JP2002088372A - Method for utilizing organic waste - Google Patents

Method for utilizing organic waste

Info

Publication number
JP2002088372A
JP2002088372A JP2000284609A JP2000284609A JP2002088372A JP 2002088372 A JP2002088372 A JP 2002088372A JP 2000284609 A JP2000284609 A JP 2000284609A JP 2000284609 A JP2000284609 A JP 2000284609A JP 2002088372 A JP2002088372 A JP 2002088372A
Authority
JP
Japan
Prior art keywords
organic waste
combustible gas
condensate
heat source
utilizing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2000284609A
Other languages
Japanese (ja)
Inventor
Kiyonori Kida
清則 喜田
Kinzo Okazaki
金造 岡崎
Shizuo Hayashi
静男 林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP2000284609A priority Critical patent/JP2002088372A/en
Publication of JP2002088372A publication Critical patent/JP2002088372A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics
    • 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
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Industrial Gases (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Coke Industry (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

PROBLEM TO BE SOLVED: To utilize a thermal decomposition gas recovered by thermally decomposing an organic waste in an oxygen-free atmosphere and a nonvolatile residue as a heat source for heating and eliminate the formation of dioxins in consequence of combustion. SOLUTION: The organic waste 1 is thermally decomposed in an oxygen-free state to produce a combustible gas, a condensate and a carbonized material, which are then subjected to dechlorinating treatments 3 and 4 and subsequently utilized as the heat source for uses utilizing the heat of combustion.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、ポリ塩化ビニー
ルなどの有機性廃棄物を熱分解して得られる生成物を暖
房等の熱源として利用する有機性廃棄物の利用方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for utilizing organic waste, which uses a product obtained by thermally decomposing organic waste such as polyvinyl chloride as a heat source for heating or the like.

【0002】[0002]

【従来の技術】ポリ塩化ビニール、ポリエチレンなどの
塩素化合物を含む有機性廃棄物は、不燃性ごみとして回
収され、それらの処理方法としては、ダイオキシンが発
生しないように高温(1200℃以上)の温度で燃焼し
て廃棄する。または、ダイオキシンが生成しないように
無酸素雰囲気内で加熱して熱分解ガスと、不揮発性残渣
を回収することが特開平11−226542号公報に開
示されている。
2. Description of the Related Art Organic waste containing chlorine compounds such as polyvinyl chloride and polyethylene is recovered as non-combustible waste, and the method of treating the waste is a high temperature (1200 ° C. or higher) so that dioxin is not generated. Burn and discard. Alternatively, JP-A-11-226542 discloses that a pyrolysis gas and a non-volatile residue are recovered by heating in an oxygen-free atmosphere so that dioxin is not generated.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、従来の
処理方法のうち1200℃以上で燃焼する方法は低温域
で燃焼中に発生するダイオキシンを分解することができ
るので、今日社会的な問題になっているダイオキシンか
ら開放される優れた方法ではあるが、1200℃以上の
高温で大量の有機性廃棄物を処理すること、または低温
処理で発生したダイオキシンを含む排ガスを1200℃
に加熱することは大量のエネルギを必要とすることから
実設備として稼動するには問題が多い。
However, among the conventional treatment methods, the method of burning at 1200 ° C. or higher can decompose dioxin generated during combustion in a low temperature range, and has become a social problem today. Although it is an excellent method of releasing dioxins, it is possible to treat a large amount of organic waste at a high temperature of 1200 ° C. or higher, or to discharge exhaust gas containing dioxin generated at a low temperature of 1200 ° C.
Heating a large amount of energy requires a large amount of energy, so that there are many problems in operating as an actual facility.

