JP3122682U - Low temperature heat treatment furnace - Google Patents

Low temperature heat treatment furnace Download PDF

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JP3122682U
JP3122682U JP2006002612U JP2006002612U JP3122682U JP 3122682 U JP3122682 U JP 3122682U JP 2006002612 U JP2006002612 U JP 2006002612U JP 2006002612 U JP2006002612 U JP 2006002612U JP 3122682 U JP3122682 U JP 3122682U
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heat treatment
treatment chamber
chamber
air
smoke
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亀久夫 内藤
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阿部 由美
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Priority to PCT/JP2007/051684 priority patent/WO2007116598A1/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/006General arrangement of incineration plant, e.g. flow sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F23G5/0276Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using direct heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/50Control or safety arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00Combustion
    • F23G2202/10Combustion in two or more stages
    • F23G2202/101Combustion in two or more stages with controlled oxidant supply
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2219/00Treatment devices
    • F23J2219/40Sorption with wet devices, e.g. scrubbers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23LSUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
    • F23L2900/00Special arrangements for supplying or treating air or oxidant for combustion; Injecting inert gas, water or steam into the combustion chamber
    • F23L2900/00001Treating oxidant before combustion, e.g. by adding a catalyst

Abstract

【課題】廃棄物を低温熱処理させる低温熱処理炉の提供。
【解決手段】外槽1の下部内側へ、給気パイプを水平方向へ突設した下部熱処理室3を設け、下部熱処理室3の上部へ、外槽1と間隙を作って設けた内筒14よりなる上部熱処理室10を設けると共に、外槽1の上部へ蓋板付きの廃棄物投入口と、煙筒16とを設け、煙筒16は散水による浄煙槽15の一側に連結し、浄煙槽15は水槽の中へ、複数の仕切板17を所定間隔に併設し、排煙が上下屈曲流動できるようにして、その他側に煙突16を連結し、外槽1の底板と、下部熱処理室3との間に空気室2を設け、下部熱処理室3と空気室2との壁板は、少なくとも2つの対向壁又は全壁板を上向き斜板とし、空気室2へ磁化空気の給送手段を連結した低温熱処理炉。ダイオキシンの分離を未然に防止することができる。
【選択図】図1
To provide a low temperature heat treatment furnace for heat treating a waste material at a low temperature.
A lower heat treatment chamber (3) is provided inside the outer tank (1) with a supply pipe projecting in a horizontal direction, and an inner cylinder (14) is provided above the lower heat treatment chamber (3) so as to form a gap with the outer tank (1). An upper heat treatment chamber 10 is provided, and a waste inlet with a cover plate is provided on the upper part of the outer tub 1 and a smoke cylinder 16, and the smoke cylinder 16 is connected to one side of a smoke purification tank 15 by sprinkling water. The tank 15 is provided with a plurality of partition plates 17 at predetermined intervals in the water tank so that the flue gas can be bent upward and downward, the chimney 16 is connected to the other side, the bottom plate of the outer tank 1 and the lower heat treatment chamber An air chamber 2 is provided between the lower heat treatment chamber 3 and the air chamber 2, and at least two opposing walls or all wall plates are upward swash plates, and magnetized air is supplied to the air chamber 2. A low-temperature heat treatment furnace connected. Separation of dioxins can be prevented beforehand.
[Selection] Figure 1

Description

この考案は、各種廃棄物を、ダイオキシンが発生しない低温度(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した低温熱処理炉に関する。   The present invention relates to a low-temperature heat treatment furnace intended to heat various kinds of wastes at a low temperature (for example, a temperature of less than 400 ° C.) at which dioxins are not generated and to make ash.

従来廃棄物の燃焼処理については、ダイオキシンを分解して無害化する高温燃焼装置と、ダイオキシンが分離(発生)しない低温乾留装置とが提案されている。
特開平11−316006 特開2005−29600 特開2003−117534
Conventionally, with regard to the combustion treatment of waste, a high-temperature combustion apparatus that decomposes and detoxifies dioxins and a low-temperature carbonization apparatus that does not separate (generate) dioxins have been proposed.
JP-A-11-316006 JP 2005-29600 A JP 2003-117534 A

従来ごみ焼却炉内に励起状態の酸素分子を含んだ空気を吹き込み、炉内のごみを完全燃焼させることにより、ダイオキシン等の有害物質の生成を抑制しようとした発明が提案されている(特許文献1)。   Conventionally, an invention has been proposed in which air containing oxygen molecules in an excited state is blown into a waste incinerator and the waste in the furnace is completely burned to suppress the generation of harmful substances such as dioxins (patent document) 1).

また磁界内を通過させて励起した燃焼用空気を処理室に導入することにより、ダイオキシンの発生なく廃棄物を乾留炭化処理するに際して安定した操業ができる技術が提案されている(特許文献2)。   In addition, a technique has been proposed in which combustion air excited by passing through a magnetic field is introduced into a processing chamber, whereby stable operation can be performed when carbonizing carbonized waste without generation of dioxins (Patent Document 2).

次に磁気処理した空気を熱処理室に導き、700℃以下で加熱され、ついで例えば800℃〜1000℃の温度処理により、ダイオキシンの発生が抑えられる技術も提案されている(特許文献3)。   Next, a technique has also been proposed in which magnetically treated air is introduced into a heat treatment chamber and heated at 700 ° C. or lower, and then the generation of dioxins is suppressed by, for example, temperature treatment at 800 ° C. to 1000 ° C. (Patent Document 3).

前記特許文献1の発明においては、ごみを完全燃焼するとしているが、完全燃焼するのに、温度が何度になるのか、酸素分子の励起がどの程度か、ダイオキシンの無害化がどのようになるのか不明であり、これらを実用化する方法の具体案が不明である。   In the invention of Patent Document 1, it is assumed that the waste is completely burned. However, what is the temperature, how much the excitation of oxygen molecules, and how detoxification of the dioxin is made to complete combustion. It is unclear whether or not a specific method for putting these into practical use is unclear.

前記特許文献2は、低温乾留に関する発明であって、明細書記載のような廃棄物に有効とされているが、果して90℃〜120℃以下で効率よく処理できるか否か不明である。また実施装置の説明があるが、明細書記載の廃棄物に、空気を均一に供給できるのか不明瞭である。   Although the said patent document 2 is invention regarding low temperature carbonization, and is considered effective for the waste as described in the specification, it is unclear whether it can be efficiently processed at 90 ° C. to 120 ° C. or less. Moreover, although there is description of the implementation apparatus, it is unclear whether air can be supplied uniformly to the waste described in the specification.

