JP2010075823A - Apparatus for decomposition treatment of organic matter - Google Patents

Apparatus for decomposition treatment of organic matter Download PDF

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JP2010075823A
JP2010075823A JP2008245885A JP2008245885A JP2010075823A JP 2010075823 A JP2010075823 A JP 2010075823A JP 2008245885 A JP2008245885 A JP 2008245885A JP 2008245885 A JP2008245885 A JP 2008245885A JP 2010075823 A JP2010075823 A JP 2010075823A
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tar
decomposition
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organic matter
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Jiro Terasawa
治朗 寺澤
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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    • Y02W30/62Plastics recycling; Rubber recycling

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Abstract

<P>PROBLEM TO BE SOLVED: To carry out combustion decomposition treatment by magnetically burning organic matter at a low temperature of 300 to 400°C by magnetized air. <P>SOLUTION: An air introduction port 22 of a magnetized air introduction pipe 21 for introducing magnetized air is formed in a bowl-shaped decomposition pot 7 while penetrating the decomposition pot 7 and, on the other hand, organic matter D is fed to the decomposition pot 7 and magnetized air for combustion enough not to extinguish fire is introduced through the magnetized air introduction pipe 21 into the organic matter D ignited by an ignition rod 26 installed in the decomposition pot 7 to carry out combustion and decomposition treatment by magnetically burning the organic matter D at a low temperature and also, smoke containing tar and steam generated by the combustion and decomposition treatment is led upward and the tar and steam are separated in a tar removal part 2 and further the smoke from which water and tar are removed is deodorized in a deodorization part 3 by exposing the smoke in an environment where a deodorization liquid is sprayed and made to be odorless and discharged. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、金属類、ガラス類、鉱物等の無機物を除く、プラスチック、ナイロン樹脂等を含む産業廃棄物、医療廃棄物、生ごみ、肉類等の食品廃棄物等の有機物を、分解釜を下部に備えた分解処理槽内に投入し、磁界内を通過させて励起した燃焼用の磁化空気を分解釜に導入し、前記有機物をガス、石油等の燃料を全く使用することなく、酸素の吸入を火が消えない程度まで抑えて、前記有機物を磁力燃焼させて燃焼分解処理すると共に、前記燃焼分解させた際に発生したタールと水蒸気による臭気と煙を除去し、無臭化して大気中に排気し、ダイオキシンを日本における発生基準値以下に抑えことができ、またCOの削減にも寄与することができる有機物分解処理装置に関するものである。 The present invention removes organic matter such as industrial waste including plastics, nylon resin, etc., medical waste, food waste such as garbage, meat, etc. Introduced into the cracking tank, the magnetized air for combustion that was excited by passing through the magnetic field and introduced into the cracking tank was introduced into the decomposition treatment tank, and the organic matter was sucked in without using any fuel such as gas or petroleum. The organic matter is combusted and decomposed by magnetically burning to the extent that the fire does not extinguish, and the odor and smoke caused by the tar and water vapor generated during the combustion and decomposition are removed, and it is exhausted into the atmosphere without being brominated. In addition, the present invention relates to an organic matter decomposition treatment apparatus that can suppress dioxins below the generation standard value in Japan and contribute to CO 2 reduction.

従来、有機物を磁力熱により分解処理する有機物処理装置が、下記の特許文献1に開示されて公知である。 2. Description of the Related Art Conventionally, an organic substance processing apparatus that decomposes an organic substance by magnetic heat is disclosed in Patent Document 1 below and is known.

そして、特許文献1に記載のものは、磁界内を通過させて励起した燃焼用空気を断面逆四角錐形状の処理室内に導入し、該処理室内に投入した有機物を乾留炭化処理するに当たって、磁界内を通過させて励起した燃焼用空気を、前記処理室の周囲の複数個所の空気導入口から処理室内に所定量、強制導入するよう構成されている。 And the thing of patent document 1 introduce | transduces the combustion air excited through the inside of a magnetic field in the process chamber of a cross-sectional inverted quadrangular pyramid shape, and in carrying out dry distillation carbonization treatment of the organic substance thrown into this process chamber, a magnetic field A predetermined amount of combustion air excited by passing through the inside is forcedly introduced into the processing chamber from a plurality of air inlets around the processing chamber.

また、処理室からの排ガスを加熱して、排ガス中の異臭発生源と煤を燃焼させて消臭・消煙を図るよう構成されている。 Further, the exhaust gas from the processing chamber is heated to burn off the off-flavor generation source and soot in the exhaust gas to deodorize and smoke.

特開2005−29600号公報JP-A-2005-29600

前記特許文献1記載のものは、処理室の形状が断面逆四角錐状をなしているため、4つの角部(コーナー部)が存在すると共に、空気導入口が前記処理室の壁面に対して直角に貫通して前記処理室に臨むようにされているため、空気導入口より導入された励起した燃焼用空気が、前記処理室の角部には死角となって到達しないので、処理室内に均一に燃焼用空気を導入することができず、従って有機物の分解処理能力が低下するという課題があった。 In the device described in Patent Document 1, since the shape of the processing chamber has an inverted quadrangular pyramid shape, there are four corners (corner portions), and the air inlet is located with respect to the wall of the processing chamber. Since the combustion air introduced from the air inlet does not reach the corner of the processing chamber as a blind spot because it penetrates at right angles and faces the processing chamber, There was a problem that the combustion air could not be uniformly introduced, and therefore the organic substance decomposition treatment capacity was lowered.

更に、前記特許文献1記載のものは、排ガスを加熱装置により800〜1200℃に加熱して、排ガス中の異臭発生源と煤を燃焼させ、これによって排ガスを完全に無害化、無色化して消臭・消煙を図っているが、前記800〜1200℃に加熱するためには、ガスや石油等の燃料を使用しなければならないので、コスト高となると共に、COの削減にも寄与しないという課題があった。 Further, in the above-mentioned Patent Document 1, the exhaust gas is heated to 800 to 1200 ° C. by a heating device to burn off the off-flavor generation source and soot in the exhaust gas, thereby making the exhaust gas completely harmless, colorless and extinguished. Odor / smoke extinguishing is attempted, but in order to heat to 800 to 1200 ° C., fuel such as gas or oil must be used, which increases costs and does not contribute to CO 2 reduction. There was a problem.

本発明は、前記課題を解決すべくなされたもので、分解処理部を構成する分解処理槽の下方部に連設された椀状の分解釜内に、磁界内を通過させて励起した燃焼用の磁化空気を導入する磁化空気導入管の空気導入口を、前記分解釜を貫通して設置する一方、前記分解釜内に有機物を投入し、然る後、前記分解釜内に設置された着火棒により着火された該有機物に対して、前記磁化空気導入管から火が消えない程度の燃焼用の磁化空気を導入して、該燃焼用磁化空気により前記有機物を300〜400℃の低温度で磁力燃焼させて燃焼分解処理をすると共に、該分解処理後に前記分解釜内において燃焼分解処理により発生したタールと水蒸気を含む煙を上昇させて、前記分解処理槽上に設置されたタール除去部で、タールと水蒸気を分離し、更に、該タール除去部に連設された消臭部で、前記水分とタールを除去された煙を、消臭液の噴霧雰囲気中に曝して消臭し、無臭化して大気中に排気するようにした有機物分解処理装置を提供しようとするものである。 The present invention has been made to solve the above-mentioned problems, and is for combustion excited by passing through a magnetic field in a bowl-shaped decomposition pot connected to a lower portion of a decomposition processing tank constituting a decomposition processing section. An air inlet of a magnetized air introduction pipe for introducing the magnetized air is installed through the decomposition kettle, while an organic substance is introduced into the decomposition kettle, and thereafter, an ignition installed in the decomposition kettle Magnetized air for combustion is introduced to the organic matter ignited by the rod from the magnetized air introduction pipe, and the organic matter is cooled at a low temperature of 300 to 400 ° C. by the magnetized air for combustion. Combustion decomposition treatment is carried out by magnetic combustion, and after the decomposition treatment, smoke containing tar and water vapor generated by the combustion decomposition treatment is raised in the decomposition vessel, and a tar removal unit installed on the decomposition treatment tank Separating tar and water vapor In the deodorization unit connected to the tar removal unit, the smoke from which the moisture and tar have been removed is exposed to the spray atmosphere of the deodorant solution to deodorize, and is not brominated and exhausted to the atmosphere. The present invention intends to provide an organic matter decomposition treatment apparatus.

