JP2007216204A - Pyrolysis apparatus for waste product - Google Patents

Pyrolysis apparatus for waste product Download PDF

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JP2007216204A
JP2007216204A JP2006073495A JP2006073495A JP2007216204A JP 2007216204 A JP2007216204 A JP 2007216204A JP 2006073495 A JP2006073495 A JP 2006073495A JP 2006073495 A JP2006073495 A JP 2006073495A JP 2007216204 A JP2007216204 A JP 2007216204A
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chamber
waste
waste product
pyrolysis
gas
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Ruiko Aoyanagi
るい子 青柳
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a pyrolysis apparatus for a waste product for solving the problem that the treatment of a waste product, presently classified into either incineration or reclamation with recycling also recommended, cannot realize satisfactory recycling in terms of cost owing to a restriction in the type of waste product, concerns environmental destruction by dioxin or the like caused by disposal in an incinerator although incineration disposal is mainly generally performed for a medical waste product such as an infectious waste product, and cannot be expected for a significant improvement in reclamation disposal owing to a reduction of disposal sites, environmental access and the like. <P>SOLUTION: The pyrolysis apparatus for the waste product is provided comprising a high frequency sterilizing chamber, a crushing chamber, a drying chamber, a dechlorination chamber, a pyrolysis carbonization chamber and a cooling chamber irrespective of the kind of a waste product, wherein pyrolysis of a waste product by heated steam is automated, a hydrocarbon oil or the like generated by pyrolysis is reused as an auxiliary fuel for a heated steam generating burner, a chlorine gas is made harmless by heated steam treatment, a clean gas is produced in a condensing tower, and external environmental pollution is not produced and residue is not generated in a waste disposal process, whereby the apparatus can contribute to environment. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は廃棄物処理における、環境の汚染、残渣の減少、又廃棄物のリサイクル率の向上等、廃棄物処理に関する装置である。The present invention is an apparatus related to waste processing, such as environmental pollution, reduction of residues, and improvement of waste recycling rate in waste processing.

従来廃棄物処理において数多くの処理が為されているが、環境汚染、残渣の処理、埋め立て処分場の減少等、地球環境に著しい影響を与えている。自然環境で消滅しないプラスチック等の科学物質は多くなる一方である。しかし科学物質等の処理は埋め立てか焼却処理が一般的で在るが、土壌汚染やダイオキシン等の環境汚染を引き起こし、付近住民の生活及び動植物の生態系に及ぼす重大な影響が危惧されている。Conventionally, many treatments are performed in waste treatment, but it has a significant impact on the global environment, such as environmental pollution, residue treatment, and reduction of landfill sites. Scientific materials such as plastics that do not disappear in the natural environment are increasing. However, the treatment of chemical substances is generally landfilled or incinerated, but it causes environmental pollution such as soil contamination and dioxin, and there are concerns about serious impacts on the lives of nearby residents and the ecosystems of animals and plants.

発明が解決しようとする課題は、廃棄物を熱分解処理する工程で排出される、排ガスを外部に排出する事無く、排ガスを再還流させ熱分解処理用の熱源等に使用、その他のガスは分別、分留し科学原材料として再利用する。並びに熱分解処理後の炭化物は土壌の浄化及び水、空気等の浄化等に使用する。The problem to be solved by the invention is that the waste is exhausted in the process of pyrolysis treatment, the exhaust gas is recirculated without being exhausted to the outside, and used as a heat source for pyrolysis treatment. Separation, fractionation and reuse as scientific raw materials. In addition, the pyrolyzed carbide is used for soil purification, water, air purification, and the like.

そこで本発明の目的は廃棄物熱分解処理装置を金属又はコンクリート並びに硬質樹脂によって形成したユニットに、廃棄物が移動し各ボックスの密閉空間の中で高周波殺菌処理、破砕、乾燥、脱塩素、ガス化、炭化、冷却等の各処理がなされる。又熱分解処理工程で排出される炭化水素油等の排出ガスは還流機構により再使用し外部環境に排気される事は無い。Therefore, the object of the present invention is to dispose of the waste pyrolysis apparatus to a unit formed of metal or concrete and hard resin, and the waste is transferred to a high-frequency sterilization treatment, crushing, drying, dechlorination, gas in the sealed space of each box. Each process such as carbonization, carbonization and cooling is performed. Further, exhaust gas such as hydrocarbon oil discharged in the pyrolysis process is reused by the reflux mechanism and is not exhausted to the external environment.