また特許文献3の発明は、熱処理物の表面温度は700℃以下の低温に継続的に抑えることができるとされ(400℃〜700℃ではダイオキシンが発生する)、かつ内部で800℃〜1000℃以上でゆっくり熱処理するので、ダイオキシン類の発生が抑えられると説明されており、結局ダイオキシンは発生するが、少ないのか、発生したダイオキシンは無害化するのか、不明である。前記のように各部の温度の制御がダイオキシン対策として有効であるとされ乍ら、具体的手段の開示がない。   In the invention of Patent Document 3, the surface temperature of the heat-treated product can be continuously suppressed to a low temperature of 700 ° C. or lower (dioxin is generated at 400 ° C. to 700 ° C.), and 800 ° C. to 1000 ° C. inside. It has been described that since heat treatment is performed slowly, the generation of dioxins can be suppressed. Dioxins are eventually generated, but it is unclear whether the dioxins generated will be harmless or not. Although the control of the temperature of each part is effective as a countermeasure against dioxins as described above, there is no disclosure of specific means.

前記特許文献1〜3は何れもダイオキシンを抑えた(又は無害化した)廃棄物の処理に関しては、この考案と軌を一にする。然し乍ら、前記各技術は具体的手段に関し、不明瞭な点を内蔵する問題点があった。これに対し、この考案は、従来装置と同一技術と、従来示されていない新技術の結合により、低温熱処理できる(ダイオキシンの発生しない)具体的装置について提案し、前記従来の問題点を解決したのである。   Patent Documents 1 to 3 are all in line with this idea regarding the treatment of wastes in which dioxins are suppressed (or detoxified). However, each of the above technologies has a problem of incorporating unclear points regarding specific means. On the other hand, this device proposed a specific apparatus capable of low-temperature heat treatment (no generation of dioxin) by combining the same technique as the conventional apparatus and a new technique not shown so far, and solved the conventional problems. It is.

即ちこの考案は、外槽の下部内側へ、給気パイプを水平方向へ突設した下部熱処理室を設け、該下部熱処理室の上部へ、外槽と間隙を作って設けた内筒よりなる上部熱処理室を設けると共に、前記外槽の上部へ蓋板付きの廃棄物投入口と、煙筒とを設け、該煙筒は散水による浄煙槽の一側に連結し、該浄煙槽の他側に煙突を連結し、前記給気パイプは、前記外槽の底板と、下部熱処理室との間の空気室と連通させ、該空気室へ磁化空気の給送手段を連結したことを特徴とする低温熱処理炉であり、外槽の下部内側へ、給気パイプを水平方向へ突設した下部熱処理室を設け、該下部熱処理室の上部へ、外槽と間隙を作って設けた内筒よりなる上部熱処理室を設けると共に、前記外槽の上部へ蓋板付きの廃棄物投入口と、煙筒とを設け、該煙筒は散水による浄煙槽の一側に連結し、該浄煙槽の他側に煙突を連結し、前記給気パイプは、前記外槽の底板と、下部熱処理室との間の空気室と連通させ、下部熱処理室と空気室との壁板は、少なくとも2つの対向壁又は全壁板を上向き斜板とし、前記空気室へ磁化空気の給送手段を連結したことを特徴とする低温熱処理炉である。   In other words, this device is provided with a lower heat treatment chamber with an air supply pipe projecting horizontally in the lower inner side of the outer tub, and an upper portion made of an inner cylinder provided with a gap with the outer tub above the lower heat treatment chamber. A heat treatment chamber is provided, and a waste inlet with a cover plate is provided on the upper part of the outer tub, and a smoke cylinder is provided. The smoke cylinder is connected to one side of the smoke purification tank by watering, and is connected to the other side of the smoke purification tank. A low temperature characterized in that a chimney is connected, the air supply pipe communicates with an air chamber between a bottom plate of the outer tub and a lower heat treatment chamber, and a feeding means for magnetized air is connected to the air chamber. This is a heat treatment furnace. A lower heat treatment chamber is provided in the lower inner side of the outer tub, with an air supply pipe projecting in the horizontal direction, and an upper portion made of an inner cylinder provided with a gap between the outer tub and the upper portion of the lower heat treatment chamber. A heat treatment chamber is provided, and a waste inlet with a cover plate is provided at the top of the outer tank, and a smoke cylinder is provided. It is connected to one side of a water purification tank, a chimney is connected to the other side of the smoke purification tank, and the air supply pipe communicates with an air chamber between a bottom plate of the outer tank and a lower heat treatment chamber. The wall plate of the lower heat treatment chamber and the air chamber is a low temperature heat treatment furnace characterized in that at least two opposing walls or all wall plates are upward swash plates, and a magnetized air feeding means is connected to the air chamber. is there.

また他の考案は、外槽の下部内側へ、給気パイプを水平方向へ突設した下部熱処理室を設け、該下部熱処理室の上部へ、外槽と間隙を作って設けた内筒よりなる上部熱処理室を設けると共に、前記外槽の上部へ蓋板付きの廃棄物投入口と、煙筒とを設け、該煙筒は散水による浄煙槽の一側に連結し、該浄煙槽は水槽の中へ、複数の仕切板を所定間隔に併設し、排煙が上下屈曲流動できるようにして、その他側に煙突を連結し、前記外槽の底板と、下部熱処理室との間に空気室を設け、下部熱処理室と空気室との壁板は、少なくとも2つの対向壁又は全壁板を上向き斜板とし、前記空気室へ磁化空気の給送手段を連結したことを特徴とする低温熱処理炉であり、給送手段は、給送パイプの外気の吸入側へファンを設置すると共に、前記給送パイプの中間部へ、永久磁石内蔵の活性処理パイプと、バルブとを直列に介装したものである。   Further, another device is provided with a lower heat treatment chamber provided with a supply pipe projecting in a horizontal direction inside a lower portion of the outer tub, and an inner cylinder provided with a gap between the outer tub and the upper portion of the lower heat treatment chamber. An upper heat treatment chamber is provided, and a waste inlet with a cover plate is provided on the upper part of the outer tub, and a smoke cylinder, the smoke cylinder is connected to one side of the smoke purification tank by watering, and the smoke purification tank is connected to the water tank. Inside, a plurality of partition plates are provided at predetermined intervals so that the flue gas can be bent up and down, and a chimney is connected to the other side, and an air chamber is provided between the bottom plate of the outer tank and the lower heat treatment chamber. The low temperature heat treatment furnace is characterized in that at least two opposing walls or all wall plates are upward swash plates, and a magnetized air feeding means is connected to the air chamber. The feeding means includes a fan installed on the outside air suction side of the feeding pipe and the feeding pipe. To the middle section, and the permanent magnets built-in active treatment pipe, in which is interposed a valve in series.