本発明は、分解処理部を構成する分解処理槽の下方部に連設された椀状の分解釜内に、磁界内を通過させて励起した燃焼用の磁化空気を導入する磁化空気導入管の空気導入口を、前記分解釜を貫通して設置する一方、前記分解釜内に有機物を投入し、然る後、前記分解釜内に1本、または複数本設置された着火棒により着火された該有機物に対して、前記磁化空気導入管から火が消えない程度の燃焼用の磁化空気を導入して、該燃焼用磁化空気により前記有機物を300〜400℃の低温度で磁力燃焼させて燃焼分解処理をすると共に、該分解処理後に前記分解釜内において燃焼分解処理により発生したタールと水蒸気を含む煙を上昇させて、前記分解処理槽上に設置されたタール除去部で、タールと水蒸気を分離し、更に、該タール除去部に連設された消臭部で、前記水分とタールを除去された煙を、消臭液の噴霧雰囲気中に曝して消臭し、無臭化して大気中に排気する有機物分解処理装置であって、前記磁化空気導入管は、前記分解釜の湾曲内周壁面に沿って磁化空気を導入すべく、1本、または複数本を1組として、これを複数組、右回り方向に傾斜して装置され、前記タール除去部は、前記分解処理部の天板を貫通して排煙ダクトが連結されると共に、該排煙ダクトの上端開口部にタール除去ボックスが連結され、且つ該タール除去ボックスの一方の側壁と、該一方の側壁と対面する他方の側壁とに、先方側を下方へ傾斜したタール付着板の基端部を、前記タールと水蒸気を含む煙がジグザグ状に移動して上昇できるように、ジグザグ状の通路を有して交互に複数枚固定して形成される一方、前記各タール付着板の先端部の下面には、抵抗エッジが垂設固定され、更に、前記タール除去ボックスの底板は一方側方向へ下り傾斜に形成され、且つ該底板の一方端には排水孔が穿設されると共に、該排水孔には排水コックが連結して形成され、前記消臭部は、前記タール除去部の天板を貫通して上方へ延設された送煙ダクトの下流側に連結して装置され、消臭ボックスの一方の側壁の上方部に、前記送煙ダクトの下流側端部を開口して連結すると共に、該消臭ボックス内の前記送煙ダクトの開口連結部よりやや下方位置まで消臭液を充填すると共に、該消臭液内にポンプを設置して、該ポンプに消臭ボックスの天板の下面に、前記消臭液を噴射する多数の噴射ノズルを設けた導水管を設置する一方、該導水管の基端部に、前記ポンプに連結された送水パイプの基端部を連結し、更に前記天板に排気パイプを連通して形成するという手段を採用することにより、上記課題を解決した。 The present invention relates to a magnetized air introduction pipe for introducing magnetized air for combustion excited by passing through a magnetic field into a bowl-shaped decomposition pot connected to a lower part of a decomposition processing tank constituting a decomposition processing section. An air inlet was installed through the cracking pot, while an organic substance was charged into the cracking pot, and then ignited by one or more ignition rods installed in the cracking pot. Combustion air that does not extinguish fire from the magnetized air introduction pipe is introduced into the organic matter, and the organic matter is combusted magnetically at a low temperature of 300 to 400 ° C. by the combustion magnetized air. In addition to the decomposition treatment, the smoke containing the tar and water vapor generated by the combustion decomposition treatment is raised in the decomposition vessel after the decomposition treatment, and the tar and the water vapor are removed at the tar removal unit installed on the decomposition treatment tank. Separated and further in the tar removal section An organic matter decomposition treatment device that removes the moisture and tar removed from the moisture and tar in a continuous deodorization unit, deodorizes it, deodorizes it, and exhausts it to the atmosphere without odorization. The magnetized air introduction pipe is installed in such a manner that one or a plurality of magnetized air is introduced along the curved inner peripheral wall surface of the cracking kettle, and a plurality of these are inclined in the clockwise direction. The tar removal unit has a smoke exhaust duct connected through the top plate of the decomposition processing unit, a tar removal box connected to an upper end opening of the smoke exhaust duct, and one of the tar removal boxes The side wall of the tar and the other side wall facing the one side wall can be moved upward in a zigzag manner by the smoke containing the tar and water vapor moving the base end portion of the tar adhering plate inclined downward on the front side. In addition, zigzag passages are fixed alternately On the other hand, a resistance edge is suspended and fixed to the lower surface of the tip portion of each tar adhering plate, and the bottom plate of the tar removal box is formed to be inclined downward in one direction, and one of the bottom plates A drain hole is drilled at the end, and a drain cock is connected to the drain hole. The deodorizing part is passed through the top plate of the tar removing part and extends upward. It is connected to the downstream side of the smoke duct, and is connected to the upper part of one side wall of the deodorization box by opening and connecting the downstream end of the smoke transmission duct, and the smoke transmission in the deodorization box. The deodorizing liquid is filled to a position slightly below the opening connection portion of the duct, and a pump is installed in the deodorizing liquid, and the deodorizing liquid is sprayed onto the lower surface of the top plate of the deodorizing box. While installing a water conduit with a number of injection nozzles at the base end of the water conduit By employing means of connecting the proximal end of the linked water pipe to the pump, formed by further communicates an exhaust pipe to the top plate, the above-mentioned problems are eliminated.

本発明有機物分解処理装置によれば、磁界内を通過させて励起した燃焼用の磁化空気が、分解処理槽の角部のない椀状をした分解釜内に投入された有機物に対して、死角を有することなく均一に導入され、前記導入された磁化空気により、有機物を300〜400℃の低温度で磁力燃焼させて燃焼分解処理することができるので、ダイオキシンを日本における発生基準値以下に抑えることができ、また有機物を磁力燃焼させて燃焼分解処理後に前記分解釜内において発生したタールと水蒸気を含む煙を上昇させて、前記分解処理槽上に設置されたタール除去部で、タールと水蒸気を分離し、更に、該タール除去部に連設された消臭部で、前記水分とタールを除去された煙を、消臭液の噴霧雰囲気中に曝して消臭し、無臭化して大気中に排気することにより、COの削減にも寄与することができるという優れた効果を奏する。 According to the organic matter decomposition treatment apparatus of the present invention, the magnetized air for combustion excited by passing through the inside of a magnetic field is a dead angle with respect to the organic matter introduced into the decomposition vessel having a bowl shape without a corner portion of the decomposition treatment tank. The organic matter can be burnt and decomposed by magnetically burning at a low temperature of 300 to 400 ° C. with the introduced magnetized air, so that dioxins are kept below the generation standard value in Japan. In addition, the organic matter can be magnetically burned to increase the smoke containing tar and water vapor generated in the decomposition vessel after the combustion decomposition treatment, and the tar removal unit installed on the decomposition treatment tank Further, in the deodorization unit connected to the tar removal unit, the smoke from which the moisture and tar have been removed is deodorized by exposing it to the spray atmosphere of the deodorant liquid, and is debridged to the atmosphere. Exhaust to It brings about an excellent effect that can contribute to the reduction of CO 2.