前記目的を達成して課題を達成するため本発明に係る廃棄物熱分解処理装置は廃棄物の種類にかかわらず処理できる。高周波放射装置によって、滅菌及び殺菌工程を設け、医療系廃棄物を処理出来る。食物残渣及プラスチック類又液体等も熱分解する事により処理出来る。熱分解処理工程で発生する排ガスは分留装置で分留後再利用が可能である。熱分解後の炭化廃棄物は利用用途が多く環境の改善等に幅広く利用できる。In order to achieve the above object and achieve the object, the waste pyrolysis apparatus according to the present invention can treat regardless of the kind of waste. A high-frequency radiation device can provide sterilization and sterilization processes to treat medical waste. Food residues and plastics or liquids can also be treated by pyrolysis. The exhaust gas generated in the pyrolysis process can be reused after fractional distillation by a fractionator. Carbonized waste after pyrolysis has many uses and can be widely used to improve the environment.

廃棄物の処理において数多くの処理方法が存在するが、大きく分類すると埋め立てか焼却が処理の80パーセント以上を締め大きな改善は無い、本発明は熱分解処理によって油化及び炭化する。熱分解処理後の廃棄物を再利用する。炭化廃棄物は多孔質性の特色を生かし、水の浄化作用等の環境改善、熱分解工程で排出される炭化水素油の再利用と、一連の処理工程で外気に放出する排ガスは無い。従って埋め立て処分場の延命と焼却炉での焼却が無く、外気排出ガスの環境汚染が無い環境にやさしい廃棄物熱分解装置である。There are a number of treatment methods in the treatment of waste, but broadly speaking, landfill or incineration is more than 80% of the treatment and there is no significant improvement. The present invention is liquefied and carbonized by pyrolysis treatment. Recycle waste after pyrolysis. Carbonized waste takes advantage of the characteristics of porosity, and there is no exhaust gas that is released into the outside air through a series of treatment steps and environmental improvement such as water purification, recycling of hydrocarbon oil discharged in the thermal decomposition process. Therefore, it is an environmentally friendly waste pyrolysis device that does not prolong the life of the landfill site and is not incinerated in the incinerator, and is free from the environmental pollution of the outside air exhaust gas.

以下、添付図面に基づいて本発明の実施例を説明する。
図1は、本発明に係る廃棄物炭化処理装置の一例を示す物である。この処理装置はコンクリート又は金属又は樹脂で形成し、5の投入口から入った廃棄物は10の搬送傾斜ベルトにて搬送される。10の搬送途中に11の高周波発生器で発生した高周波が廃棄物に照射し滅菌処理をする。滅菌処理後の廃棄物は15の破砕装置で破砕され20のフレーク充填室に搬入される。
Embodiments of the present invention will be described below with reference to the accompanying drawings.
FIG. 1 shows an example of a waste carbonization apparatus according to the present invention. This processing apparatus is made of concrete, metal, or resin, and waste that has entered from the 5 inlets is transported by 10 transporting inclined belts. During the transfer of 10, the high frequency generated by the 11 high frequency generator irradiates the waste and sterilizes it. The waste after sterilization is crushed by 15 crushing apparatuses and carried into 20 flake filling chambers.

20の充填室にセットされているフレーク搬送用コンテナ40にフレークが投入される。21の乾燥室前面ゲート29が上部に上がり搬送コンテナ40が21の乾燥室に移動する。40が21の定位置に移動後21の前面ゲートが下がり21の乾燥室が完全密封する。密封後乾燥室21の床面に設置されて入る30の電気ヒーターが加熱する。又乾燥を促進するため90の加熱蒸気発生装置で作られた加熱蒸気が31の加熱蒸気ヒーターに流入し40内部のフレークが乾燥処理される。Flakes are thrown into the container 40 for flake conveyance set in 20 filling chambers. The front gate 29 of the drying chamber 21 rises upward, and the transfer container 40 moves to the drying chamber 21. After 40 moves to the fixed position of 21, the front gate of 21 is lowered and the drying chamber of 21 is completely sealed. After sealing, 30 electric heaters installed on the floor surface of the drying chamber 21 are heated. In order to accelerate drying, the heating steam produced by the 90 heating steam generator flows into the 31 heating steam heater, and the flakes inside 40 are dried.