更に他の考案は、給気パイプは、下部熱処理室と空気室とを連通させると共に、下部熱処理室へ上下多段に、かつ中央部へ達しない長さに水平方向に突設したものであり、熱処理室に温度センサーを設け、該温度センサーの出力を、外槽上部の温度計と接続したものであり、外気の給送パイプに介装するバルブは自動開閉バルブとし、該自動開閉バルブの制御器へ、温度センサーの出力を連結することとしたものである。   Still another idea is that the air supply pipe communicates with the lower heat treatment chamber and the air chamber, and projects in a horizontal direction to the lower heat treatment chamber in the upper and lower multi-stages and to a length not reaching the center, A temperature sensor is provided in the heat treatment chamber, and the output of the temperature sensor is connected to a thermometer at the upper part of the outer tub, and the valve interposed in the outside air supply pipe is an automatic opening / closing valve, and the control of the automatic opening / closing valve The output of the temperature sensor is connected to the vessel.

前記考案において、下部熱処理室と、上部熱処理室とを分けたのは、下部熱処理室では、励起した空気を均一に混合して上部熱処理室での乾燥と熱処理をスムースにすると共に、空気と熱処理気体を循環させることにあり、高温気体の利用、乾燥、熱処理とを下部より上部へ順次行っている。   In the above device, the lower heat treatment chamber is separated from the upper heat treatment chamber. In the lower heat treatment chamber, excited air is uniformly mixed so that drying and heat treatment in the upper heat treatment chamber can be performed smoothly, and air and heat treatment can be performed. In order to circulate the gas, the use of high-temperature gas, drying, and heat treatment are sequentially performed from the lower part to the upper part.

また給気パイプは水平方向へ突出しているので、投入廃棄物を支持し、適度の空気を供給すると共に、密度を保って支持し、前記投入廃棄物を完全熱処理させることができる。特に、低温(400℃未満、好ましくは300℃〜380℃)なるが故に励起酸素が均一に浸透(混入)しなければならない。   Further, since the air supply pipe protrudes in the horizontal direction, it is possible to support the input waste, supply appropriate air, and support it while maintaining the density, so that the input waste can be completely heat-treated. In particular, because of the low temperature (less than 400 ° C., preferably 300 ° C. to 380 ° C.), the excited oxygen must penetrate uniformly (mix).

前記において、空気室を大きくとり、ここから給気パイプを介し、励起空気を均一に送り込むが為に、給気パイプは、上下2段とし、かつ熱処理室の中央に達しない程度に長短突設し、その先端は切口を下向きにして切断することが好ましい。また、先端を塞ぎ、給気パイプへ多数の通気孔を設けることもある。またロストル式にして廃棄物を支持しつつ給気するか、ロストルとは別に給気パイプのみにするかは、処理すべき主要廃棄物の形態により選定する。この考案で処理しようとする廃棄物には、特に制限がなく、家庭廃棄物及び産業廃棄物の何れでも、基本的処理形態は同一であるが、特に水分の多い廃棄物(例えば水分70%以上)と、水分の少ない廃棄物(例えば水分30%以下)とを一緒に処理する場合には適宜混合することが好ましい。また最初は、高温灰(例えば300℃以上の灰)を溜めてから、本格的に処理する方が、円滑な処理ができる。   In the above, since the air chamber is made large, and the excitation air is uniformly fed from here through the air supply pipe, the air supply pipe has two upper and lower stages, and is provided with long and short projections so as not to reach the center of the heat treatment chamber. However, it is preferable to cut the tip with the cut face downward. In addition, the tip may be closed and a large number of air holes may be provided in the air supply pipe. In addition, whether to supply air while supporting waste or to use only an air supply pipe separately from the rooster is selected according to the form of main waste to be processed. The waste to be treated by this device is not particularly limited, and the basic treatment form is the same for both household waste and industrial waste, but waste with particularly high moisture (for example, 70% or more moisture). ) And wastes with low water content (for example, water content of 30% or less) are preferably mixed as appropriate. In addition, first, after storing high-temperature ash (for example, ash of 300 ° C. or higher), it is possible to perform a smooth process by treating in earnest.

この考案の熱処理炉は、廃棄物を低温(ダイオキシンの発生温度以下、400℃未満)で、効率よく熱処理させる為に、給送空気を励起し、給気中に含まれた酸素を活性化した。従って低温であっても、効率よく熱処理させた。そこで強制給気(ファンを使用)と、給気量の調整(バルブの開度による)を図った。前記給気を過不足なく供給することは至難であるが、熱処理温度と、給気量の関係を正確に保つことにより、目的を達成した。前記熱処理は、励起した酸素によって有機物を気化させ、300℃〜380℃程度に加熱することにより炭その他を無気質の灰化するものである。   In the heat treatment furnace of this device, in order to efficiently heat-treat the waste at a low temperature (below the dioxin generation temperature, less than 400 ° C.), the supply air is excited and oxygen contained in the supply air is activated. . Therefore, it was heat-treated efficiently even at a low temperature. Therefore, forced air supply (using a fan) and adjustment of the air supply amount (depending on the valve opening) were attempted. Although it is extremely difficult to supply the supply air without excess or deficiency, the object was achieved by accurately maintaining the relationship between the heat treatment temperature and the supply amount. In the heat treatment, an organic substance is vaporized by excited oxygen and heated to about 300 ° C. to 380 ° C. to ash a charcoal and the like to anaerobic ash.