本発明は、有機物を分解処理部の分解処理槽内に投入して、該分解処理槽の下方部に連設された分解釜内に投入された前記有機物に対し、磁界内を通過させて励起した燃焼用の磁化空気を導入する磁化空気導入管を貫通して、着火棒により予め着火された有機物に対して、前記磁化空気導入管から前記磁化空気の吸入を火が消えない程度の燃焼用の磁化空気を導入して、該燃焼用磁化空気により前記有機物を300〜400℃の低温度で磁力燃焼させて、燃焼分解処理をすると共に、該分解処理後に前記分解釜内において燃焼分解処理により発生したタールと水蒸気を含む煙を上昇させて、前記分解処理槽上に設置されたタール除去部で、タールと水蒸気を分離させ、更に、該タール除去部に連設された消臭部で、前記水分とタールを除去された煙を、消臭液の噴霧雰囲気中に曝して消臭し、無臭化して大気中に排気するよう構成されている。以下、図面に基づいて本発明有機物分解処理装置を詳細に説明する。 In the present invention, an organic substance is introduced into a decomposition treatment tank of a decomposition treatment section, and the organic substance introduced into a decomposition pot connected to a lower portion of the decomposition treatment tank is excited by passing through a magnetic field. For the organic matter that has passed through the magnetized air introduction tube for introducing the magnetized air for combustion and that has been previously ignited by the ignition rod, the inhalation of the magnetized air from the magnetized air introduction tube does not extinguish the fire. And the organic matter is magnetically combusted at a low temperature of 300 to 400 ° C. by the combustion air for combustion, and is subjected to combustion decomposition treatment. After the decomposition treatment, combustion decomposition treatment is performed in the decomposition vessel. Raising the smoke containing the generated tar and water vapor, separating the tar and water vapor in the tar removing unit installed on the decomposition treatment tank, and further, in the deodorizing unit connected to the tar removing unit, Removes moisture and tar The smoke, anti Kusashi exposed in the spray atmosphere deodorizing liquid, it is configured to exhaust to the atmosphere and odorless. Hereinafter, the organic matter decomposition treatment apparatus of the present invention will be described in detail with reference to the drawings.

本発明有機物分解処理装置は、図1に示すように、有機物Dを磁界内に通過させて励起した燃焼用の磁化空気による磁力燃焼により燃焼分解処理する分解処理部1と、該分解処理部1上に、前記有機物Dを磁化空気により、燃焼分解処理することにより発生したタールと水蒸気を含む煙を導入して、タールと水蒸気を分離するタール除去部2を設置し、更に前記タール除去部2に、該タール除去部2においてタール除去された後の煙を導入して消臭する消臭部3を連設して構成されている。 As shown in FIG. 1, the organic matter decomposition treatment apparatus of the present invention includes a decomposition treatment unit 1 that performs combustion decomposition treatment by magnetic combustion using combustion magnetized air excited by passing an organic substance D in a magnetic field, and the decomposition treatment unit 1. A tar removal unit 2 for separating tar and water vapor is introduced by introducing smoke containing tar and water vapor generated by burning and decomposing the organic substance D with magnetized air. Further, the tar removal unit 2 is installed. Further, a deodorizing unit 3 for introducing and deodorizing smoke after tar removal in the tar removing unit 2 is provided.

前記分解処理部1は、断面円筒状をした外カバー4の内部に間隙部5を有して、有機物Dの投入室6と、該投入室6の下方部に、後述する磁化空気が角部に当って滞留することがないように、内径を下方に行くに従い漸次小径として椀状に形成した分解釜7を連通して備えた断面円筒状の分解処理槽8を設けて形成されている。前記外カバー4と分解処理槽8間に間隙部5を有することにより、後述する分解釜7部における有機物Dの燃焼分解処理により発生した熱が、分解処理槽8から外カバー4に伝導することがなく、作業者の安全が確保される。 The decomposition processing unit 1 has a gap portion 5 inside an outer cover 4 having a cylindrical cross section, and a magnetized air described later is formed in a corner portion of the organic substance D input chamber 6 and a lower portion of the input chamber 6. In order to prevent stagnation, the decomposition treatment tank 8 having a cylindrical cross-section provided with a disassembly kettle 7 formed in a bowl shape with a gradually decreasing diameter as it goes downward is provided. By having the gap 5 between the outer cover 4 and the decomposition treatment tank 8, heat generated by the combustion decomposition treatment of the organic matter D in the decomposition pot 7 described later is conducted from the decomposition treatment tank 8 to the outer cover 4. The safety of workers is ensured.

前記分解釜7の底面部よりやや上方の、小径部となった内周壁面に接して、有機物Dを載置する底格子9が設置されると共に、前記分解釜7の底格子9の上下に股がって、分解処理されて発生した灰を排出する灰排出口10を開口する一方、外カバー4から前記灰を外部へ排出できるように、前記灰排出口10と外カバー4とを排出管11で連通して、該外カバー4に開閉自在に設けた開閉扉12を開放して灰を排出できるように形成されている。 A bottom grid 9 on which the organic substance D is placed is installed in contact with an inner peripheral wall surface having a small diameter part slightly above the bottom surface of the decomposition pot 7 and above and below the bottom grid 9 of the decomposition pot 7. The ash discharge port 10 and the outer cover 4 are discharged so that the ash can be discharged to the outside from the outer cover 4 while opening the ash discharge port 10 for crushing and discharging the ash generated by the decomposition treatment. It is formed so that the ash can be discharged by opening and closing the open / close door 12 provided in the outer cover 4 so as to be openable and closable.

更に、前記分解処理槽8の上端面を天板13で密閉すると共に、該天板13の一方側寄りに有機物Dの投入管14を貫通して密に固定する一方、該投入管14の上方部は前記外カバー4より上方へ突出して上端に前記有機物Dの投入口15を開口すると共に、前記投入管14の下端部には、有機物Dの落下口16を開口して前記投入室6に臨ませ、更に、前記投入口15および落下口16に開閉蓋17・18を開閉自在、且つ密閉できるように取付けて形成されている。 Further, the upper end surface of the decomposition treatment tank 8 is sealed with a top plate 13, and the organic substance D insertion pipe 14 is passed through and closely fixed to one side of the top board 13, while the upper side of the introduction pipe 14 is fixed. The portion protrudes upward from the outer cover 4 and opens the organic substance D inlet 15 at the upper end, and the organic substance D dropping port 16 is opened at the lower end of the inlet pipe 14 into the inlet chamber 6. Furthermore, the opening and closing lids 17 and 18 are attached to the charging port 15 and the dropping port 16 so that they can be opened and closed and sealed.

前記投入管14の投入口15に取付けられた開閉蓋17は、作業者が該開閉蓋17の上面の基端部側に突設された取っ手19を持って上方へ開放することができるよう取付けると共に、該投入管14の落下口16に取付けられた開閉蓋18は、下方へ開放されるよう取付けるが、前記開閉蓋18は、前記分解処理槽8内に設置されているため、外カバー4に取付けられた制御装置20による電動式の開閉操作により開閉するか、または前記分解処理槽8外に設けた開閉レバー(図示省略)の操作により開閉できるよう形成されている。図1においては、制御装置20による電動式で開閉できるよう図示されており、以下実施例の説明は電動式として説明する。 The open / close lid 17 attached to the input port 15 of the input tube 14 is attached so that an operator can open the handle 19 with a handle 19 protruding from the base end side of the upper surface of the open / close lid 17. At the same time, the opening / closing lid 18 attached to the dropping port 16 of the charging pipe 14 is attached so as to be opened downward. However, since the opening / closing lid 18 is installed in the decomposition treatment tank 8, the outer cover 4. It is formed so that it can be opened / closed by an electric opening / closing operation by a control device 20 attached to the door or by an operation of an opening / closing lever (not shown) provided outside the decomposition treatment tank 8. In FIG. 1, the control device 20 is illustrated so as to be opened and closed by an electric type, and the description of the embodiment will be described below as an electric type.