21の乾燥処理後搬送用コンテナ40が22の脱塩素室に送られる。この移動時21の背面ゲートが開き22の定位置に移動後閉まる。22が密閉後60の窒素ガス発生装置で作られた窒素ガスが62、63、65を通り22の脱塩素室に充満し22の室内の空気を50の塩素ガス回収回路に押し込む窒素ガスとの置き換えは21から22、23、24、25の各室もその作業工程ごとに行われる。この一連の流れで22の室内は窒素ガスで充たされ発火燃焼しない空間となる。22の室内にセットされている30の電気ヒーターと31の加熱蒸気ヒーターが加熱され40の中のフレークが熱分解する、この時点で塩素ガスが発生し、この塩素ガスを53で回収50のスクラバーで水に接触させ回収する。After the drying process 21, the transfer container 40 is sent to the dechlorination chamber 22. During this movement, the rear gate 21 opens and moves to a fixed position 22 and then closes. The nitrogen gas produced by the nitrogen gas generator 60 after the 22 is sealed passes through the 62, 63, 65 to fill the 22 dechlorination chamber and push the air in the chamber 22 into the 50 chlorine gas recovery circuit. Replacement is also performed in each chamber from 21 to 22, 23, 24, and 25. With this series of flows, the room 22 is filled with nitrogen gas and becomes a space that does not ignite and burn. 30 electric heaters set in 22 rooms and 31 heating steam heaters are heated, and flakes in 40 are pyrolyzed. At this point, chlorine gas is generated, and this chlorine gas is recovered in 53. 50 scrubbers Contact with water to recover.

炭化室23、24、25に搬入されたフレークは30の電気ヒーターと31の加熱蒸気ヒーターによって過熱されフレークを熱分解炭化させる。炭化工程で発生する炭化水素油は70の炭化水冷却器に入り73炭化水素油回収回路を通り75炭化水素分留装置で分留され77を通り80に貯蔵される。The flakes carried into the carbonization chambers 23, 24, and 25 are overheated by 30 electric heaters and 31 heating steam heaters to pyrolytically carbonize the flakes. The hydrocarbon oil generated in the carbonization process enters 70 hydrocarbon coolers, passes through 73 hydrocarbon oil recovery circuit, is fractionated by 75 hydrocarbon fractionator, and is stored in 80 through 77.

80に貯蔵された各炭化水素油は85、86、87の回路を通り90の熱風発生器の補助バーナー91で90の加熱蒸気発生熱源の補助燃料としてリサイクルする。Each hydrocarbon oil stored in 80 passes through circuits 85, 86, and 87 and is recycled as an auxiliary fuel for 90 heating steam generating heat sources by an auxiliary burner 91 of 90 hot air generators.

又フレーク搬送コンテナは35のコンテナリターンコンベアで移動し、コンテナ90度旋回装置38によって旋回20に戻る。又35を移動途中で39のコンテナは90度反転装置によりコンテナ内部のフレークを受け入れコンテナに空ける。The flake carrier container moves on the container return conveyor 35 and returns to the turn 20 by the container 90-degree turning device 38. While moving 35, the container 39 receives flakes inside the container by the 90-degree reversing device and empties the container.

冷却室26、27、28の各室は45の熱交換器によって冷却される、この冷却室も他の21、22、23、24、25の室同様ゲートの開閉が前後別々に開閉し各室は完全密閉の空間となる。Each of the cooling chambers 26, 27, and 28 is cooled by 45 heat exchangers, and this cooling chamber is also opened and closed separately in the front and rear as in the other 21, 22, 23, 24, and 25 chambers. Becomes a completely enclosed space.

図2は本発明に使用する炭化室の一例である。
各室のゲート29はくさび形形状をしており40の移動に合せて前面ゲートが開いた時背面ゲートは閉じる、これの繰り返しによって各室21、22、23、24、25、26、27は密閉される。又40のコンテナが移動する時21、22、23、24、25の各室に窒素ガスの補充が自動供給される。
FIG. 2 is an example of a carbonization chamber used in the present invention.
The gate 29 of each chamber has a wedge shape, and when the front gate is opened in accordance with the movement of the 40, the rear gate is closed. By repeating this, each chamber 21, 22, 23, 24, 25, 26, 27 is Sealed. When 40 containers are moved, replenishment of nitrogen gas is automatically supplied to the chambers 21, 22, 23, 24 and 25.