そこで熟練者がバルブ調整すれば、目的を達成できるが、汎用化する為には、温度センサーの出力(熱処理温度)と、バルブの開閉との適性値を求め、これを制御系に組み込むことによって自動制御が確実になった。然し乍ら少容量の熱処理炉にあっては、給気量と、熱処理温度とを、手動調整できるように、図表などを付属させることもできる。また上部熱処理室は、二重壁の内側に設けたので、最も高温部分は熱遮断される。   Therefore, if an expert adjusts the valve, the purpose can be achieved, but in order to make it versatile, the appropriate values of the output of the temperature sensor (heat treatment temperature) and the opening and closing of the valve are obtained and incorporated into the control system. Automatic control has been ensured. However, in a small-capacity heat treatment furnace, a chart or the like can be attached so that the air supply amount and the heat treatment temperature can be manually adjusted. In addition, since the upper heat treatment chamber is provided inside the double wall, the highest temperature portion is thermally shielded.

従って外槽壁は60℃以下位であり、作業者が触れても火傷を生じるおそれはない位である。この原因は、上部熱処理室内の熱処理温度が低い為に、輻射熱が外槽壁に伝達されることが少ないからである。また外槽壁と、内筒との間隙を気体が流動(下降)する為でもある。然し乍ら、外槽壁を断熱被覆して、熱の放散を防止することを妨げるものではない。   Therefore, the outer tank wall is at a temperature of about 60 ° C. or less, and there is no possibility of causing burns even if the operator touches it. This is because the heat treatment temperature in the upper heat treatment chamber is low, so that radiant heat is hardly transmitted to the outer tank wall. This is also because the gas flows (falls) through the gap between the outer tank wall and the inner cylinder. However, it does not prevent the outer tank wall from being heat-insulated to prevent heat dissipation.

この考案における空気励起については、給送量に対応して永久磁石の容量を増加させることにより、十分の処理ができる。更に遠赤外線発生セラミックス類を給送パイプに連接した処理パイプ内へ充填し、永久磁石の磁力との相乗作用を求めることも有用であるが、その最良については今後の研究課題となる。   With regard to air excitation in this device, sufficient processing can be performed by increasing the capacity of the permanent magnet corresponding to the amount of feed. In addition, it is useful to fill far-infrared-generating ceramics into a processing pipe connected to a feeding pipe to obtain a synergistic effect with the magnetic force of a permanent magnet, but the best will be a future research subject.

この考案によれば、廃棄物は低温(例えば380℃以下)で熱処理される為に、ダイオキシンは分離せず、従って煙の中及び灰の中は共にダイオキシン濃度が低い(表1)。また廃棄物は灰のみになる為に、残りの重量は5%以下、容量も5%前後となる。前記における空気の磁化は、例えば2000ガウス〜4000ガウスの永久磁場で、0.1m/分〜1m/分の処理を行う。 According to this device, since the waste is heat-treated at a low temperature (for example, 380 ° C. or lower), dioxins are not separated, and thus the concentration of dioxins is low in both smoke and ash (Table 1). Further, since the waste is only ash, the remaining weight is 5% or less and the capacity is about 5%. Magnetization of the air in said, for example in 2000 gauss to 4000 gauss permanent magnetic field, performing 0.1 m 3 / min to 1 m 3 / min of the processing.

また前記のように、供給する空気を強力な磁場を通過させることによって、空気中の酸素をイオン化して、その活性を向上(酸化力の強化)させる。その結果、熱分解処理が促進される。即ち一般の燃焼処理と異なり、低温酸化(低温処理)であっても、急速に処理される。前記酸素の活性化によって、恰も燃焼のように、又はそれ以上に早く分解処理される。   Further, as described above, the supplied air is passed through a strong magnetic field to ionize oxygen in the air and improve its activity (strengthening the oxidizing power). As a result, the thermal decomposition process is promoted. That is, unlike general combustion processing, even low-temperature oxidation (low-temperature processing) is processed rapidly. By the activation of the oxygen, soot is decomposed as if it burns or even faster.

この考案の装置は原則的にバッチ式であって、一度に100kg〜1000kgとか、装置の大きさに対応した量を一度に処理することができると共に、若干の連続処理(例えば100kg容量の装置であっても、順次投入により300kgの処理も可能)もできる。この場合には、最初投入後ある程度の時間(例えば熱処理開始後3時間)の経過後100kg追加し、次の2時間後に最終の100kgを追加することもできる。また2時間間隔で継続投入しても支障はない。   The device of the present invention is basically a batch type, and can process 100 kg to 1000 kg at a time or an amount corresponding to the size of the device at the same time, and a little continuous processing (for example, a device of 100 kg capacity). Even if it is, processing of 300 kg is also possible by sequential charging). In this case, 100 kg can be added after a lapse of a certain time after the first charging (for example, 3 hours after the start of heat treatment), and the final 100 kg can be added after the next 2 hours. Moreover, there is no problem even if it is continuously input at intervals of 2 hours.

このような処理方式をとれば、連続処理炉となるが、灰は適宜取り出し、篩にかけて半処理固形物を再処理する。   If such a processing method is taken, it becomes a continuous processing furnace, but the ash is appropriately taken out and sieved to reprocess the semi-processed solid matter.

この考案の装置によれば、励起空気の制限通気により廃棄物を低温熱処理させて灰にすることができるので、ダイオキシンの発生を極めて少量(基準内)に抑えた中で、各種廃棄物を確実、かつ効率よく処理できる効果がある。   According to the device of this device, waste can be heat-treated at low temperature by limited ventilation of excitation air, so that various wastes can be reliably generated while dioxin generation is suppressed to a very small amount (within standard). In addition, there is an effect that it can be processed efficiently.

また各種廃棄物を、直接かつ容易に低温熱処理して灰にするので、最終的にきわめて少量(例えば5%以下)になる効果がある。更に灰を土壌改良剤に使用すれば、処理後の廃棄物0になる効果がある。   In addition, various wastes are directly and easily subjected to low-temperature heat treatment to make ash, so that there is an effect that the final amount becomes extremely small (eg, 5% or less). Furthermore, if ash is used as a soil conditioner, there is an effect that the waste after the treatment becomes zero.

この考案は、外槽の下部内側へ空気室と、下部熱処理室を順次設置し、前記空気室と、下部熱処理室とは、上向傾斜の側壁で仕切る。前記空気室には、活性空気の給送パイプを連結し、前記上向傾斜の側壁には、給気パイプを貫通して、前記空気室と、下部熱処理室とを連通させ、前記給気パイプの下部熱処理室側を下向きに斜切開口させて給気とロストルを兼用させる。前記給送パイプには、活性処理パイプと、バルブとを介装してある。   In this device, an air chamber and a lower heat treatment chamber are sequentially installed inside the lower part of the outer tub, and the air chamber and the lower heat treatment chamber are partitioned by an upwardly inclined side wall. An active air supply pipe is connected to the air chamber, and an air supply pipe is passed through the upward inclined side wall so that the air chamber communicates with the lower heat treatment chamber. The lower heat treatment chamber side is opened obliquely downward so that both air supply and rooster are used. The feeding pipe is provided with an active processing pipe and a valve.