本発明有機物分解処理装置は、有機物Dを分解処理槽8内に連続して投入し、連続分解処理ができるよう構成されている。先ず、本発明有機物分解処理装置を稼動させる前の第1段階として、外カバー4の外部に設置された階段Sを作業者が登って、投入管14の投入口15に取付けられた開閉蓋17を取っ手19を用いて開放すると共に、前記投入管14の落下口16に取付けられた開閉蓋18を制御装置20により開放した後、前記有機物Dを該投入管14内に投入して、投入室6を経て下方の分解釜7の底格子9上に落下させる。 The organic matter decomposition treatment apparatus of the present invention is configured so that the organic matter D can be continuously charged into the decomposition treatment tank 8 and can be continuously decomposed. First, as a first step before operating the organic matter decomposition processing apparatus of the present invention, the operator climbs the staircase S installed outside the outer cover 4 and opens and closes lid 17 attached to the inlet 15 of the inlet pipe 14. Is opened using the handle 19 and the opening / closing lid 18 attached to the drop port 16 of the charging pipe 14 is opened by the control device 20, and then the organic substance D is charged into the charging pipe 14, 6, it is dropped onto the bottom grid 9 of the lower decomposition pot 7.

そして、前記投入室6および分解釜7内に適宜量の有機物Dを投入した後、前記開閉蓋17・18をそれぞれ閉鎖して、前記分解処理槽8内を密閉状態として分解処理の準備工程を完了する。前記したように、本発明有機物分解処理装置は、連続して分解処理可能であるため、前記準備工程において分解処理槽8内に投入された有機物Dが、分解釜7において第1次の分解処理中に、前記開閉蓋17を開放して第2次の有機物Dを投入管14内に投入して、該開閉蓋17を閉鎖して貯留しておき、前記分解釜7内の分解処理により、第1次の有機物Dの容量が減容された段階で、開閉蓋18を開放して、第2次の有機物Dを分解処理中の第1次の有機物D上に投下することができる。以下同一操作を繰返すことにより、連続分解処理が可能となる。 An appropriate amount of the organic substance D is introduced into the charging chamber 6 and the decomposition kettle 7, and then the open / close lids 17 and 18 are closed, and the decomposition treatment tank 8 is sealed to prepare a decomposition treatment preparation step. Complete. As described above, since the organic matter decomposition treatment apparatus of the present invention can be continuously decomposed, the organic matter D introduced into the decomposition treatment tank 8 in the preparation step is subjected to the primary decomposition treatment in the decomposition pot 7. Inside, the opening / closing lid 17 is opened and the secondary organic substance D is introduced into the charging pipe 14, the opening / closing lid 17 is closed and stored, and by the decomposition process in the decomposition pot 7, When the volume of the primary organic substance D is reduced, the opening / closing lid 18 is opened, and the secondary organic substance D can be dropped onto the primary organic substance D being decomposed. Thereafter, by repeating the same operation, continuous decomposition processing can be performed.

一方、前記分解処理部1の分解釜7の周壁には、磁化空気を該分解釜7内に投入された有機物Dに導入するため、複数組の磁化空気導入管21を貫通して、その先端の空気導入口22が前記有機物Dに臨むように配置されている。 On the other hand, in order to introduce the magnetized air into the organic substance D introduced into the decomposition kettle 7 on the peripheral wall of the cracking kettle 7 of the decomposition processing unit 1, a plurality of sets of magnetized air introduction pipes 21 are penetrated and the tip thereof The air inlet 22 is arranged so as to face the organic matter D.

前記磁化空気導入管21は、北半球における磁気の流れは右回り(時計回り)であるので、前記分解釜7内に導入された磁化空気も滞留することなく、右回りに椀状の分解釜7の湾曲内周壁面に沿って導入すべく、図3に示すように、複数の磁化空気導入管21が右回り方向に、特に限定する必要はないが、好ましくは120℃程度の傾斜角度をもって装置されている。なお、図3においては、磁化空気導入管21は3本を1組として4組設置されているが、1本、または複数本を1組として複数組設置してもよく、その本数および組数は、有機物Dの処理量および分解釜7の容量によって任意に設定することができる。 In the magnetized air introduction pipe 21, the magnetic flow in the northern hemisphere is clockwise (clockwise). Therefore, the magnetized air introduced into the decomposition pot 7 does not stay, and the bowl-shaped decomposition pot 7 rotates clockwise. As shown in FIG. 3, the plurality of magnetized air introduction pipes 21 need not be limited in the clockwise direction as shown in FIG. 3, but preferably have an inclination angle of about 120 ° C. Has been. In FIG. 3, four magnetized air introduction pipes 21 are installed as three groups, but one or a plurality of magnetized air introduction pipes 21 may be installed. Can be arbitrarily set according to the processing amount of the organic substance D and the capacity of the decomposition vessel 7.

また、前記磁化空気導入管21は、外カバー4および分解釜7を貫通して設置されているが、該分解釜7外に突出した磁化空気導入管21の上流側端部である空気取入口23には、自然吸気で空気を取入れる取入空気量を調整するバルブ24が設けられると共に、該バルブ24より下流側の磁化空気導入管21の外周には、前記空気取入口23より取入れた空気を、磁界内を通過させて励起した燃焼用の磁化空気とすべく、並列状の磁石25が周設されている。 The magnetized air introduction pipe 21 is installed through the outer cover 4 and the decomposition pot 7, and is an air inlet that is an upstream end portion of the magnetized air introduction pipe 21 protruding outside the decomposition pot 7. 23 is provided with a valve 24 for adjusting the intake air amount for taking in air by natural intake air, and the outer periphery of the magnetized air introduction pipe 21 downstream from the valve 24 is introduced from the air intake port 23. Parallel magnets 25 are provided around the air so as to be magnetized air for combustion excited by passing through the magnetic field.

前記空気取入口23より取入れた空気を磁化して燃焼用の磁化空気とする並列状の磁石26は、特に限定する必要はないが、好ましくは、3000〜15000G、特に好ましくは8000G程度の磁場の強さを有する永久磁石、または電磁石を使用することが推奨される。 The parallel magnet 26 that magnetizes the air taken in from the air inlet 23 to become magnetized air for combustion is not particularly limited, but preferably has a magnetic field of about 3000 to 15000 G, particularly preferably about 8000 G. It is recommended to use a strong permanent magnet or an electromagnet.

また、前記分解釜7を貫通した複数組の磁化空気導入管21のうち、それぞれ対面位置となるいずれか2本の磁化空気導入管21には、本発明有機物分解処理装置の稼動前に、前記分解釜7に最初に投入して底格子9上に落下した有機物Dに着火して燃焼させるための、着火用の着火棒26が添設されており、該着火棒26は、図示していない電力供給用コードに接続されると共に、該電力供給用コードは制御装置20に連結されている。前記着火棒26は、前記底格子9上に落下した有機物Dに、該着火棒26が接触していなくても着火させる必要があるため、800℃程度の高温となるよう設定され、また前記着火棒26への通電は制御装置20により行い、前記有機物Dがある程度燃焼するまで通電を続けるが、その通電時間はタイマー設定により行うことが推奨される。 In addition, among the plurality of sets of magnetized air introduction pipes 21 penetrating the decomposition kettle 7, any two magnetized air introduction pipes 21 respectively facing each other are provided with the above-described organic matter decomposition treatment apparatus before the operation thereof. An ignition rod 26 for ignition is attached to ignite and burn the organic matter D that is first put into the decomposition pot 7 and dropped on the bottom grid 9, and this ignition rod 26 is not shown. The power supply cord is connected to the control device 20 while being connected to the power supply cord. The ignition rod 26 needs to be ignited even if the ignition rod 26 is not in contact with the organic matter D that has fallen on the bottom grid 9, so that the ignition rod 26 is set to a high temperature of about 800 ° C. The energization of the rod 26 is performed by the control device 20 and the energization is continued until the organic matter D is combusted to some extent. However, it is recommended that the energization time be set by a timer.