【0004】また、無酸素雰囲気で熱分解して熱分解ガ
ス、および不揮発性残渣を回収する方法についても回収
しただけでは熱分解ガス、および不揮発性残渣の後処理
に問題が残る。この発明は上記課題を解決するためにな
されたもので、その目的とするところは、有機性廃棄物
を無酸素雰囲気で熱分解して回収した熱分解ガス、およ
び不揮発性残渣を暖房用の熱源として利用するととも
に、燃焼に伴うダイオキシンの発生を無くした有機性廃
棄物の利用方法を提供することにある。
[0004] Further, with respect to a method of recovering a pyrolysis gas and a non-volatile residue by pyrolysis in an oxygen-free atmosphere, a problem remains in the post-treatment of the pyrolysis gas and the non-volatile residue only by recovering the same. The present invention has been made in order to solve the above-mentioned problems, and has as its object to provide a pyrolysis gas obtained by thermally decomposing organic waste in an oxygen-free atmosphere, and a non-volatile residue to be used as a heat source for heating. Another object of the present invention is to provide a method of using organic waste, which eliminates generation of dioxin due to combustion.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に請求項1記載の発明は、有機性廃棄物を無酸素状態で
熱分解して、可燃ガス、凝縮液、および炭化物を生成
し、該可燃ガス、および凝縮液、炭化物を脱塩素処理し
た後、暖房用の熱源として利用することを特徴とする。
According to the first aspect of the present invention, an organic waste is thermally decomposed in an oxygen-free state to produce a combustible gas, a condensate, and a carbide. The combustible gas, the condensate, and the carbide are dechlorinated and then used as a heat source for heating.

【0006】また、請求項2の発明は、請求項1記載の
有機性廃棄物の利用方法において、有機性廃棄物を熱分
解するする装置は、開閉可能な蓋、および可燃ガス引出
し口を有し、内部を不活性ガス雰囲気に保持する密閉式
の加熱室と、該加熱室を外側から誘導加熱する誘導コイ
ルとで構成することを特徴とする。また、請求項3の発
明は、請求項1記載の有機性廃棄物の利用方法におい
て、有機性廃棄物の熱分解は間欠操業とし、熱分解中に
発せする可燃ガスは即時熱源として利用し、凝縮液、お
よび炭化物は熱分解停止中に熱源として利用して熱源の
供給が終日連続するようにしたことを特徴とする。ま
た、請求項4の発明は、請求項1ないし請求項3のいず
れかに記載の有機性廃棄物の利用方法において、有機性
廃棄物を熱分解して得られる可燃ガスを回収する際に、
可燃ガス中に含有される塩素を除去する脱塩処理を行
い、脱塩後の可燃ガスをアキュームレータで平均化して
後段に供給するようにしたことを特徴とする。また、請
求項5の発明は、請求項1または請求項4に記載の有機
性廃棄物からの利用方法において、有機性廃棄物を熱分
解して得られる凝縮液を貯留タンクに回収する際に、凝
縮液中に含有される塩素を除去する脱塩処理を行うこと
を特徴とする。
According to a second aspect of the present invention, in the method for utilizing organic waste according to the first aspect, the apparatus for thermally decomposing the organic waste has an openable / closable lid and a combustible gas outlet. Further, it is characterized by comprising a closed-type heating chamber for holding the inside in an inert gas atmosphere, and an induction coil for induction-heating the heating chamber from the outside. The invention according to claim 3 is the method for utilizing organic waste according to claim 1, wherein the thermal decomposition of the organic waste is an intermittent operation, and the combustible gas generated during the thermal decomposition is used as an immediate heat source; The condensate and the carbide are used as a heat source during the stop of the thermal decomposition so that the supply of the heat source is continuously performed throughout the day. According to a fourth aspect of the present invention, in the method for utilizing an organic waste according to any one of the first to third aspects, when recovering a combustible gas obtained by thermally decomposing the organic waste,
A desalination treatment for removing chlorine contained in the combustible gas is performed, and the combustible gas after desalination is averaged by an accumulator and supplied to a subsequent stage. According to a fifth aspect of the present invention, in the method of utilizing an organic waste according to the first or fourth aspect, the condensate obtained by thermally decomposing the organic waste is collected in a storage tank. And a desalination treatment for removing chlorine contained in the condensate.