前記下部熱処理室の上部には、外槽内壁と、若干の間隙を保って、同心状に内筒を固定して上部熱処理室とする。この間隙により、外槽外への熱損失を極力防止する。   In the upper part of the lower heat treatment chamber, an inner cylinder is fixed concentrically with the inner wall of the outer tub, and an upper heat treatment chamber is formed. This gap prevents heat loss outside the outer tank as much as possible.

前記外槽の頂板に一側に投入口を設けて密閉蓋を開閉自在に被冠する。前記頂板の他側に煙筒を設けて浄煙槽の一側へ開口させ、前記浄煙槽には、所定間隔で縦仕切板を併設して、上下屈曲煙道を形成し、前記浄煙槽の他側に煙突を設けると共に、前記浄煙槽内へ適量の水を入れて、排煙が水面に接触浄化されるようにしてある。この水は適宜取り換えて、浄煙効率を高く保つことにする。前記浄煙槽中に散水部を設けて浄煙することもできる。   An inlet is provided on one side of the top plate of the outer tub so that the sealing lid can be freely opened and closed. A smoke cylinder is provided on the other side of the top plate and opened to one side of the smoke septic tank. The smoke septic tank is provided with vertical partition plates at predetermined intervals to form a vertically bent flue, and the smoke septic tank A chimney is provided on the other side, and an appropriate amount of water is put into the smoke clarifier so that the smoke is contacted and purified on the water surface. This water will be replaced as appropriate to keep the smoke purification efficiency high. A sprinkler may be provided in the smoke clarifier to purify the smoke.

前記活性処理パイプ内には永久磁石を設置して、通過空気を磁化し、又は永久磁石と共に、遠赤外線発生鉱物(例えば麦飯石、電気石など)を収容し、磁気処理と遠赤処理をさせて、空気の活性化(励起、イオン化)を促進させることができる。   A permanent magnet is installed in the active treatment pipe to magnetize the passing air, or together with the permanent magnet, contain far-infrared ray generating minerals (for example, barley stone, tourmaline, etc.) to perform magnetic treatment and far-red treatment. Thus, air activation (excitation, ionization) can be promoted.

[調査例1]
本願考案の装置を使用して、次の条件で熱処理した場合の各種物質の含有量は次のとおりである。
[Survey Example 1]
The content of various substances when heat-treated under the following conditions using the device of the present invention is as follows.

1.条件
(1)使用廃棄物 家庭用廃棄物(水分90%)
(2)熱処理 3時間80℃以下で連続熱処理
(3)空気量 毎分0.1m
(4)永久磁石 4000ガウス
2.ダイオキシン類を測定した所、表1を得た(基準値より著しく少ない)。

Figure 0003122682
1. Condition (1) Waste used Household waste (water content 90%)
(2) Heat treatment Continuous heat treatment at 80 ° C. or less for 3 hours (3) Air volume 0.1 m 3 / min
(4) Permanent magnet 4000 Gauss 2. When dioxins were measured, Table 1 was obtained (significantly less than the reference value).
Figure 0003122682

3.一酸化炭素、酸素濃度連続測定及びばい煙測定をした所、表2を得た(但し煙浄化をしていない)。この場合に、一酸化炭素以外の各物質量は著しく少なくなっている。従って、一酸化炭素低減の処置を設けることが好ましい。

Figure 0003122682
3. When carbon monoxide, oxygen concentration continuous measurement and soot smoke measurement were performed, Table 2 was obtained (however, smoke was not purified). In this case, the amount of each substance other than carbon monoxide is remarkably reduced. Therefore, it is preferable to provide a measure for reducing carbon monoxide.
Figure 0003122682

この発明の実施例を図1、2について説明すると、四角筒状の外槽1の下部内側へ空気室2を設けて、その上部へ、下部熱処理室3を設ける。前記空気室2は前記外槽1の下部の三側壁へ、直角三角形の斜辺に相当する斜板4a、4b、4c(全体をいう場合は4とする)を設けて、斜板4と、外槽の隅部により断面三角形の空気室2a、2b、2cを連通して設け、前記下部熱処理室3と給気パイプ3aで連通させると共に、前記空気室2へ、二つの給送パイプ5、5の一端を連結し、給送パイプ5、5の他端には、ファン6、6を夫々設けて外界に開口し、この給送パイプ5、5の中間部には、バルブ7、7と、活性処理パイプ8、8とを介装する。前記活性処理パイプ8、8内には、永久磁石(例えば4000ガウス)を対向設置して、通過空気を磁化する。前記活性処理パイプ8、8中には、永久磁石の他に、遠赤外線発生鉱物(例えば電気石又は麦飯石など)を充填することもある。   An embodiment of the present invention will be described with reference to FIGS. 1 and 2. An air chamber 2 is provided inside a lower portion of a rectangular tubular outer tank 1, and a lower heat treatment chamber 3 is provided above the air chamber 2. The air chamber 2 is provided with swash plates 4a, 4b, 4c (4 in the whole case) corresponding to the hypotenuse of the right triangle on the three side walls at the bottom of the outer tub 1, Air chambers 2 a, 2 b, 2 c having a triangular cross section are communicated with each other at the corner of the tank, communicated by the lower heat treatment chamber 3 and the air supply pipe 3 a, and two supply pipes 5, 5 are connected to the air chamber 2. One end of the feed pipes 5 and 5 are connected to the other ends thereof, and fans 6 and 6 are provided at the other ends of the feed pipes 5 and 5 respectively, and are opened to the outside. The active processing pipes 8 and 8 are interposed. Permanent magnets (for example, 4000 gauss) are installed in the active processing pipes 8 and 8 so as to magnetize the passing air. In addition to permanent magnets, the active treatment pipes 8 and 8 may be filled with a far-infrared ray generating mineral (for example, tourmaline or barley stone).