なお、前記着火棒26は、実施例においては、磁化空気導入管21のうち、それぞれ対面位置となるいずれか2本の磁化空気導入管21の空気導入口22に近接して添設されているが、その取付位置および本数は任意であり、底格子9上の有機物Dを着火させることができる取付位置および本数であればよい。 In the embodiment, the ignition rod 26 is attached adjacent to the air inlets 22 of any two of the magnetized air introduction pipes 21 that face each other. However, the attachment position and the number thereof are arbitrary, and may be any attachment position and the number that can ignite the organic matter D on the bottom lattice 9.

前記構成より成る分解処理部1の分解釜7で、有機物Dを磁化空気により燃焼分解すると、前記有機物Dは熱分解され、臭気の主成分となるタールと水蒸気を含む煙が発生するが、本発明装置においては、前記タールと水蒸気を含む煙を、前記分解処理槽8から上昇させて、前記分解処理槽8上に設置されたタール除去部2内に流入させ、該タール除去部2内において、前記煙中のタールと水蒸気を分離し、更に該タールと水蒸気を分離した後の煙は、前記タール除去部2に連設された消臭部3内に導入されて消臭され、無臭化して大気中へ排気できるよう形成されている。 When the organic substance D is combusted and decomposed with magnetized air in the decomposition vessel 7 of the decomposition processing unit 1 having the above-described configuration, the organic substance D is thermally decomposed to generate smoke containing tar and water vapor as main components of odor. In the invention apparatus, the smoke containing the tar and water vapor is raised from the decomposition treatment tank 8 and flows into the tar removal unit 2 installed on the decomposition treatment tank 8. The tar and water vapor in the smoke are separated, and the smoke after the tar and water vapor are further separated is introduced into the deodorizing unit 3 connected to the tar removing unit 2 to be deodorized and debrominated. So that it can be exhausted to the atmosphere.

前記タール除去部2は、前記分解処理部1の天板13の他方側寄りに、該天板13を貫通して排煙ダクト27が連結されると共に、該排煙ダクト27の上端開口部28にタール除去ボックス29を連結する一方、該タール除去ボックス29の一方の側壁30と、該一方の側壁30と対面する他方の側壁31とに、貼着性のあるタールを付着させるため、先方側を下方へ傾斜したタール付着板32の基端部を、タールと水蒸気を含む煙がジグザグ状に移動して上昇できるように、ジグザグ状の通路33を有して交互に複数枚固定して形成されている。なお、前記タール付着板32は、熱をもったタールを冷却させるために、冷却作用を有するセラミックスにより製造することが推奨される。 The tar removing unit 2 is connected to the other side of the top plate 13 of the decomposition processing unit 1 through the top plate 13 and connected to a smoke exhaust duct 27, and an upper end opening 28 of the smoke exhaust duct 27. While the tar removal box 29 is connected to the one side wall 30, the tar removal box 29 is attached to the one side wall 30 and the other side wall 31 facing the one side wall 30. A base end portion of the tar adhering plate 32 inclined downward is formed by alternately fixing a plurality of zigzag passages 33 so that smoke containing tar and water vapor can move up in a zigzag manner. Has been. In addition, in order to cool the tar with heat, it is recommended that the tar adhering plate 32 be made of ceramics having a cooling action.

また、前記各タール付着板32の先端部の下面には、抵抗エッジ34が垂設されており、該各タール付着板32の末端部において、前記各タール付着板32間の通路33の通過中に、該各タール付着板32の下面に付着したタールが、前記抵抗エッジ34によって、前記各タール付着板32から飛出すのを阻止することにより、前記タールの該各タール付着板32への付着効率を上げることができる。 Further, a resistance edge 34 is suspended from the lower surface of the tip of each tar adhering plate 32, and the end portion of each tar adhering plate 32 is passing through the passage 33 between the tar adhering plates 32. Further, the tar adhering to each tar adhering plate 32 is prevented by the tars adhering to the lower surface of each tar adhering plate 32 being prevented from jumping out from each tar adhering plate 32 by the resistance edge 34. Efficiency can be increased.

前記タール除去部2に流入した前記タールと水蒸気を含む煙は、図5の矢印で示すように、前記ジグザグ状に設置された各タール付着板32間の通路33を上昇して通過する間に、前記各タール付着板32の下面に貼着性のあるタールが付着すると共に、該水蒸気が一部のタール分と結合して液状タールとなってそれぞれ該各タール付着板32の下面の傾斜面に当って下方へ滴下した液状タールのうち、下段のタール付着板32aの下面の傾斜面に当って下方へ滴下した液状タールは、末端部の抵抗エッジ34aから、前記タール除去ボックス29の底板35上に滴下し、中段のタール付着板32bの下面の傾斜面に当って下方へ滴下した液状タールは、末端部の抵抗エッジ34bから前記下段のタール付着板32aの上面に滴下し、その傾斜面に沿って流下して、末端部から前記タール除去ボックス29の底板35上に滴下し、更に、上段のタール付着板32cの下面の傾斜面に当って下方へ滴下した液状タールは、末端部の抵抗エッジ34cから前記中段のタール付着板32bの上面に滴下して、その傾斜面に沿って流下し、そして該中段のタール付着板32bの末端部から前記下段のタール付着板32aの上面に滴下し、更にその傾斜面に沿って流下して、末端部から前記タール除去ボックス29の底板35上に滴下する。 The smoke containing the tar and water vapor that has flowed into the tar removing unit 2 is raised while passing through the passages 33 between the tar adhering plates 32 installed in a zigzag shape, as indicated by arrows in FIG. In addition, sticking tar adheres to the lower surface of each tar attachment plate 32, and the water vapor combines with a part of tar to form a liquid tar, which is an inclined surface on the lower surface of each tar attachment plate 32, respectively. Among the liquid tars dropped downward on the bottom, the liquid tar dropped downward on the inclined surface of the lower surface of the tar attachment plate 32a on the lower stage passes through the bottom edge 35 of the tar removal box 29 from the resistance edge 34a at the end. The liquid tar dropped on the lower surface of the middle tar attachment plate 32b and dropped downward is dropped from the resistance edge 34b of the end portion onto the upper surface of the lower tar attachment plate 32a. The liquid tar that has flowed down along the surface and dropped onto the bottom plate 35 of the tar removal box 29 from the end portion and further dropped downward on the inclined surface of the lower surface of the upper tar attaching plate 32c From the resistance edge 34c to the upper surface of the middle tar attachment plate 32b, flow down along the inclined surface, and from the end of the middle tar attachment plate 32b to the upper surface of the lower tar attachment plate 32a. Then, it is dropped along the inclined surface and dropped onto the bottom plate 35 of the tar removal box 29 from the end portion.

そして、前記タール除去ボックス29の底板35は一方側方向へ下り傾斜に形成され、且つ該底板35の一方端には排水孔36が穿設されると共に、該排水孔36には排水コック37が連結され、前記底板35上に滴下して留った液状タールを、前記排水コック37を開いて排水孔36を介して排出するよう構成されている。 A bottom plate 35 of the tar removal box 29 is formed to be inclined downward in one direction, and a drain hole 36 is formed at one end of the bottom plate 35, and a drain cock 37 is provided in the drain hole 36. The liquid tar, which is connected and dropped on the bottom plate 35, is configured to be discharged through the drain hole 36 by opening the drain cock 37.

