯子10が鋼製ステップ台9から外れて、危険である。そこで、図6(b)に示すように、鋼製ステップ台9のL字鋼枠において、梯子10を寄せ掛ける所定の位置に、梯子10の幅寸法に合わせた一対の係止孔9bが穿設される。一方、梯子10の先端には、ステップ台9の前記係止孔9bに嵌合係止するフック10aが形成されている。
したがって、使用時において、鋼製梯子10のフック10aを鋼製ステップ台9の係止孔9bに嵌合すると、鋼製梯子10はその自重により鋼製梯子10のフック10aは、鋼製ステップ台9の係止孔9bに嵌合し他まま浮き上がることもなく、確りと係合状態を保つことができるので、梯子10がステップ台9から外れ落ちる虞もなく、処理物の運搬作業を安全に行なうことができる。
In this device, as shown in FIG. 6 (a), when the inlet 11 is high in the installed magnetized supply type fumigation processing apparatus A, it is transported around the inlet 11 to a higher position. A steel step base 9 can be arranged as an auxiliary device. A steel ladder 10 is provided as a set on the steel step base 9.
When the steel ladder 10 is brought close to the steel step base 9, when a large load is applied to the ladder 10 simply by bringing the upper end of the beam portion of the steel ladder 10 close to the steel step base 9, The steel ladder 10 is detached from the steel step table 9, which is dangerous. Therefore, as shown in FIG. 6B, in the L-shaped steel frame of the steel step base 9, a pair of locking holes 9b matching the width of the ladder 10 are formed at predetermined positions where the ladder 10 is brought close to. Established. On the other hand, a hook 10 a that fits and locks into the locking hole 9 b of the step table 9 is formed at the tip of the ladder 10.
Therefore, in use, when the hook 10a of the steel ladder 10 is fitted into the locking hole 9b of the steel step base 9, the steel ladder 10 is caused to move by the weight of the steel ladder 10 so that the hook 10a of the steel ladder 10 becomes the steel step base. 9 can be securely engaged with the locking hole 9b without being lifted, and the ladder 10 can be safely removed from the step base 9, and the work can be transported safely. Can be done.

この考案の磁化給気式燻蒸処理装置Aにおいて、2重壁をなす処理筐体1の鋼板壁板の外側は、9mmの比較的厚い鋼板の使用により急激な熱伝達を抑制し、外表面の温度上昇を緩和して過熱防止対策を施しているが、燻蒸処理中に、異常薫蒸で外表面が基準以上に高温となる場合を考慮し、念には念を入れ、作業者等のまさかの火傷の危険を回避するため、図6に示すように、さらに処理筐体1の周囲に熱防護ネットを取り付け、二重に安全を図ることもできる。
以下、図面を用いて、さらに詳細に説明をする。
In the magnetization supply type fumigation processing apparatus A of the present invention, the outside of the steel plate wall plate of the processing casing 1 forming a double wall suppresses rapid heat transfer by using a relatively thick steel plate of 9 mm, Although measures to prevent overheating have been taken by mitigating the temperature rise, it is necessary to consider the case where the outside surface becomes hotter than the standard due to abnormal fumigation during the fumigation process. In order to avoid the risk of burns, as shown in FIG. 6, a thermal protection net can be further attached around the processing housing 1 to double safety.
Hereinafter, it explains in detail using a drawing.