前記下部熱処理室3の上部には、外槽1の内壁と間隙を設け、内筒9を遊嵌して上部熱処理室10を形成し、前記外槽1の頂板11へ投入口12を設け、該投入口12へ開閉蓋13を被冠する。   In the upper part of the lower heat treatment chamber 3, a gap is provided between the inner wall of the outer tub 1, the inner tube 9 is loosely fitted to form an upper heat treatment chamber 10, and an inlet 12 is provided in the top plate 11 of the outer tub 1, An opening / closing lid 13 is put on the inlet 12.

また前記頂板11へ円筒14を設置し、円筒14の上端部を浄煙槽15の一側に連結し、該浄煙槽15の他側へ煙突16を連設する。   A cylinder 14 is installed on the top plate 11, an upper end portion of the cylinder 14 is connected to one side of the smoke purification tank 15, and a chimney 16 is connected to the other side of the smoke purification tank 15.

前記浄煙槽15は、四周閉鎖して、直方体状の煙道を形成してあり、浄煙槽15の内部は複数の仕切板17、17を所定間隔で縦設し、排煙が屈曲流動する如く仕切板17、17の上部(頂板15a)と、水面19との間に排煙の通過間隙18、18を設ける。前記浄煙槽15の終端側に煙突16を設けて、この発明の熱処理炉25を完成したものである。   The smoke clarification tank 15 is closed four times to form a rectangular parallelepiped-shaped flue. Inside the smoke clarification tank 15, a plurality of partition plates 17 and 17 are provided vertically at predetermined intervals, and the flue gas bends and flows. As described above, smoke passing passages 18 and 18 are provided between the upper portions (top plate 15 a) of the partition plates 17 and 17 and the water surface 19. A chimney 16 is provided on the end side of the smoke purification tank 15 to complete the heat treatment furnace 25 of the present invention.

前記実施例において、この熱処理炉の使用状態を説明すると、廃棄物を入れた容器を持って階段21から踏板22に到り、開閉蓋13を開いて、前記廃棄物を投入口12から矢示23のように投入し(図1(a))、前記廃棄物の1/3程度になったならば、開閉蓋13を閉鎖する。次に、下部熱処理室3に通じる蓋24を開いて、点火した紙又は木を矢示26の方向へ差し入れて点火する。この場合に給気パイプ3aから永久磁石(麦飯石、電気石入り)で励起した空気が空気室を介して、下部熱処理室へ供給されるので、廃棄物が良く熱処理される。ついで火力給気を調節して、温度を350℃程度として、他の廃棄物も熱処理する。前記のようにして処理の結果、灰の深さが20cm〜30cmになったならば、開閉蓋13を開いて、新たな廃棄物を順次投入し、上部熱処理室に充満したならば、開閉蓋13を閉じる。このように、磁化空気を送りつつ低温度処理すれば、新しく充填した廃棄物は、下から順次処理される。前記処理により生じた排煙は矢示27、28のように上昇する煙と、矢示29、30のように下降する煙とに分けられる。この場合に上昇排煙として煙筒14を出た排煙は、浄煙槽15内を矢示31、32、33、34のように屈曲流動し、矢示20のように煙突16から外界へ排出される。   In the above embodiment, the state of use of the heat treatment furnace will be described. Holding the waste container, the staircase 21 reaches the tread 22, the open / close lid 13 is opened, and the waste is indicated by the arrow 12. 23 (FIG. 1 (a)), and when it becomes about 1/3 of the waste, the open / close lid 13 is closed. Next, the lid 24 leading to the lower heat treatment chamber 3 is opened, and the ignited paper or wood is inserted in the direction of the arrow 26 and ignited. In this case, since the air excited by the permanent magnet (with barley stone and tourmaline) is supplied from the air supply pipe 3a to the lower heat treatment chamber through the air chamber, the waste is well heat treated. Next, the thermal power supply is adjusted so that the temperature is about 350 ° C., and other wastes are also heat-treated. As a result of the treatment as described above, when the ash depth becomes 20 cm to 30 cm, the open / close lid 13 is opened, new waste is sequentially added, and when the upper heat treatment chamber is filled, the open / close lid is opened. 13 is closed. In this way, if the low temperature treatment is performed while sending magnetized air, the newly filled waste is sequentially treated from the bottom. The flue gas generated by the processing is divided into smoke rising as indicated by arrows 27 and 28 and smoke falling as indicated by arrows 29 and 30. In this case, the flue gas exiting the smoke cylinder 14 as rising flue gas bends and flows in the smoke purification tank 15 as indicated by arrows 31, 32, 33, and 34, and is discharged from the chimney 16 to the outside as indicated by arrow 20. Is done.

前記排煙は、屈曲流動中に、水面19と接触するので、水によっても浄化されると共に、大粒子は水中へ沈下し、水面との当接煙は、煙中の微粒子を捕えられ浄化されるので、煙突から出る排煙は外界放出できる程度まで浄化される。   The flue gas comes into contact with the water surface 19 during the bending flow and is also purified by water, and the large particles sink into the water, and the contact smoke with the water surface is trapped and purified by the fine particles in the smoke. Therefore, the smoke emitted from the chimney is purified to the extent that it can be released to the outside world.

前記において、給気は矢示35、35のように強制吸入され、活性処理パイプ8、8で活性化処理されると共に、バルブ7によって送気量が調整され(例えば1m/1分)、高温熱処理しないように調節される。前記ファン6は通常使用しないが、加圧給送を要する場合のみ使用される。 In the above, the air supply is forced inhalation as arrow 35, while being treated activated with active treatment pipes 8,8, the amount of air is adjusted by a valve 7 (e.g. 1 m 3/1 min), The temperature is adjusted so as not to be heat-treated. The fan 6 is not normally used, but is used only when pressurized feeding is required.

前記において浄煙槽15の上部には、太陽電池36が設置され、その電力は、コード37のようにファン6又はセンサーなどの電源として給電される。太陽の出ない時(例えば夜間)には、蓄電池を使用する。   In the above, the solar cell 36 is installed in the upper part of the smoke purification tank 15, and the electric power is fed as a power source for the fan 6 or a sensor like the cord 37. When the sun does not come out (for example, at night), a storage battery is used.