冷却室26、27、28、は水を循環させ冷却する。各室の床面及び壁面に水の循環装置を設け熱を吸収する。熱交換する冷水は49の冷却水デリバリー管を通り各室の熱交換器に入り熱交換する。熱交換後の温水は冷却水リターン回路48を通り45の熱交換器に入り冷却される。The cooling chambers 26, 27, and 28 circulate and cool water. A water circulation device is installed on the floor and wall of each room to absorb heat. The cold water to be heat exchanged passes through the 49 cooling water delivery pipes and enters the heat exchangers of the respective chambers to exchange heat. The hot water after the heat exchange passes through the cooling water return circuit 48 and enters the heat exchanger 45 to be cooled.

図3は本発明に使用する加熱蒸気及び冷却水回路の一例である。
加熱蒸気は各室の加熱蒸気ヒーターを通過後96の加熱蒸気排出回路を通り97の凝縮塔において凝縮水とクリーンガスに分離排出する。又冷却水リターンで熱交換器45に流入する冷却水は、凝縮水と混合され循環する。
FIG. 3 is an example of a heating steam and cooling water circuit used in the present invention.
The heated steam passes through a heated steam heater in each chamber, passes through a heated steam discharge circuit 96, and is separated and discharged into condensed water and clean gas in a 97 condensing tower. The cooling water flowing into the heat exchanger 45 by the cooling water return is mixed with the condensed water and circulated.

以上説明したように本発明に係る廃棄物熱分解処理装置は、廃棄物の種類を問わず処理でき、ダイオキシン等の排出ガスや埋立残渣の減少など地球環境に配慮し、並びに廃棄物の再利用、環境汚染の防止又廃棄物の炭化による水及び空気の浄化など環境に貢献する装置である。As described above, the waste pyrolysis apparatus according to the present invention can treat any kind of waste, considers the global environment such as reduction of exhaust gas such as dioxin and landfill residue, and reuses waste. It is a device that contributes to the environment by preventing environmental pollution and purifying water and air by carbonizing waste.

本発明に係る廃棄物熱分解処理装置の一例を示す斜視図である。It is a perspective view which shows an example of the waste pyrolysis processing apparatus which concerns on this invention. 本発明に係る廃棄物熱分解処理装置の一例を示す断面図である。It is sectional drawing which shows an example of the waste pyrolysis processing apparatus which concerns on this invention. 本発明に係る廃棄物熱分解処理装置の一例を示す斜視図である。It is a perspective view which shows an example of the waste pyrolysis processing apparatus which concerns on this invention.

符号の説明Explanation of symbols

5 廃棄物投入口
10 搬送傾斜コンベア
11 高周波発生器
15 破砕装置
20 フレーク充填室
21 乾燥室
22 脱塩素室
23 炭化室1
24 炭化室2
25 炭化室3
26 冷却室1
27 冷却室2
28 冷却室3
29 開閉ゲート
30 電機ヒーター
31 加熱蒸気ヒーター
35 コンテナリターンコンベア
36 コンテナ搬送チェーンコンベア
38 コンテナ90°旋回装置
39 コンテナ90°反転装置
40 フレーク搬送用コンテナ
45 熱交換器
47 無害温水取り出し口
48 冷却水リターン回路
49 冷却水デリバリー回路
50 スクラバー
53 塩素ガス回収回路
60 窒素ガス発生装置
62 窒素ガス供給回路1
63 窒素ガス貯蔵タンク
65 窒素ガス供給回路2
70 炭化水素冷却塔
73 炭化水素油回路1
75 炭化水素分留装置
77 分離後炭化水素油回路
80 炭化水素油貯蔵タンク
85 重質油供給回路
86 中質油供給回路
87 軽質油供給回路
90 加熱蒸気発生装置
91 補助バーナー
95 加熱蒸気供給回路
96 加熱蒸気排出回路
97 凝縮塔
98 凝縮水
99 クリーンガス廃棄塔
5 Waste input 10 Conveying inclined conveyor 11 High-frequency generator 15 Crushing device 20 Flake filling chamber 21 Drying chamber 22 Dechlorination chamber 23 Carbonization chamber 1
24 Carbonization chamber 2
25 Carbonization chamber 3
26 Cooling chamber 1
27 Cooling chamber 2
28 Cooling chamber 3
29 Opening / Closing Gate 30 Electric Heater 31 Heating Steam Heater 35 Container Return Conveyor 36 Container Transport Chain Conveyor 38 Container 90 ° Swivel Device 39 Container 90 ° Inversion Device 40 Flakes Transport Container 45 Heat Exchanger 47 Harmless Hot Water Extraction Port 48 Cooling Water Return Circuit 49 Cooling water delivery circuit 50 Scrubber 53 Chlorine gas recovery circuit 60 Nitrogen gas generator 62 Nitrogen gas supply circuit 1
63 Nitrogen gas storage tank 65 Nitrogen gas supply circuit 2
70 Hydrocarbon cooling tower 73 Hydrocarbon oil circuit 1
75 Hydrocarbon fractionator 77 Hydrocarbon oil circuit 80 after separation Hydrocarbon oil storage tank 85 Heavy oil supply circuit 86 Medium oil supply circuit 87 Light oil supply circuit 90 Heating steam generator 91 Auxiliary burner 95 Heating steam supply circuit 96 Heated steam discharge circuit 97 Condensing tower 98 Condensed water 99 Clean gas disposal tower