図1は、磁化給気式燻蒸処理装置Aの全体を概略的に示す。
図1において、磁化給気式燻蒸処理装置Aは、燻蒸処理部として、燻蒸処理するための処理筐体1は、その頂部に廃棄物投入口11を備え開閉蓋12により施蓋され、処理筐体1の内側に間隔を置いて矩形筒体2が配設され、上下に連通する矩形筒体2の内側が処理物蓄積空間となり、また、処理筐体1と矩形筒体2の間には気流循環路S4が形成される。処理筐体1は、処理物蓄積空間S1下方における対抗する一方の各側面下部に傾斜案内板3、3が傾斜固接される。各傾斜案内板3の固接により傾斜案内板3、3間の内側空間は燻蒸処理空間S3として形成され、また、傾斜案内板3と処理筐体1の間には隅に三角形状の貯気室S2が形成される。また、処理筐体1の対抗する他方の各側面下部に灰取出し口13を備え、この灰取出し口13には開閉する扉14を備える。
ここで、処理筐体1の内壁に傾斜し、側壁、底壁に固接される傾斜案内板3は、全周縁がタック溶接で固接され、その周縁には処理物の水分を下方の貯気室S2へと導く通口3aが形成されている。
ここで、傾斜案内板3に形成された通口3aから貯気室S2に導かれ、貯気室S2に導かれた水分は、さらにドレーン室Dへと入り、ドレーン室Dを形成する処理筐体1の底面から排水パイプ5aを通じて排水される。
また、磁化給気式燻蒸処理装置Aは、燻蒸処理部への磁化給気を創生するための磁化給気部として、処理筐体1の裏面に、給気磁化手段62及び流量調整弁63を介在して配設される給気配管61を備え、給気配管61は給気磁化手段62及び流量調整弁63を介して前記貯気室S2に連通し、また、前記傾斜案内板3には燻蒸処理空間S3へ向けて突設する複数の給気パイプ64を備え、その際、給気パイプ64は各傾斜案内板3より燻蒸処理室S3へ向けて相対抗するよう水平状に複数配設され、これら給気配管61、給気磁化手段62、流量調整弁63、貯気室S2及び給気パイプ64は、給気配管61から貯気室S2及び給気パイプ64を通じて燻蒸処理空間S3へ空気を磁化し供給する磁化給気装置6を構成し、この磁化給気装置6が複数設置される。
さらに、磁化給気式燻蒸処理装置Aは、燻蒸処理空間S3で発生の燻蒸煙を消煙・脱臭処理する、燻蒸煙消煙・脱臭処理部として、処理筐体1の上部に連結管7を介して接続され、燻蒸処理空間S3から発生された燻蒸煙の消煙及び脱臭処理をする水タンク8を備える。
FIG. 1 schematically shows the entire magnetization supply type fumigation processing apparatus A.
In FIG. 1, the magnetization supply type fumigation processing apparatus A is a fumigation processing unit, and a processing case 1 for fumigation processing is provided with a waste input port 11 at the top thereof and covered with an opening / closing lid 12, and the processing case 1 A rectangular cylinder 2 is disposed inside the body 1 with a space therebetween, and the inside of the rectangular cylinder 2 communicating with the top and bottom serves as a processing object accumulation space. An air flow circulation path S4 is formed. In the processing case 1, the inclined guide plates 3 and 3 are inclined and fixedly connected to lower portions of one side facing each other below the processed product storage space S1. The inner space between the inclined guide plates 3 and 3 is formed as a fumigation processing space S3 by the tight contact of each inclined guide plate 3, and a triangular air reservoir is formed at the corner between the inclined guide plate 3 and the processing housing 1. Chamber S2 is formed. Further, an ash extraction port 13 is provided at the lower part of each other side surface facing the processing casing 1, and the ash extraction port 13 is provided with a door 14 that opens and closes.
Here, the inclined guide plate 3 which is inclined to the inner wall of the processing housing 1 and fixedly contacted to the side wall and the bottom wall is fixedly attached to the entire periphery by tack welding, and moisture of the processed material is stored in the periphery on the lower side. A vent 3a leading to the air chamber S2 is formed.
Here, the water that is guided to the gas storage chamber S2 from the opening 3a formed in the inclined guide plate 3 and enters the gas storage chamber S2 further enters the drain chamber D to form the drain chamber D. The water is drained from the bottom surface of the body 1 through the drain pipe 5a.
In addition, the magnetization supply type fumigation processing apparatus A serves as a magnetization supply unit for creating magnetization supply to the fumigation processing unit. The air supply pipe 61 communicates with the air storage chamber S2 through the air supply magnetizing means 62 and the flow rate adjusting valve 63, and is connected to the inclined guide plate 3. Has a plurality of air supply pipes 64 projecting toward the fumigation processing space S3. At this time, a plurality of air supply pipes 64 are horizontally arranged so as to oppose each of the inclined guide plates 3 toward the fumigation processing chamber S3. The air supply pipe 61, the air supply magnetizing means 62, the flow rate adjusting valve 63, the air storage chamber S2, and the air supply pipe 64 are provided in the fumigation processing space S3 from the air supply pipe 61 through the air storage chamber S2 and the air supply pipe 64. The magnetization air supply device 6 is configured to magnetize and supply air to the There are multiple installation.
Further, the magnetized air supply type fumigation processing apparatus A is a fumigation smoke deodorizing / deodorizing treatment unit for removing the fumigation smoke generated in the fumigation processing space S3. And a water tank 8 for performing deodorizing and deodorizing treatment of the fumigation smoke generated from the fumigation treatment space S3.

処理筐体1の内側に間隔を置いて、その内側を上下に連通する矩形筒体2が配設されており、処理筐体1の頂部に備える廃棄物投入口11を施蓋する開閉蓋12を開放し、廃棄物を投入すると、処理物蓄積空間を形成する矩形筒体2内を含めて、処理筐体1内に廃棄物Bが蓄積される。
実際、本体部分は処理筐体1と矩形筒体2からなる二重構造になり、内壁の矩形筒体2は6mmの鉄板で構成され、これに対し外壁の処理筐体1は9mmと厚めに構成されおり、両者の取り付け間隔は50mmの空間が空けられる。
なお、前記した外壁の処理筐体1の鉄板の9mmの厚みは、熱伝達距離を長くしてできるだけ表面温度が高熱化することを防止するためであり、また磁気を遮断し、外部への磁気漏れを防止するためのものでもある。また、処理筐体内壁と矩形筒体2の間に形成された空隙は、燻蒸処理中に、中央の燻蒸処理熱源により自然対流が発生し、略中央から発生する燻蒸煙の上昇気流が、天上部分で中央上昇気流から四方に拡散し、周辺4箇所から前記空隙内を反転流下する一連の循環燻蒸煙の通路となり、この循環燻蒸煙は、この空隙を通り、燻蒸処理室S3内へ再度下方から送り込まれ、燻蒸処理の促進を補助する。
A rectangular cylinder 2 is provided inside the processing case 1 with a space therebetween, and the inside of the processing case 1 communicates up and down, and an open / close lid 12 that covers a waste input port 11 provided at the top of the processing case 1. When the waste is opened and the waste is introduced, the waste B is accumulated in the processing casing 1 including the inside of the rectangular cylinder 2 that forms the processed material accumulation space.
Actually, the main body has a double structure consisting of a processing casing 1 and a rectangular cylindrical body 2. The rectangular cylindrical body 2 on the inner wall is composed of a 6 mm iron plate, whereas the processing casing 1 on the outer wall is 9 mm thicker. The space between the two is 50 mm.
The thickness of 9 mm of the iron plate of the processing casing 1 of the outer wall described above is to prevent the surface temperature from becoming as high as possible by lengthening the heat transfer distance, and also to cut off the magnetism and prevent the magnetism to the outside. It is also for preventing leakage. In addition, the air gap formed between the inner wall of the processing casing and the rectangular cylinder 2 is caused by natural convection generated by the central fumigation heat source during the fumigation process. Part of this is a series of circulating fumigation smoke that diffuses in four directions from the central ascending airflow and reversely flows down in the gap from the four surroundings. This circulating fumigation smoke passes again through this gap and into the fumigation treatment chamber S3 again. To help promote fumigation.