前記実施例は、比較的小型の熱処理炉(例えば一度に1000kg処理)について説明したが、熱処理室の構造、廃棄物の投入設備(例えば自動投入)及び浄煙装置の効率化などを行うことにより、処理能力を増大し(例えば1000kg〜10000kg)又は連続処理装置とすることもできる。   Although the said Example demonstrated the comparatively small heat processing furnace (for example, 1000 kg processing at once), by performing the structure of a heat processing chamber, the waste input equipment (for example, automatic input), and the efficiency of a smoke purifier, etc. , Increasing the processing capacity (eg 1000 kg to 10000 kg) or a continuous processing device.

前記処理能力の増大に伴い、これに対応する給送空気の活性化処理能力を増大させることは当然である。然し乍ら、給送空気の励起と、低温熱処理の維持は行うことが必要不可欠である。   As the processing capacity increases, it is natural to increase the supply processing capacity corresponding to this. However, it is essential to excite the feed air and maintain the low temperature heat treatment.

前記における低温処理の温度制御には、供給空気の量を制御して行うことができる。例えば、前記煙筒14の基部に温度センサー46をセットし、温度センサー46の出力を制御器47に入力させ、制御器47の出力を給送パイプ5のバルブ7(この場合には自動バルブにする)に指示して、開度を定めれば排気温度により、給気量を制御し、処理温度を制御することができる。   The temperature control of the low-temperature treatment in the above can be performed by controlling the amount of supply air. For example, the temperature sensor 46 is set at the base of the smoke cylinder 14, the output of the temperature sensor 46 is input to the controller 47, and the output of the controller 47 is the valve 7 of the feed pipe 5 (in this case, an automatic valve). ) And the opening degree is determined, the supply amount can be controlled by the exhaust temperature, and the processing temperature can be controlled.

前記のような自動バルブでない時には、温度を見てバルブを手動的に調節し、処理温度を決める。   When the automatic valve is not as described above, the processing temperature is determined by manually adjusting the valve by looking at the temperature.

前記実施例において、浄煙槽の内側上部に散水管を設置し、適宜散水させれば、通過煙を浄化することができる。前記散水を噴霧とすることもできる。   In the said Example, if a sprinkling pipe is installed in the inner upper part of a smoke-cleaning tank and it sprays suitably, passing smoke can be purified. The water spray may be sprayed.

この考案の他の実施例を図4について説明する。この実施例は、外槽40を円筒形としたもので、その他の形状構造、機能(装置)は実施例1とほぼ同様である。実施例2の場合には、空気室39を断面三角形の環状とし、浄煙槽41を半環状としたものである。   Another embodiment of the present invention will be described with reference to FIG. In this embodiment, the outer tub 40 is cylindrical, and the other shape structure and function (apparatus) are substantially the same as those in the first embodiment. In the case of Example 2, the air chamber 39 has an annular shape with a triangular cross section, and the smoke purification tank 41 has a semi-annular shape.

前記実施例2は、外槽40を円筒状にしたので、下部熱処理室3と、上部熱処理室10とはほぼ同一とすることができる。然し乍ら廃棄物投入口12は外槽40の頂板38の中央部に設けて開閉蓋13を被冠してある。従って浄煙槽41は、前後半円形(平面)41a、41aとして、一側を連結部41bで連結し、一方の半円形41aの一側下部へ円筒42を連結し、他方の半円形41bの一側上部へ煙突43を連結することも考えられる。   In the second embodiment, since the outer tub 40 is cylindrical, the lower heat treatment chamber 3 and the upper heat treatment chamber 10 can be made substantially the same. However, the waste inlet 12 is provided at the center of the top plate 38 of the outer tub 40 and is covered with the opening / closing lid 13. Accordingly, the smoke purification tank 41 is connected to one side by a connecting part 41b as front and rear half circles (planes) 41a and 41a, and the cylinder 42 is connected to one lower part of one semicircle 41a, and the other semicircle 41b It is also conceivable to connect the chimney 43 to the upper part on one side.

この場合には、廃棄物の投入を容易にする為に、投入シュート(図示してない)を設けることもできる。図中44はコード、45は太陽電池、48は下部熱処理室へ通じる蓋であって、給送パイプ5は実施例1と同一である。   In this case, an input chute (not shown) can be provided to facilitate the input of waste. In the figure, 44 is a cord, 45 is a solar cell, 48 is a lid leading to the lower heat treatment chamber, and the feed pipe 5 is the same as in the first embodiment.

(a)この考案の実施例の一部を破切した正面図、(b)同じく底面図。(A) The front view which broke off a part of Example of this invention, (b) Similarly bottom view. (a)同じく一部を省略した横断平面図、(b)同じく左側面図。(A) The cross-sectional top view which abbreviate | omitted one part, (b) The left side view similarly. (a)同じく平面図、(b)同じく右側面図。(A) Similarly top view, (b) Right side view. (a)同じく他の実施例の一部横断平面図、(b)同じく一部を破切した正面図、(c)同じく浄煙槽の平面図。(A) A partially cross-sectional plan view of another embodiment, (b) A front view in which a part is broken, and (c) A plan view of a smoke purification tank.

符号の説明Explanation of symbols

1 外槽
2 空気室
3 下部熱処理室
4a、4b、4c 斜板
5 給送パイプ
6 ファン
8 活性処理パイプ
9 内筒
10 上部熱処理室
11 頂板
12 投入口
13 開閉蓋
14 円筒
15 浄煙槽
16 煙突
17 仕切板
18 通過間隙
19 水面
20 煙突
25 熱処理炉
DESCRIPTION OF SYMBOLS 1 Outer tank 2 Air chamber 3 Lower heat processing chamber 4a, 4b, 4c Swash plate 5 Feeding pipe 6 Fan 8 Active processing pipe 9 Inner cylinder 10 Upper heat processing chamber 11 Top plate 12 Inlet 13 Opening lid 14 Cylinder 15 Smoke tank 16 Chimney 17 Partition plate 18 Passing gap 19 Water surface 20 Chimney 25 Heat treatment furnace

Claims (7)