前記のように、前記悪臭の原因となるタールと水蒸気のうち、タールは前記タール除去部2の各タール付着板32に付着することによって煙から除去されるが、前記各タール付着板32は、これに多くのタールが付着した場合、前記タール除去ボックス29の両側壁30・31を取外し(前記取外す手段は、例えば蝶番を使用して開閉自在とする等、任意であり、図示していない)、前記タールが付着した各タール付着板32を新しいタール付着板32に取換えて使用する。勿論、新しいタール付着板32に取換えるのではなく、洗浄して再利用することも可能である。 As described above, among tar and water vapor that cause the malodor, tar is removed from the smoke by adhering to each tar adhering plate 32 of the tar removing unit 2, but each tar adhering plate 32 is When a large amount of tar adheres to this, both side walls 30 and 31 of the tar removal box 29 are removed (the means for removing is optional, for example, it can be opened and closed using a hinge, not shown) The tar adhering plates 32 to which the tar has adhered are replaced with new tar adhering plates 32 for use. Of course, it is also possible to clean and reuse instead of replacing the tar mounting plate 32 with a new one.

一方、前記タール除去部2に連通する消臭部3は、前記タール除去ボックス29の天板38を貫通して上方へ延設された送煙ダクト39の下流側に連結して装置される。すなわち、消臭部3は、箱状の消臭ボックス40の一方の側壁41の上方部に、前記送煙ダクト39の下流側端部を開口して連結すると共に、該消臭ボックス40内の前記送煙ダクト39の開口連結部よりやや下方位置まで、タールを除去する作用を有する消臭液42を充填すると共に、該消臭液42内にポンプ43を設置して、該ポンプ43に消臭ボックス40の天板44の下面に多数の噴射ノズル45を設けた導水管46を設置する一方、該導水管46の基端部に、前記ポンプ43に連結された送水パイプ47の基端部を連結し、更に前記天板44に消臭された空気を大気中へ排気する排気パイプ48を連通して形成されている。
On the other hand, the deodorizing unit 3 communicating with the tar removing unit 2 is connected to the downstream side of the smoke transmission duct 39 extending upward through the top plate 38 of the tar removing box 29. That is, the deodorizing unit 3 is connected to the upper part of one side wall 41 of the box-shaped deodorizing box 40 by opening the downstream end portion of the smoke transmission duct 39, and the inside of the deodorizing box 40. A deodorizing liquid 42 having an action of removing tar is filled up to a position slightly below the opening connecting portion of the smoke sending duct 39, and a pump 43 is installed in the deodorizing liquid 42, and the pump 43 is turned off. A water guide pipe 46 provided with a number of injection nozzles 45 is installed on the lower surface of the top plate 44 of the odor box 40, and a base end portion of a water supply pipe 47 connected to the pump 43 at the base end portion of the water guide pipe 46. And an exhaust pipe 48 that exhausts the deodorized air to the atmosphere.

前記構成より消臭部3の消臭ボックス40内に、タール除去部2においてタールおよび水蒸気を除去された煙が、図5の矢印で示すように、送煙ダクト39を介して導入されると、前記消臭ボックス40の天板44と消臭液42間の空間部49内に前記煙が充満する一方、該充満した煙に対して導水管46の噴射ノズル45から、ポンプ43により送水された消臭液42を噴霧状に噴射して、該噴霧雰囲気中に煙を曝して消臭する。前記消臭されて無臭化されたた空気は、無臭空気として、前記排気パイプ48から大気中に排気される。 When the smoke from which tar and water vapor have been removed in the tar removal unit 2 is introduced into the deodorization box 40 of the deodorization unit 3 from the above configuration through the smoke transmission duct 39 as shown by the arrows in FIG. The space 49 between the top plate 44 and the deodorizing liquid 42 of the deodorizing box 40 is filled with the smoke, and the filled smoke is fed by the pump 43 from the spray nozzle 45 of the water conduit 46. The deodorizing liquid 42 is sprayed in the form of a spray, and smoke is exposed to the spray atmosphere to deodorize it. The deodorized and non-brominated air is exhausted from the exhaust pipe 48 to the atmosphere as odorless air.

そして、前記噴射ノズル45から煙に対して噴霧状に噴射された後の消臭液42は、消煙ボックス40内の消臭液42中に落下して、ポンプ43を介して循環使用され、適宜時間経過後、新しい消臭液42と取換える。 The deodorizing liquid 42 after being sprayed from the spray nozzle 45 in the form of a spray falls into the deodorizing liquid 42 in the smoke eliminating box 40 and is circulated through the pump 43, After an appropriate time has elapsed, the deodorizing liquid 42 is replaced.

前記構成より成る本発明有機物分解処理装置の作用について説明する。先ず、前記したように、分解処理の準備工程において、先ず外カバー4の開閉蓋17および落下口16の開閉蓋18をそれぞれ開放して、第1次の有機物Dを投入管14内に投入して、投入室6を経て下方の分解釜7の底格子9上に落下させた後、前記開閉蓋17および開閉蓋18を閉鎖して、前記分解処理槽8内を密閉状態とする。 The operation of the organic matter decomposition treatment apparatus of the present invention having the above configuration will be described. First, as described above, in the preparation process for the decomposition process, first, the opening / closing lid 17 of the outer cover 4 and the opening / closing lid 18 of the dropping port 16 are opened, and the first organic substance D is put into the charging pipe 14. Then, after dropping onto the bottom lattice 9 of the lower decomposition kettle 7 through the charging chamber 6, the open / close lid 17 and the open / close lid 18 are closed, and the inside of the decomposition treatment tank 8 is sealed.

前記底格子9上に有機物Dが落下すると、制御装置20により着火棒26に通電して、該着火棒26を発熱させて800℃程度の温度にまで発熱すると、該着火棒26の発熱により、前記底格子9上の有機物Dが着火して燃焼を始める。この初期の段階においては、バルブ24を全開にしておくが、これにより磁化空気導入管21から多くの磁化空気が分解釜7内に磁気空気導入管21を介して導入されて、前記着火棒26による有機物Dの燃焼を助けると共に、消臭部3における噴射ノズル45からの消臭液42の噴射も開始される。 When the organic substance D falls on the bottom grid 9, the control device 20 energizes the ignition rod 26, and the ignition rod 26 generates heat to generate a temperature of about 800 ° C. When the ignition rod 26 generates heat, The organic substance D on the bottom lattice 9 ignites and starts to burn. In this initial stage, the valve 24 is fully opened. As a result, a large amount of magnetized air is introduced from the magnetized air introduction pipe 21 into the cracking vessel 7 via the magnetic air introduction pipe 21, and the ignition rod 26. The combustion of the organic substance D due to the odor is started, and the injection of the deodorizing liquid 42 from the injection nozzle 45 in the deodorizing unit 3 is also started.

前記着火棒26の発熱により底格子9上の有機物Dは燃焼を始め、煙が分解処理槽8からタール除去部2および消臭部3を経て、排気パイプ48から排煙されるが、作業者は該排気パイプ48から排煙される煙の色を注視し、その色によって以下の操作をすることになる。 The organic matter D on the bottom grid 9 starts to combust due to the heat generated by the ignition rod 26, and the smoke is exhausted from the decomposition treatment tank 8 through the tar removing unit 2 and the deodorizing unit 3 and exhausted from the exhaust pipe 48. Gazes at the color of the smoke exhausted from the exhaust pipe 48 and performs the following operations according to the color.

すなわち、前記着火棒26への通電後、3〜5分経過後に排気パイプ46から排煙が始まり、煙の色が薄い茶色で立ち登っている間は、前記バルブ24を全開にしたままにしておいて、磁化空気を最大限磁気空気導入管21の空気導入口22から分解釜7内に導入する。そして、10分位経過後に、煙の色が白く拡散している状態になると、前記バルブ24を50%程度の開放状態にして、前記磁化空気の分解釜7への導入を半分程度とする。 That is, after the energization of the ignition rod 26, smoke is started from the exhaust pipe 46 after 3 to 5 minutes have passed, and the valve 24 is kept fully open while the smoke color is light brown. Then, the magnetized air is introduced into the decomposition pot 7 from the air inlet 22 of the magnetic air inlet pipe 21 to the maximum extent. When the smoke color is diffused white after about 10 minutes, the valve 24 is opened to about 50%, and the introduction of the magnetized air into the decomposition kettle 7 is halved.