また、処理筐体1には、処理筐体1の内側で対向する両隅部に三角形状の貯気室S2を形成するため傾斜案内板3が接合される。この場合、この処理筐体1の内側に接合される傾斜案内板3の4つ周縁には、通口3aが形成される。
また、対向する傾斜案内板3には、処理筐体1の底面から所定の小さな高さに位置して底面と並行で水平な灰床板4が溶接により接合され、処理筐体1の底板5とこの灰床板4との間にドレーン室Dが形成される。
上記において、傾斜案内板3は、例えば、処理筐体1の一側面と接する上方の水平をなす縁、処理筐体1の他の側面と傾斜して接する2つの傾斜縁及び処理筐体1の底面と接する下方の直線をなす縁の4つの縁が、それぞれ点在的接合するようにタック溶接され、点溶接の間には 通口3aが形成される。なお、傾斜案内板3の接合4周縁は、タック溶接に限定されるものではなく、接合4周縁それぞれ断続的な深さの浅い凹溝を形成し、凸部箇所において溶接することもできる。
In addition, an inclined guide plate 3 is joined to the processing casing 1 in order to form a triangular storage chamber S2 at both corners facing each other inside the processing casing 1. In this case, through-holes 3 a are formed at the four peripheral edges of the inclined guide plate 3 joined to the inside of the processing housing 1.
In addition, an ash floor plate 4 which is located at a predetermined small height from the bottom surface of the processing housing 1 and is parallel to the bottom surface is joined to the opposing inclined guide plates 3 by welding, and the bottom plate 5 of the processing housing 1 A drain chamber D is formed between the ash floor plate 4.
In the above description, the inclined guide plate 3 includes, for example, an upper horizontal edge in contact with one side surface of the processing housing 1, two inclined edges in contact with the other side surface of the processing housing 1, and the processing housing 1. Four edges, which form a straight line on the lower side in contact with the bottom surface, are tack welded so as to be interspersed with each other, and a through hole 3a is formed during spot welding. Note that the periphery of the joint 4 of the inclined guide plate 3 is not limited to tack welding, and each of the periphery of the joint 4 can be formed with a groove having a shallow depth and can be welded at the convex portion.

したがって、追加的に水分を含んだ廃棄物Bが投入口11から、燻蒸処理空間S3、処理物蓄積空間S1を形成する投入室に投入されたとき、処理物の水分を、火芯玉(コア)への流動を回避して、下方貯気室S2へ導くことができるようにされ、具体的には水分は廃棄物Bから処理室の内壁、傾斜案内面を伝って、前記傾斜案内板3端縁の通口3aを通じて貯気室S2へ、さらに、処理室の下部に二重底により形成されたドレーン室Dへともたらされる。さらに排水パイプ5aを通じて、排水可能とされる。
また、傾斜案内板3と灰床板4の溶接においても上述したと同様にタック溶接による構造が推奨され、上記同様、投入された廃棄物Bに含まれる水分は、前記の処理室の内壁、傾斜案内面を伝って、前記傾斜案内板3端縁の通口3aからに止まらず、この傾斜案内板3と灰床板の溶接部の通口3aを通じてもドレーン室Dへともたらされる。
Accordingly, when the waste B additionally containing moisture is introduced from the inlet 11 into the input chamber that forms the fumigation treatment space S3 and the treatment product storage space S1, the moisture of the treatment is removed from the fireball (core ), And can be guided to the lower storage chamber S2. Specifically, the moisture is transferred from the waste B through the inner wall of the processing chamber and the inclined guide surface to the inclined guide plate 3. It is brought to the gas storage chamber S2 through the edge opening 3a, and further to the drain chamber D formed by a double bottom at the lower part of the processing chamber. Further, the water can be drained through the drain pipe 5a.
Also, in the welding of the inclined guide plate 3 and the ash floor plate 4, a structure by tack welding is recommended in the same manner as described above, and the moisture contained in the waste B that has been introduced is inclined to the inner wall of the processing chamber as described above. The drainage chamber D is brought into the drain chamber D through the guide surface, not only through the through-hole 3a at the edge of the inclined guide plate 3, but also through the through-hole 3a of the welded portion between the inclined guide plate 3 and the ashtray plate.

図3に示すように、本考案は、燻蒸処理箇所S3への磁化給気を創生するための磁化給気装置6として、処理筐体1裏面の4箇所に、貯気室S2に連通する給気配管61が接続され、給気管61には給気磁化手段62が介在され、さらに途中に流量調整弁63が接続されている。この図では、各部品の配置をコンパクトにまとめるため、エルボ管を接続したU字管として、平行な給気配管61の部分に給気磁化手段62、流量調整弁63をそれぞれ配置するものとして示される。しかしこれに限定されるものではない。さらに、磁化給気装置6は、流量調整弁63に続いて連通する貯気室S2の内側に、図2に示すように、前記貯気室S2を形成する各傾斜案内板3の表面に、傾斜案内板3表面から燻蒸処理空間S3へ向けて相対抗するよう、水平状に設置される複数給気パイプ64を備えて構成される
ここで、磁化手段62は、永久磁石を使用する例として説明する。永久磁石は高磁性のもの(4000〜4500ガウス)使用が望ましい。
As shown in FIG. 3, the present invention communicates with the gas storage chamber S <b> 2 at four locations on the back surface of the processing housing 1 as a magnetization air supply device 6 for creating a magnetization air supply to the fumigation processing location S <b> 3. An air supply pipe 61 is connected, an air supply magnetizing means 62 is interposed in the air supply pipe 61, and a flow rate adjusting valve 63 is connected in the middle. In this figure, in order to make the arrangement of each component compact, it is shown that the air supply magnetizing means 62 and the flow rate adjusting valve 63 are respectively arranged in a portion of the parallel air supply pipe 61 as a U-shaped pipe connected with an elbow pipe. It is. However, the present invention is not limited to this. Further, the magnetizing air supply device 6 is provided on the surface of each inclined guide plate 3 forming the air storage chamber S2 inside the air storage chamber S2 communicating with the flow rate adjusting valve 63, as shown in FIG. A plurality of air supply pipes 64 are provided horizontally so as to oppose each other from the surface of the inclined guide plate 3 toward the fumigation processing space S3.
Here, the magnetizing means 62 will be described as an example using a permanent magnet. It is desirable to use a permanent magnet having a high magnetic property (4000 to 4500 gauss).