外槽の下部内側へ、給気パイプを水平方向へ突設した下部熱処理室を設け、該下部熱処理室の上部へ、外槽と間隙を作って設けた内筒よりなる上部熱処理室を設けると共に、前記外槽の上部へ蓋板付きの廃棄物投入口と、煙筒とを設け、該煙筒は散水による浄煙槽の一側に連結し、該浄煙槽の他側に煙突を連結し、前記給気パイプは、前記外槽の底板と、下部熱処理室との間の空気室と連通させ、該空気室へ磁化空気の給送手段を連結したことを特徴とする低温熱処理炉。   A lower heat treatment chamber with an air supply pipe projecting in the horizontal direction is provided inside the lower portion of the outer tub, and an upper heat treatment chamber comprising an inner cylinder provided with a gap with the outer tub is provided above the lower heat treatment chamber. A waste inlet with a cover plate on the upper part of the outer tank, and a smoke cylinder, the smoke cylinder is connected to one side of the smoke purification tank by watering, and a chimney is connected to the other side of the smoke purification tank, The low temperature heat treatment furnace characterized in that the air supply pipe communicates with an air chamber between a bottom plate of the outer tub and a lower heat treatment chamber, and a magnetized air feeding means is connected to the air chamber. 外槽の下部内側へ、給気パイプを水平方向へ突設した下部熱処理室を設け、該下部熱処理室の上部へ、外槽と間隙を作って設けた内筒よりなる上部熱処理室を設けると共に、前記外槽の上部へ蓋板付きの廃棄物投入口と、煙筒とを設け、該煙筒は散水による浄煙槽の一側に連結し、該浄煙槽の他側に煙突を連結し、前記給気パイプは、前記外槽の底板と、下部熱処理室との間の空気室と連通させ、下部熱処理室と空気室との壁板は、少なくとも2つの対向壁又は全壁板を上向き斜板とし、前記空気室へ磁化空気の給送手段を連結したことを特徴とする低温熱処理炉。   A lower heat treatment chamber with an air supply pipe projecting horizontally is provided inside the lower portion of the outer tub, and an upper heat treatment chamber comprising an inner cylinder provided with a gap with the outer tub is provided above the lower heat treatment chamber. A waste inlet with a cover plate on the upper part of the outer tank, and a smoke cylinder, the smoke cylinder is connected to one side of the smoke purification tank by watering, and a chimney is connected to the other side of the smoke purification tank, The air supply pipe communicates with an air chamber between the bottom plate of the outer tub and the lower heat treatment chamber, and the wall plate between the lower heat treatment chamber and the air chamber has at least two opposing walls or all wall plates inclined upward. A low-temperature heat treatment furnace characterized in that a plate is used, and magnetized air feeding means is connected to the air chamber. 外槽の下部内側へ、給気パイプを水平方向へ突設した下部熱処理室を設け、該下部熱処理室の上部へ、外槽と間隙を作って設けた内筒よりなる上部熱処理室を設けると共に、前記外槽の上部へ蓋板付きの廃棄物投入口と、煙筒とを設け、該煙筒は散水による浄煙槽の一側に連結し、該浄煙槽は水槽の中へ、複数の仕切板を所定間隔に併設し、排煙が上下屈曲流動できるようにして、その他側に煙突を連結し、前記外槽の底板と、下部熱処理室との間に空気室を設け、下部熱処理室と空気室との壁板は、少なくとも2つの対向壁又は全壁板を上向き斜板とし、前記空気室へ磁化空気の給送手段を連結したことを特徴とする低温熱処理炉。   A lower heat treatment chamber with an air supply pipe projecting horizontally is provided inside the lower portion of the outer tub, and an upper heat treatment chamber comprising an inner cylinder provided with a gap with the outer tub is provided above the lower heat treatment chamber. A waste inlet with a cover plate on the upper part of the outer tub and a smoke cylinder, and the smoke cylinder is connected to one side of the water purification tank by watering, and the smoke tank is divided into a plurality of partitions. A plate is provided at a predetermined interval so that the flue gas can be bent upward and downward, a chimney is connected to the other side, an air chamber is provided between the bottom plate of the outer tank and the lower heat treatment chamber, A low temperature heat treatment furnace characterized in that at least two opposing walls or all wall plates are upwardly facing swash plates, and a magnetized air feeding means is connected to the air chamber. 給送手段は、給送パイプの外気の吸入側へファンを設置すると共に、前記給送パイプの中間部へ、永久磁石内蔵の活性処理パイプと、バルブとを直列に介装したことを特徴とする請求項1、2又は3記載の低温熱処理炉。   The feeding means is characterized in that a fan is installed on the outside suction side of the feeding pipe, and an active processing pipe with a built-in permanent magnet and a valve are interposed in series in the middle of the feeding pipe. The low-temperature heat treatment furnace according to claim 1, 2, or 3. 給気パイプは、下部熱処理室と空気室とを連通させると共に、下部熱処理室へ上下多段に、かつ中央部へ達しない長さに水平方向に突設したことを特徴とする請求項1、2又は3記載の低温熱処理炉。   The air supply pipe communicates between the lower heat treatment chamber and the air chamber, and is provided in the lower heat treatment chamber so as to protrude vertically in a multistage manner and not to reach the center portion. Or the low-temperature heat treatment furnace as described in 3. 熱処理室に温度センサーを設け、該温度センサーの出力を、外槽上部の温度計と接続したことを特徴とする請求項1、2又は3記載の低温熱処理炉。   4. A low-temperature heat treatment furnace according to claim 1, wherein a temperature sensor is provided in the heat treatment chamber, and an output of the temperature sensor is connected to a thermometer at the upper part of the outer tub. 外気の給送パイプに介装するバルブは自動開閉バルブとし、該自動開閉バルブの制御器へ、温度センサーの出力を連結することとした請求項6記載の低温熱処理炉。   The low-temperature heat treatment furnace according to claim 6, wherein the valve interposed in the outside air supply pipe is an automatic opening / closing valve, and the output of the temperature sensor is connected to the controller of the automatic opening / closing valve.
JP2006002612U 2006-04-07 2006-04-07 Low temperature heat treatment furnace Expired - Fee Related JP3122682U (en)

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JP2010155231A (en) * 2008-12-26 2010-07-15 Shoichi Yamamoto Method of making cold decomposition treatment of material to be treated and device using this method
JP2012013369A (en) * 2010-07-02 2012-01-19 Iwamoto:Kk Waste treatment machine
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WO2007116598A1 (en) * 2006-04-07 2007-10-18 Abe, Yumi Method of low-temperature heat treatment of waste and apparatus therefor
JP2010155231A (en) * 2008-12-26 2010-07-15 Shoichi Yamamoto Method of making cold decomposition treatment of material to be treated and device using this method
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JP2015163833A (en) * 2014-01-28 2015-09-10 株式会社五常 Low-temperature pyrolysis treatment furnace, low-temperature pyrolysis treatment system, and low-temperature pyrolysis treatment method

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