その後、25分位経過して、煙の色が白く、且つ淡く立ち登っている状態になると、前記バルブ24を25%程度の開放状態にして磁気空気の分解釜7への導入量を更に押さえ、そのままの状態で30分〜40分経過後に、前記バルブ24を10%〜15%程度、好ましくは11%〜14%程度の開放状態にして、磁化空気の導入量を、前記着火して燃焼し続けている有機物Dの火が消えない程度の最低限に押さえ、然る後、前記制御装置20により着火棒26への通電を停止する。 Then, after about 25 minutes, when the smoke is white and lightly rising, the valve 24 is opened to about 25% to further reduce the amount of magnetic air introduced into the decomposition kettle 7. After 30 to 40 minutes, the valve 24 is opened to about 10% to 15%, preferably about 11% to 14%, and the introduced amount of magnetized air is ignited and burned. The organic D is kept to a minimum so that the fire is not extinguished, and then the energization of the ignition rod 26 is stopped by the control device 20.

前記着火棒26への通電を停止すると、磁化空気導入管21の空気導入口22より分解釜7への磁化空気の導入量が、前記燃焼し続けている有機物Dの火が消えない程度であるため、前記分解釜7内の有機物Dは燃焼分解している状態が継続するが、前記各空気導入口22から磁化空気が椀状をした分解釜7内に、滞留することなく導入され続けて、分解釜7内において磁場を作ると共に、前記燃焼分
解を始めるよう、前記有機物Dに供給され、その結果、該有機物Dは通常の燃焼による焼却ではなく、分解釜7内において、300℃〜400℃の低温度で有機物の化学反応を変えて、該有機物の分子・原子の結合を断ち切る分解作用を起こし、タールと水蒸気を含む煙となって分解処理槽8内を上昇し、タール除去部2内へ流入する。
When energization of the ignition rod 26 is stopped, the amount of magnetized air introduced from the air inlet 22 of the magnetized air inlet pipe 21 into the decomposition kettle 7 is such that the burning of the organic matter D that continues to burn does not disappear. Therefore, the organic substance D in the decomposition vessel 7 continues to be burned and decomposed, but the magnetized air continues to be introduced from the air introduction ports 22 into the decomposition vessel 7 having a bowl shape without stagnation. The organic substance D is supplied to the organic substance D so as to create a magnetic field in the decomposition vessel 7 and to start the combustion decomposition. As a result, the organic substance D is not incinerated by normal combustion, but in the decomposition vessel 7 at 300 ° C. to 400 ° C. The chemical reaction of the organic substance is changed at a low temperature of 0 ° C. to cause a decomposition action that breaks the bonds between the molecules and atoms of the organic substance, and smoke that contains tar and water vapor rises in the decomposition treatment tank 8, and the tar removal unit 2 Flows in.

前記したように、本発明有機物分解処理装置は、第1次の有機物Dが分解釜7で分解処理中において、分解処理槽8内に第2次の有機物Dを投入して連続して分解処理可能である。従って、前記のように、連続して分解処理して行くと、前記着火棒26への通電は、第1次の有機物Dの分解処理槽8内への投入後の1回のみで、第2次以降の有機物Dの投入後には前記着火棒26への通電は不要である。 As described above, in the organic matter decomposition treatment apparatus of the present invention, while the primary organic matter D is being decomposed in the decomposition vessel 7, the secondary organic matter D is put into the decomposition treatment tank 8 and continuously decomposed. Is possible. Therefore, as described above, when the decomposition treatment is continuously performed, the ignition rod 26 is energized only once after the first organic substance D is introduced into the decomposition treatment tank 8, and the second It is not necessary to energize the ignition rod 26 after the next and subsequent introduction of the organic substance D.

前記分解釜7において有機物Dの分解処理により発生したタールと水蒸気を含む煙以外の灰は、分解処理終了後に灰取出口10を開口して、該分解釜7の底面や底格子9上に溜った灰を取出して排出する。 Ashes other than smoke containing tar and water vapor generated by the decomposition treatment of the organic substance D in the decomposition vessel 7 are opened on the bottom of the decomposition vessel 7 and on the bottom grid 9 after the decomposition treatment is completed. Remove and discharge the ash.

前記分解釜7における有機物Dの分解処理により発生したタールと水蒸気を含む煙は、前記のように、分解処理槽8内を上昇し、タール除去部2へ流入されて、該タール除去部2内において、ジグザグ状の通路33を上昇して通過することにより、各タール付着板32の下面にタールを付着させると共に、液状タールとして底板35上に滴下させて、煙からタールと水蒸気を分離させる。 As described above, the smoke containing tar and water vapor generated by the decomposition treatment of the organic substance D in the decomposition vessel 7 ascends in the decomposition treatment tank 8 and flows into the tar removal unit 2. , The tar is attached to the lower surface of each tar adhering plate 32 and dropped on the bottom plate 35 as a liquid tar to separate the tar and water vapor from the smoke.

前記タール除去部2において、タールと水蒸気を分離された煙は、更に送煙ダクト39を経て消臭部3内に流入して消臭される。すなわち、前記したように、消臭部3内に流入した煙は、噴射ノズル45から消臭液42が噴霧状に噴射された噴霧雰囲気中に曝されて消臭される。そして、分解処理部1において分解処理されて発生したタールと水蒸気を含む煙は、前記タール除去部2および消臭部3において、タールと水蒸気が除去されると共に、消臭されて無臭化した空気として、排気パイプ48から大気中に排気される。 In the tar removal unit 2, the smoke from which tar and water vapor are separated flows into the deodorization unit 3 through the smoke transmission duct 39 and is deodorized. That is, as described above, the smoke flowing into the deodorizing unit 3 is deodorized by being exposed to the spray atmosphere in which the deodorizing liquid 42 is sprayed from the spray nozzle 45. Then, the smoke containing tar and water vapor generated by the decomposition processing in the decomposition processing unit 1 removes the tar and water vapor in the tar removal unit 2 and the deodorization unit 3 and is deodorized and air-free. As shown in FIG.

本発明有機物分解処理装置の全体の概略斜視図である。It is a schematic perspective view of the whole organic substance decomposition processing apparatus of this invention. 同概略縦断図である。It is the same schematic longitudinal cross-sectional view. 本発明有機物分解処理装置における分解釜部分の横断平面図である。It is a cross-sectional top view of the decomposition pot part in the organic substance decomposition processing apparatus of this invention. 本発明有機物分解処理装置における分解釜と磁化空気導入管と着火棒および灰取出口を示す要部の縦断面図である。It is a longitudinal cross-sectional view of the principal part which shows the decomposition | disassembly pot, the magnetized air introduction pipe | tube, the ignition rod, and the ash removal outlet in this invention organic substance decomposition processing apparatus. 本発明有機物分解処理装置における消臭部と消煙部を示す要部の概略縦断面図である。It is a schematic longitudinal cross-sectional view of the principal part which shows the deodorizing part and smoke eliminating part in this invention organic substance decomposition processing apparatus.