本考案では、永久磁石を用いた磁界を通して燻蒸処理空間S3への給気をし、燻蒸処理により炭化ないし灰化処理するもので、その際、300〜400℃以下、好ましくは370前後の低温処理になる用に制御される。ここでは、300〜400℃以下の低温でありながら、ダイオキシンなどの有害物質の排出を1/3以下に抑えることができた。本考案は、要するに、先行の燃焼処理とは異なる薫蒸処理によりは有機物処理可能とした低公害処理装置であって、従来の焼却炉のようなロストル、着火バーナー、二次燃焼機を不要とし、構造の簡素化を図ることのできる磁化給気式燻蒸処理装置であるということができる。
濃縮酸素と磁気による薫蒸で有機物を分解処理する上記の場合、燃焼によるダイオキシンは、検出基準を下回る測定結果を得ることができた。
In the present invention, air is supplied to the fumigation treatment space S3 through a magnetic field using a permanent magnet, and carbonization or ashing treatment is carried out by fumigation. At that time, a low temperature treatment of 300 to 400 ° C. or less, preferably around 370 is performed. Controlled to become. Here, the discharge of harmful substances such as dioxin could be suppressed to 1/3 or less, even at a low temperature of 300 to 400 ° C. or less. In short, the present invention is a low-pollution treatment device that can treat organic substances by fumigation treatment different from the previous combustion treatment, and eliminates the need for a rooster, ignition burner, and secondary combustor like a conventional incinerator. Therefore, it can be said that the structure is a magnetization supply type fumigation processing device that can be simplified.
In the above case where the organic matter is decomposed by fumigation with concentrated oxygen and magnetism, dioxins by combustion were able to obtain measurement results below the detection standard.

本考案に係る磁化給気式燻蒸処理装置Aの燻蒸処理は次の通りである。
稼働当初、装置底部の灰蓄積部S5に灰を蓄積しておく必要がある。
これは、本考案の磁化給気式燻蒸処理装置Aにより燻蒸処理された灰が、磁気を帯びたイオンパウダー灰として蓄積され、この炉の下部に蓄積されたイオンパウダー灰の磁気が給気された磁気を帯びた空気の磁気に反応させることにより、燻蒸処理を磁気的な相乗効果により炉内を安定させ処理能力を高めることができることによる。
そのため、下部に灰がない場合は、できるだけ乾いた処理物(ゴミなど)によって灰を蓄積する。先ず、処理筐体1上部の投入口11から、できるだけ乾いた処理物(ゴミなど)を所定量投入し、蓄積すべき必要量の灰を確保できる量を見込んで投入した後、蓋を閉鎖する。灰取出し口13を開き、灰取出し口13から火種を投入し、処理筐体内に蓄積された処理物(ゴミなど)を着火し、扉14を閉じて灰取出し口13を閉鎖する。
扉14の閉鎖により、本処理装置の裏面に配設された給気配管61及びこれに設置の磁気装置62、流量調整弁63、貯気室S2、給気パイプ64を含む磁化供気装置6を操作する。最初開放されていた流量調整弁63を徐々に絞りながら活性化された空気を取入れる。そこで、燻蒸処理室S3内に取り入れられた酸素に磁力線を作用させることで、装置内部に全方向性を持った磁界を発生させ、これにより20%の常磁性をもつ酸素と78%の反磁性をもつ窒素及び微量元素に分かれ、無酸素状態の炉内で磁気低温プラズマが発生される。装置内では、低温で濃縮され微小化された酸素と磁気による薫蒸処理が実行され、ダイオキシンの発生が極力抑制される。
(図5(a)参照)
The fumigation processing of the magnetization supply type fumigation processing apparatus A according to the present invention is as follows.
At the beginning of operation, it is necessary to store ash in the ash storage section S5 at the bottom of the apparatus.
This is because the ash fumigated by the magnetized air supply type fumigation apparatus A of the present invention is accumulated as magnetic ion powder ash, and the magnetism of the ion powder ash accumulated in the lower part of the furnace is supplied. By reacting with the magnetism of the magnetized air, the fumigation process can be stabilized in the furnace by the magnetic synergistic effect and the treatment capacity can be increased.
For this reason, if there is no ash at the bottom, the ash is accumulated by the processed product (dust etc.) as dry as possible. First, a predetermined amount of processed material (dust, etc.) that is as dry as possible is introduced from the inlet 11 at the top of the processing housing 1, and an amount that can secure the required amount of ash to be accumulated is introduced, and then the lid is closed. . The ash removal opening 13 is opened, fire is introduced from the ash removal opening 13, the processed material (trash etc.) accumulated in the processing casing is ignited, the door 14 is closed, and the ash removal opening 13 is closed.
A magnetized air supply device 6 including an air supply pipe 61 disposed on the back surface of the present processing apparatus and a magnetic device 62 installed therein, a flow rate adjusting valve 63, an air storage chamber S2, and an air supply pipe 64 by closing the door 14. To operate. The activated air is taken in while gradually reducing the flow rate adjustment valve 63 that was initially opened. Therefore, by applying a magnetic field line to the oxygen taken into the fumigation processing chamber S3, a magnetic field having omnidirectionality is generated inside the apparatus, thereby 20% paramagnetic oxygen and 78% diamagnetism. It is divided into nitrogen and trace elements, and magnetic low-temperature plasma is generated in an oxygen-free furnace. In the apparatus, fumigation treatment with oxygen and magnetism concentrated at a low temperature and atomized is executed, and the generation of dioxins is suppressed as much as possible.
(See Fig. 5 (a))