Claims (6)

廃棄物の種類にかかわらず殺菌、分別を自動処理し低温度で全ての原材料を炭化できる炭化装置。A carbonizer that can automatically disinfect and sort all raw materials at low temperatures regardless of the type of waste. 廃棄物の投入時投入ゲートが開口し、投入後ゲートを閉鎖、ゲート封鎖後、高周波発生装置で廃棄物を滅菌、滅菌室から破砕室への移動後、回転破砕刃にて破砕、破砕完了後下部のゲートが開口し原材料を下部移動装置に落下移動させる一連の装置。When the waste is input, the input gate opens. After the input, the gate is closed. After the gate is closed, the waste is sterilized with a high-frequency generator. After moving from the sterilization chamber to the crushing chamber, crushing with the rotary crushing blade and crushing is completed. A series of devices that open the lower gate and move the raw material to the lower moving device. 水分量の多い廃棄物を乾燥、滅菌する加熱蒸気発生供給装置。Heated steam generation and supply device that dries and sterilizes waste with high water content. 廃棄物が炭化する工程で排出する高温ガスを外部環境に排気しない、ガス循環とガスの再利用をするガス分留、分別循環させる一連の装置。A series of devices that do not exhaust the high-temperature gas discharged in the process of carbonizing waste to the external environment, perform gas fractionation and recycle the gas, and recycle the gas. 再利用するガスの供給を受け稼動する燃焼バーナーと分別ガス供給装置。Combustion burner and fractionated gas supply device that operates with the supply of gas to be reused. ゲートの開閉によって個室を形成し、その各個室が移動されてくる原材料を滅菌、破砕、乾燥、炭化、冷却、と一連の処理工程を継続的に処理できる移動自動装置。A mobile automatic device that can form a single chamber by opening and closing the gate and continuously process a series of processing steps such as sterilization, crushing, drying, carbonization, and cooling of the raw material to which each chamber is moved.
JP2006073495A 2006-02-17 2006-02-17 Pyrolysis apparatus for waste product Pending JP2007216204A (en)

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Cited By (6)

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KR100868725B1 (en) 2007-10-05 2008-11-13 한국생산기술연구원 Process for environmentally friendly treatment of wastes and production of clean syn gas therefrom
CN103624059A (en) * 2012-08-22 2014-03-12 黄广禧 House refuse splitting decomposition processing technological processes
CN103624055A (en) * 2012-08-22 2014-03-12 黄广禧 Method for inhibiting generation of dioxin through mixed cracking of straw and household garbage
CN110014025A (en) * 2019-04-22 2019-07-16 东营方塘环保科技有限公司 Community medicine waste number interconnects recovery and processing system
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100868725B1 (en) 2007-10-05 2008-11-13 한국생산기술연구원 Process for environmentally friendly treatment of wastes and production of clean syn gas therefrom
CN103624059A (en) * 2012-08-22 2014-03-12 黄广禧 House refuse splitting decomposition processing technological processes
CN103624055A (en) * 2012-08-22 2014-03-12 黄广禧 Method for inhibiting generation of dioxin through mixed cracking of straw and household garbage
CN110014025A (en) * 2019-04-22 2019-07-16 东营方塘环保科技有限公司 Community medicine waste number interconnects recovery and processing system
CN111530886A (en) * 2020-05-04 2020-08-14 陈红霞 Water-based color paste raw material recycling and pretreating device
CN114101253A (en) * 2021-11-16 2022-03-01 长葛市人民医院 Isolatable medical waste treatment recycling bin disinfection equipment

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