符号の説明Explanation of symbols

D 有機物
S 階段
1 分解処理部
2 タール除去部
3 消臭部
4 外カバー
5 間隙部
6 投入室
7 分解釜
8 分解処理槽
9 底格子
10 灰排出口
11 排出管
12 開閉扉
13 天板
14 投入管
15 投入口
16 落下口
17 開閉蓋
18 開閉蓋
19 取っ手
20 制御装置
21 磁化空気導入管
22 空気導入口
23 空気取入口
24 バルブ
25 磁石
26 着火棒
27 排煙ダクト
28 上端開口部
29 タール除去ボックス
30 一方の側壁
31 他方の側壁
32 タール付着板
33 通路
34 抵抗エッジ
35 底板
36 排水孔
37 排水コック
38 天板
39 送煙ダクト
40 消臭ボックス
41 一方の側壁
42 消臭液
43 ポンプ
44 天板
45 噴射ノズル
46 導水管
47 送水パイプ
48 排気パイプ
49 空間部
D Organic matter S Staircase 1 Decomposition processing section 2 Tar removal section 3 Deodorization section 4 Outer cover 5 Gap 6 Input chamber 7 Decomposition pot 8 Decomposition treatment tank 9 Bottom grid 10 Ash discharge port 11 Discharge pipe 12 Opening door 13 Top plate 14 Input Pipe 15 Input port 16 Drop port 17 Open / close lid 18 Open / close lid 19 Handle 20 Control device 21 Magnetized air introduction tube 22 Air introduction port 23 Air intake port 24 Valve 25 Magnet 26 Igniting rod 27 Smoke duct 28 Upper end opening 29 Tar removal box 30 Side wall 31 Side wall 32 Tar attachment plate 33 Passage 34 Resistance edge 35 Bottom plate 36 Drain hole 37 Drain cock 38 Top plate 39 Smoke duct 40 Deodorization box 41 One side wall 42 Deodorant liquid 43 Pump 44 Top plate 45 Spray nozzle 46 Water conduit 47 Water supply pipe 48 Exhaust pipe 49 Space

Claims (1)

分解処理部を構成する分解処理槽の下方部に連設された椀状の分解釜内に、磁界内を通過させて励起した燃焼用の磁化空気を導入する磁化空気導入管の空気導入口を、前記分解釜を貫通して設置する一方、前記分解釜内に有機物を投入し、然る後、前記分解釜内に1本、または複数本設置された着火棒により着火された該有機物に対して、前記磁化空気導入管から火が消えない程度の燃焼用の磁化空気を導入して、該燃焼用磁化空気により前記有機物を300〜400℃の低温度で磁力燃焼させて燃焼分解処理をすると共に、該分解処理後に前記分解釜内において燃焼分解処理により発生したタールと水蒸気を含む煙を上昇させて、前記分解処理槽上に設置されたタール除去部で、タールと水蒸気を分離し、更に、該タール除去部に連設された消臭部で、前記水分とタールを除去された煙を、消臭液の噴霧雰囲気中に曝して消臭し、無臭化して大気中に排気する有機物分解処理装置であって、
前記磁化空気導入管は、前記分解釜の湾曲内周壁面に沿って磁化空気を導入すべく、1本、または複数本を1組として、これを複数組、右回り方向に傾斜して装置され、
前記タール除去部は、前記分解処理部の天板を貫通して排煙ダクトが連結されると共に、該排煙ダクトの上端開口部にタール除去ボックスが連結され、且つ該タール除去ボックスの一方の側壁と、該一方の側壁と対面する他方の側壁とに、先方側を下方へ傾斜したタール付着板の基端部を、前記タールと水蒸気を含む煙がジグザグ状に移動して上昇できるように、ジグザグ状の通路を有して交互に複数枚固定して形成される一方、前記各タール付着板の先端部の下面には、抵抗エッジが垂設固定され、更に、前記タール除去ボックスの底板は一方側方向へ下り傾斜に形成され、且つ該底板の一方端には排水孔が穿設されると共に、該排水孔には排水コックが連結して形成され、

前記消臭部は、前記タール除去部の天板を貫通して上方へ延設された送煙ダクトの下流側に連結して装置され、消臭ボックスの一方の側壁の上方部に、前記送煙ダクトの下流側端部を開口して連結すると共に、該消臭ボックス内の前記送煙ダクトの開口連結部よりやや下方位置まで消臭液を充填すると共に、該消臭液内にポンプを設置して、該ポンプに消臭ボックスの天板の下面に、前記消臭液を噴射する多数の噴射ノズルを設けた導水管を設置する一方、該導水管の基端部に、前記ポンプに連結された送水パイプの基端部を連結し、更に前記天板に排気パイプを連通して形成されたことを特徴とする有機物分解処理装置。
An air inlet of a magnetized air introduction pipe for introducing magnetized air for combustion that has been excited by passing through a magnetic field into a bowl-shaped decomposition pot connected to the lower part of the decomposition processing tank constituting the decomposition processing section. , While penetrating the cracker, while introducing an organic substance into the cracker, and then, against the organic matter ignited by one or more ignition rods installed in the cracker Then, the magnetized air for combustion that does not extinguish the fire is introduced from the magnetized air introduction pipe, and the organic matter is magnetically burned at a low temperature of 300 to 400 ° C. by the magnetized air for combustion to perform the combustion decomposition treatment. In addition, the smoke containing the tar and steam generated by the combustion cracking process in the cracking kettle after the cracking process is raised, and the tar and the steam are separated at the tar removing unit installed on the cracking tank, The tar removal unit In the deodorization part, the smoke from which the moisture and tar have been removed is exposed to a spray atmosphere of a deodorant liquid to deodorize, deodorize and exhaust into the atmosphere,
The magnetized air introduction pipe is installed in such a manner that one or a plurality of magnetized air is introduced along the curved inner peripheral wall surface of the cracking kettle, and a plurality of these are inclined in the clockwise direction. ,
The tar removal unit has a smoke exhaust duct connected through the top plate of the decomposition processing unit, a tar removal box connected to an upper end opening of the smoke exhaust duct, and one of the tar removal boxes To the side wall and the other side wall facing the one side wall, the base end portion of the tar adhering plate inclined downward on the front side so that the smoke containing the tar and water vapor can move in a zigzag shape and rise. A plurality of zigzag-shaped passages are alternately fixed to each other, and a resistance edge is vertically fixed to the lower surface of the tip of each tar adhering plate. Further, the bottom plate of the tar removal box Is formed so as to be inclined downward in one side direction, and a drain hole is formed at one end of the bottom plate, and a drain cock is connected to the drain hole,

The deodorization unit is connected to a downstream side of a smoke transmission duct that extends upward through the top plate of the tar removal unit, and is connected to the upper portion of one side wall of the deodorization box. The downstream end of the smoke duct is opened and connected, and the deodorizing liquid is filled to a position slightly below the opening connecting part of the smoke transmission duct in the deodorizing box, and a pump is placed in the deodorized liquid. Installed and installed on the bottom surface of the top plate of the deodorizing box on the pump is a water conduit provided with a number of injection nozzles for injecting the deodorant liquid, while the pump is installed at the base end of the water conduit. An organic matter decomposition treatment apparatus, which is formed by connecting base ends of connected water supply pipes and further connecting exhaust pipes to the top plate.
JP2008245885A 2008-09-25 2008-09-25 Apparatus for decomposition treatment of organic matter Pending JP2010075823A (en)

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WO2013133194A1 (en) * 2012-03-06 2013-09-12 東和開発株式会社 Processing device for substance to be processed
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WO2016125858A1 (en) * 2015-02-06 2016-08-11 シンエイメタルテック株式会社 Magnetic decomposition device, and magnetic decomposition method
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WO2018123565A1 (en) * 2016-12-28 2018-07-05 坂本 優蔵 Low-temperature pyrolytic treatment device for organic matter
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CN108662587A (en) * 2018-06-07 2018-10-16 广西凯泉环保工程有限公司 A kind of biological deodorizing and pyrolysis rubbish processing to be harmless system
JP2021120144A (en) * 2020-01-30 2021-08-19 弘明 太幡 Device for converting organic material to inorganic material
WO2023281703A1 (en) * 2021-07-08 2023-01-12 株式会社Clear Sky Apparatus for forming inorganic substance from organic substance
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