投入された蓄積された処理物(ゴミなど)は、前記貯気室S2を形成する各傾斜案内板3の表面から燻蒸処理室S3へ向けて相対抗するよう水平状に複数配設される給気パイプ64により支持されており、投入直後の処理待ちの状態から、燻蒸処理による熱で乾燥されながら処理待ちの状態へと降下移行し、その後燻蒸処理され、中央部分に火芯玉(コア)が形成される。燻蒸処理中の処理物は常に磁場振動に曝された状態と置かれている。最終的に燻蒸処理されると灰化され、灰床へと崩落し灰Cとなって蓄積される。以後、燻蒸処理・灰化に伴って容積縮小され除去された空所を補うように徐々に処理物が降下し続け、燻蒸処理が続行される(図5(a)参照)。
この燻蒸処理は、今までの燃焼の原理とは異なるもので、この燻蒸処理によれば、燃焼処理灰のダイオキシンの検出、排気中のダイオキシンの検出も基準値をはるかに下回ったものとすることができる。
A plurality of the accumulated processed materials (trash etc.) that are thrown in are arranged in a horizontal manner so as to oppose each other from the surface of each inclined guide plate 3 forming the air storage chamber S2 toward the fumigation processing chamber S3. It is supported by the air pipe 64, and it is lowered from the state of waiting for processing immediately after being put into the state of waiting for processing while being dried by the heat of the fumigation process, and then subjected to fumigation treatment. Is formed. Processed products during fumigation are always exposed to magnetic field vibrations. When it is finally subjected to fumigation, it is ashed, falls to an ash bed, and accumulates as ash C. Thereafter, the treated product gradually descends so as to make up for the voids that have been reduced in volume due to fumigation and ashing, and the fumigation process is continued (see FIG. 5A).
This fumigation process is different from the conventional combustion principle. According to this fumigation process, the detection of dioxin in combustion ash and the detection of dioxin in exhaust gas shall be far below the standard value. Can do.

次にまた、開閉蓋12を開いて処理筐体1上部の投入口11から、処理物蓄積空間S1内に適宜の処理物を所定量投入し、満杯に装填し終わったら、開閉蓋12を閉鎖して、燻蒸処理を継続する。
開閉蓋12の閉鎖し、前記と同様の燻蒸処理が実行される。この際も、ダイオキシンの発生が極力抑制される。
なお、従来、燃焼炉におけるダイオキシン生成を抑制するため、800℃以上の高温での処理が義務付けられ、二次燃焼機関の設置が必要であったが、本装置は燻蒸処理であるので、二次燃焼機関の設置を不要とし、低温処理(300〜400℃)でもダイオキシンの発生しにくい装置であると同時に、極力酸素の供給を抑えて、ダイオキシン類の基となる二つのベンゼン環を酸素で結び付けない(図5(b)参照)。
その際、飛び出したCL ̄はNa ̄等と結合し、安定した化合物となる。さらに、NOx・SOx類にも有効に作用し、有害物質の発生を抑制することができる。
さらに、燻熱状態で有機物の振動エネルギーが熱を発生させ、処理物を白灰化させる。
通常、処理を完了するまでの行なうまでの時間は約10時間ほどであった。処理中は、未開封のまま放置する。
この燻蒸処理を実施する際における、投入される処理物の性状についての留意点として、含水量の高い(65%以上)を投入した場合には処理時間が延びることがある。また、安全のため、燻蒸処理の途中で蓋開閉は行なわないこと、が挙げられる。
Next, the opening / closing lid 12 is opened, and a predetermined amount of an appropriate processing object is introduced into the processing object accumulation space S1 from the insertion port 11 at the top of the processing casing 1, and when the loading is completed, the opening / closing lid 12 is closed. Then, continue the fumigation process.
The open / close lid 12 is closed, and the fumigation process similar to the above is performed. Also at this time, generation of dioxins is suppressed as much as possible.
Conventionally, in order to suppress the production of dioxins in the combustion furnace, a treatment at a high temperature of 800 ° C. or higher has been obligatory, and a secondary combustion engine has been required to be installed. It is not necessary to install a combustion engine, and it is a device that does not easily generate dioxins even at low temperatures (300-400 ° C). At the same time, it suppresses the supply of oxygen as much as possible and connects the two benzene rings that form the basis of dioxins with oxygen. No (see FIG. 5B).
At that time, the popped out CL ̄ is combined with Na ̄ and the like to become a stable compound. Furthermore, it effectively acts on NOx / SOx and can suppress the generation of harmful substances.
In addition, the vibration energy of the organic matter generates heat in a scorching state, causing the processed product to become gray.
Usually, the time until completion of the treatment is about 10 hours. Leave unopened during processing.
When carrying out this fumigation process, as a point to keep in mind regarding the properties of the processed product to be added, the processing time may be extended when a high water content (65% or more) is added. In addition, for safety, the lid is not opened and closed during the fumigation process.

以上の燻蒸処理において、燻蒸処理箇所S3内における、燻蒸の中心となっている火芯玉(コア)の位置について変更するする必要が生じたときは、複数の給気パイプに接続の流量調整弁63の開度を個別に調整することにより、火芯玉(コア)位置を調整することができる。   In the fumigation process described above, when there is a need to change the position of the fireball (core) that is the center of fumigation in the fumigation point S3, the flow rate adjusting valves connected to the plurality of supply pipes By adjusting the opening degree of 63 individually, the position of the fireball (core) can be adjusted.