【0007】上記請求項1〜5の構成により、無酸素雰
囲気で有機性廃棄物を熱分解して得られた可燃ガスは、
酸素と触れる前に、苛性ソーダなどのアルカリ性液で可
燃ガス中に含まれる塩素を無害な化合物になるように中
和する脱塩素処理を行い、また凝縮液も同様のアルカリ
性液と混合して凝縮液中の塩素を処理する脱塩素処理と
処理後の油水分離処理とにより含有塩素を除去して、そ
れらを燃焼させてもダイオキシンが発生しない燃料とし
て利用することが可能になる。また、上記有機性廃棄物
を熱分解する操業は夜間電力を使用して行い、操業中に
発生し脱塩素処理した可燃ガスは即時熱源として利用
し、脱塩素処理した凝縮液と、炭化物は有機性廃棄物の
熱分解操業の停止中に熱源として使用することにより、
安価なランニングコストで終日連続して熱源を供給する
ことが可能になる。なお、処理中における可燃ガスの発
生は一様ではないのでアキュームレータを通して均一に
排出することが望ましい。また、可燃ガスによる熱エネ
ルギが不足する場合は、有機性廃棄物の熱分解する操業
中であっても、凝縮液、もしくは炭化物を熱源として併
用することにより終日の熱源供給量を平均化することが
可能になる。
[0007] According to the constitution of the first to fifth aspects, the combustible gas obtained by thermally decomposing the organic waste in an oxygen-free atmosphere,
Before contacting with oxygen, dechlorination is performed to neutralize chlorine contained in combustible gas into an harmless compound with an alkaline liquid such as caustic soda, and condensate is mixed with a similar alkaline liquid to form condensate. The chlorine contained is removed by the dechlorination treatment for treating the chlorine therein and the oil-water separation treatment after the treatment, and it can be used as a fuel that does not generate dioxin even if it is burned. In addition, the operation to pyrolyze the organic waste is performed using nighttime electric power, the combustible gas generated during the operation and dechlorinated is used as an immediate heat source, and the dechlorinated condensate and the carbide are converted to organic. By using as a heat source during the shutdown of pyrolysis of municipal waste,
It becomes possible to supply a heat source continuously all day at a low running cost. Since the generation of combustible gas during the treatment is not uniform, it is desirable to uniformly discharge the gas through the accumulator. Also, if the heat energy from the combustible gas is insufficient, even during the operation of thermal decomposition of organic waste, use the condensate or carbide as a heat source to average the amount of heat source supplied throughout the day. Becomes possible.

【0008】さらに凝縮液および炭化物は、タンクある
いは容器等に詰めれば遠地への輸送が可能となるので、
遠地の施設の熱源として使用することが可能になる。ポ
リ塩化ビニール、ポリエチレンなどの塩素化合物を含む
有機性廃棄物は、実験の結果では無酸素雰囲気内で熱分
解すると熱分解温度にもよるが、10〜15%の炭化物
と、30〜65%の凝縮液と、残りが可燃ガスとにな
る。これらの比率は熱分解温度が低い程凝縮液が多く生
成される傾向にある。また、各生成物の保有エネルギは
炭化物が約5000Kcal/Kg,凝縮液は約100
00Kcal/Kg、可燃ガスは約7000Kcal/
Kgであった。このことは有機性廃棄物からの生成物を
熱源として利用することが可能であることを示してい
る。
Further, the condensate and the carbide can be transported to a remote place by packing them in a tank or a container.
It can be used as a heat source for distant facilities. Organic waste containing chlorine compounds such as polyvinyl chloride and polyethylene can be thermally decomposed in an oxygen-free atmosphere, depending on the pyrolysis temperature. The condensate and the remainder become combustible gas. These ratios tend to generate more condensate as the thermal decomposition temperature is lower. The energy of each product is about 5000 Kcal / Kg for carbide and about 100 for condensate.
00Kcal / Kg, flammable gas is about 7000Kcal /
Kg. This indicates that the product from organic waste can be used as a heat source.