本考案の磁化給気式燻蒸処理装置Aによる燻蒸処理終了後、処理装置下部の灰床板4に蓄積された灰Cについては、次の無機物分別処理が実行される。
本考案の磁化給気式燻蒸処理装置Aでは無機物(金属、石、ガラス)は燻蒸処理できないので、投入処理物にこれらが混入されたまま燻蒸処理されたときには、燻蒸処理の結果、処理できない無機物(金属、ガラス等)は灰Cに混ざって下部に蓄積される。この場合、無機物(金属、ガラス等)を包含した灰を装置外へ取出し、篩などを用いて除去する。この除去作業は、無機物(金属、ガラス等)の蓄積量により、何回かの燻蒸処理終了を経た後一括して実施するか、灰Cを装置外へ取出し、その取出の都度に実施するか、さらに一旦別のヤードに貯蔵しておいて、定期的に実施するか、任意である。このようにして蓄積された灰の中から、金属、ガラスなどが分別撤去される。
After the fumigation process by the magnetization supply type fumigation apparatus A of the present invention, the following inorganic substance separation process is performed on the ash C accumulated on the ash floor plate 4 at the lower part of the treatment apparatus.
Since the inorganic material (metal, stone, glass) cannot be fumigated by the magnetization supply type fumigation processing apparatus A of the present invention, when the fumigation treatment is carried out with these being mixed in the treated material, the inorganic material that cannot be treated as a result of the fumigation treatment. (Metal, glass, etc.) is mixed with ash C and accumulated in the lower part. In this case, ash containing inorganic substances (metal, glass, etc.) is taken out of the apparatus and removed using a sieve or the like. Depending on the accumulated amount of inorganic substances (metal, glass, etc.), this removal work should be carried out in batch after several fumigation treatments are completed, or ash C is taken out of the device and is taken every time it is taken out In addition, it is stored in another yard once and is carried out regularly or arbitrarily. Metal, glass, etc. are separated and removed from the ash accumulated in this way.

燻蒸煙の消煙・消臭処理は、処理筐体1の上部に搭載の水タンク8により実行される。
水タンク8は、その内部に前後の室に区切る左右長手方向のゲート81a、前方室と後方室において各室を複数の区分室に隙間を通じて連通するように仕切るゲート81b、81cを備え、また、水タンク8の上部に給水のための給水口82、水タンク8の底部に排水のための排水口84、水タンク8内の水位Lを所定のレベルに維持させ、所定レベル以上の水をオーバーフローさせる溢水口83を備える。そこで、各接続口の接続される給排水ライン(図示省略)に備える弁(図示省略)によって、水タンク8内の水位Lを所定のレベルに維持するよう蓄水し、燻蒸煙の上下ジグザグ状の流動が許容できるようにする。
そこで水タンク8が所定の水位Lに蓄水したとき、その内部を前後の室に区切る左右長手方向のゲート81aと、前方室と後方室において各室を複数の区分室に隙間を通じて連通するように仕切るゲート81b、81cを通じて、燻蒸煙は、前後迂回路に形成された上下ジグザグ状の煙道Pを通過する中で、燻蒸煙に含まれるダスト、煙成分が捕獲され、上部の排気筒85から排出される。このとき、大半は蒸気であり、煙ではなく、目視では殆んど見えない程度の湯煙になり排気筒85から排出される。このように、本考案の磁化給気式燻蒸処理装置Aでは燻蒸処理に伴う煙塵を排出することはない。
The fumigation / deodorization process of the fumigation smoke is executed by the water tank 8 mounted on the upper part of the processing housing 1.
The water tank 8 includes a gate 81a in the longitudinal direction that divides the front and rear chambers inside the water tank 8, gates 81b and 81c that partition the chambers in the front chamber and the rear chamber so as to communicate with a plurality of compartments through gaps, A water inlet 82 for supplying water at the top of the water tank 8, a drain outlet 84 for draining at the bottom of the water tank 8, and maintaining the water level L in the water tank 8 at a predetermined level, overflowing water above a predetermined level. An overflow port 83 is provided. Therefore, water is stored so as to maintain the water level L in the water tank 8 at a predetermined level by a valve (not shown) provided in a water supply / drainage line (not shown) to which each connection port is connected. Make the flow acceptable.
Therefore, when the water tank 8 stores water at a predetermined water level L, the left and right longitudinal gates 81a that divide the interior of the water tank 8 into front and rear chambers, and each chamber in the front chamber and the rear chamber communicate with a plurality of compartments through gaps. The fumigation smoke passes through the upper and lower zigzag flue P formed in the front and rear detours through the gates 81b and 81c, and dust and smoke components contained in the fumigation smoke are captured, and the upper exhaust pipe 85 is captured. Discharged from. At this time, most of the steam is vapor, not smoke, but hot steam that is hardly visible to the naked eye and is discharged from the exhaust pipe 85. Thus, in the magnetization supply type fumigation processing apparatus A of the present invention, the dust accompanying the fumigation process is not discharged.

燻蒸煙は、これが水タンク8の水に吸収されて貯留されたものは、木酢液としての副産物に生まれ変わり得る原料として利用でき、また、水タンク8の処理後、排気筒85から排出される水蒸気は、微かな燻蒸臭(副産物として生成される木酢液の臭気)はあるが、焼却を行ったときのような煙や異臭はない。このように、排気筒85から排出される排出物は、煙ではなく水蒸気であって、環境にやさしく、公害の虞はないので、居住周辺環境にあっても安心して使用できる。   The fumigation smoke, which is absorbed and stored in the water in the water tank 8, can be used as a raw material that can be reborn as a by-product as a pyroligneous acid solution, and the steam discharged from the exhaust pipe 85 after the treatment of the water tank 8. Although there is a slight fumigation odor (odor of wood vinegar produced as a by-product), there is no smoke or off-flavor like incineration. As described above, the exhaust discharged from the exhaust pipe 85 is not smoke but is water vapor, which is environmentally friendly and has no risk of pollution.