【0009】さらに、実験によれば100Kgの有機性
廃棄物を熱分解する正味電力量は10Kw×3時間であ
ったので熱分解炉の熱効率を50%とした場合、0.6
KHWH/Kgが実際に必用な電力量となる。そして、
その結果の生成物の量とエネルギとを前記のとおりとす
ると可燃ガス、および凝縮液、炭化物のエネルギの合計
は(5000×0.15+10000×0.65+70
00×0.2)Kcal/Kg/860Kcal/KW
H=10KWHとなり、熱分解に投入したエネルギの約
16倍のエネルギが得られたことになり、エネルギ的に
も充分に収支がとれる。
Further, according to the experiment, the net electric energy for thermally decomposing 100 kg of organic waste was 10 Kw × 3 hours.
KHWH / Kg is the actually required power amount. And
Assuming that the amount and energy of the resulting product are as described above, the total energy of the combustible gas, condensate, and carbide is (5000 × 0.15 + 10000 × 0.65 + 70).
00 × 0.2) Kcal / Kg / 860Kcal / KW
H = 10 KWH, which means that about 16 times the energy input to the thermal decomposition was obtained, and a sufficient balance can be obtained in terms of energy.

【0010】例えば、一方では農事用に使用されたポリ
塩化ビニール、ポリエチレンなどの塩素化合物を含む有
機性廃棄物があり、他方温室や畜舎などに暖房が必用な
場合、この発明の有機性廃棄物の利用方法を適用して、
前記有機性廃棄物を熱分解して得られた生成物を暖房用
熱源として利用すれば、不燃ごみの廃棄を無くし、暖房
の熱源を得る一石二鳥のメリットとなる。
For example, on the one hand, there is an organic waste containing chlorine compounds such as polyvinyl chloride and polyethylene used for farming, and on the other hand, when the greenhouse or the livestock house needs heating, the organic waste of the present invention is used. Apply the usage of
If a product obtained by thermally decomposing the organic waste is used as a heat source for heating, it is possible to eliminate the disposal of non-combustible refuse and obtain the advantage of two birds with one heat source for obtaining a heat source for heating.

【0011】[0011]

【発明の実施の形態】図1はこの発明の実施の形態の主
要部のブロック図を示す。この図1において、1はポリ
塩化ビニール、ポリエチレンなどの塩素化合物を含む有
機性廃棄物、2は有機性廃棄物1を無酸素雰囲気中で熱
分解する熱分解装置であり、開閉可能な蓋、および可燃
ガス引出し口を有し、内部を不活性ガス雰囲気に保持す
る密閉式の加熱室と、該加熱室を外側から誘導加熱する
誘導コイルとで構成されている。そして、この熱分解装
置2により熱分解された有機性廃棄物1は可燃ガス、お
よび凝縮液、炭化物としてそれぞれ可燃ガスライン、お
よび凝縮液ライン、炭化物ラインを経由して取出され
る。前記可燃ガスラインの途中には苛性ソーダ溶液で、
可燃ガス中に含まれる塩素を中和するするようにした脱
塩素処理3の工程を設けてガスバーナ9で可燃ガスを燃
焼させて、暖房7に用いる際にダイオキシンが発生しな
いようにしている。また、可燃ガスのガスバーナ9への
送量を平均化するためのアキュームレータ6が脱塩素処
理3の工程の後に設けられている。
FIG. 1 is a block diagram showing a main part of an embodiment of the present invention. In FIG. 1, reference numeral 1 denotes an organic waste containing a chlorine compound such as polyvinyl chloride or polyethylene, and reference numeral 2 denotes a pyrolysis apparatus for thermally decomposing the organic waste 1 in an oxygen-free atmosphere. And a hermetic heating chamber having a combustible gas outlet and maintaining the interior in an inert gas atmosphere, and an induction coil for induction heating the heating chamber from the outside. The organic waste 1 thermally decomposed by the pyrolysis device 2 is taken out as a combustible gas, a condensate, and a carbide through a combustible gas line, a condensate line, and a carbide line, respectively. In the middle of the combustible gas line is a caustic soda solution,
A step of a dechlorination treatment 3 for neutralizing chlorine contained in the combustible gas is provided, and the combustible gas is burned by the gas burner 9 so that dioxin is not generated when used for the heating 7. An accumulator 6 for averaging the amount of combustible gas sent to the gas burner 9 is provided after the dechlorination process 3.