本願考案の磁化給気式燻蒸処理装置を全体的に示すが、給気パイプを含め磁化給気装置を省略し、炉内の傾斜案内板部分について斜視的に透視して示した概要図である。FIG. 1 is a schematic diagram showing a perspective view of a tilted guide plate portion in a furnace, omitting a magnetized air supply device including an air supply pipe, generally showing a magnetization air supply type fumigation processing device of the present invention. . 磁化給気式燻蒸処理装置を正面から見た概要図である。It is the schematic which looked at the magnetization supply type fumigation processing apparatus from the front. 磁化給気式燻蒸処理装置を裏面から見た磁化給気装置の一部、給気磁化手段、流量調整弁の配置を示す概要図である。It is the schematic which shows arrangement | positioning of a part of magnetization supply apparatus which looked at the magnetization supply type | formula fumigation apparatus from the back surface, supply air magnetization means, and a flow regulating valve. 水タンクの分解斜視図であり、(a)は上蓋部分を取り外した状態を、(b)は水タンクを組み立てるための分解図である。It is a disassembled perspective view of a water tank, (a) is the state which removed the upper cover part, (b) is an exploded view for assembling a water tank. 燻蒸処理を説明するための概要図であり、(a)は装置内における有機廃棄物の燻蒸処理過程を状況位置で示し、(b)はプラズマの分解工程を図解的に示す図である。It is the schematic for demonstrating fumigation processing, (a) shows the fumigation process of the organic waste in an apparatus in a situation position, (b) is a figure which shows the decomposition | disassembly process of plasma graphically. 磁化給気式燻蒸処理装置の付属装置を示し、(a)は処理装置に側面に設置される熱防護ネット及び隣設のステップ台と梯子の概要図であり、(b)はステップ台と梯子結合部分で(a)の丸印部分を拡大して示す断面図である。The attached apparatus of a magnetization supply type fumigation processing apparatus is shown, (a) is a schematic diagram of the heat protection net installed on the side of the processing apparatus and the adjacent step base and ladder, and (b) is the step base and ladder. It is sectional drawing which expands and shows the circled part of (a) in the coupling | bond part.

符号の説明Explanation of symbols

1 処理筐体
1a 脚
11 処理物投入口
12 開閉蓋
12a 把手
12b 牽引ロープ
12c バランスウェイト
13 灰取出し口
14 扉
2 矩形筒体
3 傾斜案内板
3a 通口
4 灰床板
4a 通口
5 底板
5a 排水パイプ
6 磁化給気装置
61 給気配管
62 給気磁化手段
63 流量調整弁
64 給気パイプ
64a 下側傾斜給気口
7 連結管
8 水タンク
81 ゲート
81a,81b,81c ゲート
82 注水管
83 溢水管
84 ドレーン
85 排気筒
9 ステップ台
9a 脚
9b 係止孔
10 梯子
10a フック
11 熱防護ネット
A 磁化給気式燻蒸処理装置
B 廃棄物
C 灰
D ドレーン室
L 水位
P 煙道
S1 処理物蓄積空間
S2 貯気室
S3 燻蒸処理空間
S4 循環路
S5 灰蓄積部
W 貯水
DESCRIPTION OF SYMBOLS 1 Processing housing | casing 1a Leg 11 Processed material inlet 12 Opening / closing lid 12a Handle 12b Tow rope 12c Balance weight 13 Ash extraction port 14 Door 2 Rectangular cylinder 3 Inclined guide plate 3a Outlet 4 Ash floor plate 4a Through port 5 Bottom plate 5a Drain pipe 6 Magnetized air supply device 61 Air supply pipe 62 Air supply magnetizing means 63 Flow rate adjusting valve 64 Air supply pipe 64a Lower inclined air supply port 7 Connection pipe 8 Water tank 81 Gate 81a, 81b, 81c Gate 82 Water injection pipe 83 Overflow pipe 84 Drain 85 Exhaust tube 9 Step base 9a Leg 9b Locking hole 10 Ladder 10a Hook 11 Thermal protection net A Magnetized air supply type fumigation processing equipment B Waste
C Ash D Drain room L Water level
P Flue S1 Processed product storage space S2 Storage chamber S3 Fumigation processing space S4 Circulation path S5 Ash storage unit W Water storage

Claims (6)

処理筐体は、その頂部に備える処理物投入口及びこれを施蓋する開閉蓋と、その周壁内側に間隔を置いて循環路Sを形成して配設され、その内側を上下に連通し処理物蓄積空間を形成する矩形筒体と、さらに処理物蓄積空間下方で、処理筐体の一方の対抗する側面下部に各設置の傾斜案内板により傾斜案内板の内側に形成される燻蒸処理空間及び傾斜案内板と筐体内壁間に形成される三角形状の貯気室と、処理筐体1の他方の対抗する側面の各側面下部に備える灰取出し口及びこれを開閉する扉と、処理筐体の裏面に給気磁化手段及び流量調整弁を介し配設され、前記貯気室に連通する給気配管及び前記傾斜案内板より燻蒸処理空間へ向けて突設される給気パイプを含み、給気パイプが各傾斜案内板より燻蒸処理空間へ向けて相対抗するよう水平状に複数配設され、給気配管から貯気室及び給気パイプを通じて燻蒸処理箇所へ空気を磁化し供給する複数の磁化給気装置と、処理筐体の上部に連結管を介して接続され、燻蒸処理空間から発生の燻蒸煙の消煙及び脱臭処理をする水タンクを備え、処理筐体内壁に接合される傾斜案内板の周縁は処理物の水分を下方へ導く通口が形成され、ドレーン室を通じ処理筐体の底面から排水可能に構成されていることを特徴とする磁化給気式燻蒸処理装置。   The processing housing is disposed with a processing material inlet provided at the top, an opening / closing lid for covering the processing port, and a circulation path S formed at an interval on the inner side of the peripheral wall. A rectangular cylinder that forms an object accumulation space, and a fumigation treatment space that is formed inside the inclined guide plate by an inclined guide plate installed at the lower part of one side of the processing housing at the lower side of the process storage space, and A triangular storage chamber formed between the inclined guide plate and the inner wall of the housing, an ash outlet provided at the lower portion of each side of the other side of the processing housing 1, a door for opening and closing the opening, and the processing housing An air supply pipe arranged on the back surface of the air supply via a supply air magnetizing means and a flow rate adjusting valve and communicating with the air storage chamber and an air supply pipe projecting from the inclined guide plate toward the fumigation treatment space. The air pipes oppose each fumigation space from each inclined guide plate Plurally arranged in a flat shape, connected to a plurality of magnetized air supply devices that magnetize and supply air from the air supply piping to the fumigation processing location through the air storage chamber and the air supply pipe, via a connecting pipe And a water tank that eliminates and deodorizes the fumigation smoke generated from the fumigation treatment space, and the peripheral edge of the inclined guide plate joined to the inner wall of the treatment housing is formed with a passage that guides the moisture of the treated product downward. A magnetized air supply type fumigation processing apparatus, characterized in that it can be drained from the bottom surface of the processing casing through the drain chamber. 請求項1において、前記給気磁化手段は永久磁石を使用するものであることを特徴とする磁化給気式燻蒸処理装置。 2. The magnetization supply type fumigation processing apparatus according to claim 1, wherein the supply air magnetization means uses a permanent magnet . 請求項1又は2において、前記水平対向的に複数配設される給気パイプは、給気パイプの各先端を傾斜壁面に略並行する面内に位置させる共に給気パイプ相互を千鳥状に多段に配置し、給気パイプの先端を下方側に向く下側傾斜給気口としたことを特徴とする磁化給気式燻蒸処理装置。 3. The air supply pipes according to claim 1 or 2, wherein a plurality of the air supply pipes arranged horizontally opposed to each other are arranged such that each end of the air supply pipe is positioned in a plane substantially parallel to the inclined wall surface and the air supply pipes are multi-staged in a staggered manner. A magnetized air supply type fumigation processing apparatus, characterized in that the air supply pipe is a lower inclined air supply port with the front end of the air supply pipe facing downward. 請求項1ないし3のいずれかにおいて、前記水タンクは水槽を天井から前後に仕切る1枚のゲートと、前方の空間を複数に仕切る複数のゲート及び後方の空間を複数に仕切る複数のゲートと、水タンクに給水する注水管、水タンクから排水するドレーン及び水タンクの水位を所定のレベルに維持する溢水管とを備え、燻蒸処理空間から排出の燻蒸煙を前方空間及びこれに続いて後方空間を上下ジグザグ状に屈曲流動できるように、前後に仕切る1枚のゲートの後流部に流路を形成したことを特徴とする磁化給気式燻蒸処理装置。   The water tank according to any one of claims 1 to 3, wherein the water tank is a gate that partitions the water tank forward and backward from the ceiling, a plurality of gates that divide the front space into a plurality of spaces, and a plurality of gates that divide the rear space into a plurality of spaces. A water injection pipe that supplies water to the water tank, a drain that drains from the water tank, and an overflow pipe that maintains the water level of the water tank at a predetermined level. The fumigation smoke discharged from the fumigation treatment space is in the front space and subsequently in the rear space. A magnetized air supply type fumigation processing device is characterized in that a flow path is formed in the wake portion of one gate that is divided forward and backward so that it can be bent and flow in a zigzag shape. 請求項1ないし4のいずれかにおいて、処理筐体1の4側面に熱防護ネットを付設したことを特徴とする磁化給気式燻蒸処理装置。 5. The magnetization supply type fumigation processing apparatus according to claim 1, wherein a thermal protection net is attached to four side surfaces of the processing housing 1. 請求項1ないし5のいずれかにおいて、磁化給気式燻蒸処理装置の周辺に隣接して設置され、高所での投入物の投入作業に供する鋼製ステップ台と鋼製梯子を備え、ステップは上部に水平な金網の足場を有する脚付き台座に孔を有し、梯子は、その先端に形成した折り曲げたフック状の係止突起を有し、前記台座の孔と梯子のフック状突起を嵌合係止可能としたことを特徴とする磁化給気式燻蒸処理装置。
In any one of Claims 1 thru | or 5, It is installed adjacent to the circumference | surroundings of the magnetization supply type | formula fumigation processing apparatus, It is equipped with the steel step stand and steel ladder which are used for the injection | throwing-in operation | work of an input in a high place, A step is There is a hole in a legged pedestal with a horizontal wire mesh scaffolding at the top, and the ladder has a bent hook-like locking projection formed at the tip, and the hole in the pedestal and the hook-like projection on the ladder are fitted A magnetized air supply type fumigation processing device characterized in that it can be locked together.
JP2006010043U 2006-12-12 2006-12-12 Magnetized air supply type fumigation equipment Expired - Fee Related JP3129814U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009113008A (en) * 2007-11-09 2009-05-28 Inretto Kk Fluid magnetizer, magnetized fluid feeding apparatus, magnetic treatment apparatus, and magnetic treatment method
JP2013126642A (en) * 2011-12-19 2013-06-27 Esujekku:Kk Method and device for decomposing organic substance

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009113008A (en) * 2007-11-09 2009-05-28 Inretto Kk Fluid magnetizer, magnetized fluid feeding apparatus, magnetic treatment apparatus, and magnetic treatment method
JP2013126642A (en) * 2011-12-19 2013-06-27 Esujekku:Kk Method and device for decomposing organic substance

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