【0012】また、凝縮液ラインにも苛性ソーダ溶液と
混合させて凝縮液中に含まれる塩素を中和し、その後、
油水分離装置(図示されていない)を通す脱塩素処理4
の工程を設けて、塩素を含まない凝縮液を貯留タンク8
に送油して、そこから必要に応じてオイルバーナ10に
給油して暖房7に供している。また、炭化物ラインでは
炭化物は可燃ガス、および凝縮液が取出された後の残留
物として熱分解処理装置2がバッチ処理装置の場合熱分
解終了後に取出されて、手作業、または規模によっては
電磁力を応用した金属分離機などによって炭化物中の金
属を分離する異物除去処理5の工程を経由して、図示さ
れていない一次貯留場所に送られ、そこから必要に応じ
て燃焼器11に送られ暖房のように供せられる。
Further, the condensate line is also mixed with a caustic soda solution to neutralize chlorine contained in the condensate, and thereafter,
Dechlorination 4 through an oil / water separator (not shown)
And the condensate containing no chlorine is stored in the storage tank 8.
The oil is supplied to an oil burner 10 and supplied to a heater 7 as needed. In the carbide line, carbide is taken out as a residue after the combustible gas and condensate are taken out, and when the pyrolysis treatment unit 2 is a batch treatment unit, it is taken out after the end of the pyrolysis. Is sent to a primary storage location (not shown) via a foreign matter removal process 5 for separating metals in carbides by a metal separator or the like to which the metal is separated, and then sent to the combustor 11 as necessary to heat. Served like.

【0013】なお、脱塩素処理された後の凝縮液と、炭
化物とは、図中一点鎖線で示したように輸送用タンク1
2、および輸送用容器13などに詰めて輸送できるの
で、遠地輸送して所望の場所で暖房要として使用しても
良い。上記は燃焼熱を利用する用途は暖房についてのみ
説明したが燃焼熱を発電など別の要とに利用することも
できる。
The condensate and the carbide after the dechlorination treatment are combined with the transport tank 1 as shown by the dashed line in the figure.
2, since it can be packed and transported in the transport container 13 or the like, it may be transported distantly and used at a desired place as a heating element. In the above description, the use of combustion heat is described only for heating, but the combustion heat can be used for another purpose such as power generation.

【0014】[0014]

【発明の効果】この発明によれば、ポリ塩化ビニール、
ポリエチレンなどの塩素化合物を含む有機性廃棄物を無
酸素雰囲気で熱分解して、有害物質になる恐れがある塩
素を酸素に触れる前に中和して無害な物質に変えている
ので、ダイオキシンを発生させること無く、減容、およ
び燃料化できる効果がある。また、安価な夜間電力を使
用してポリ塩化ビニール、ポリエチレンなどの塩素化合
物を含む有機性廃棄物を処理し、投入電力量の約16倍
の熱エネルギを取出せるので、農事用などのように一方
では有機生廃棄物があり、他方ハウスなどの暖房用熱源
が必用な場合、廃棄物を安価に、かつ無公害で有効に利
用できる効果がある。
According to the present invention, polyvinyl chloride,
Organic waste containing chlorine compounds such as polyethylene is thermally decomposed in an oxygen-free atmosphere, and chlorine, which may become a harmful substance, is neutralized before touching oxygen to change it into harmless substances. There is an effect that the volume can be reduced and the fuel can be used without causing the generation. Also, organic waste containing chlorine compounds such as polyvinyl chloride and polyethylene can be treated using inexpensive night-time electricity, and heat energy that is about 16 times the input power can be extracted. On the one hand, there is an organic raw waste, and on the other hand, when a heating heat source such as a house is necessary, there is an effect that the waste can be effectively used at low cost and without pollution.

【図面の簡単な説明】[Brief description of the drawings]

【図1】この発明の実施の形態の主要部分のブロック図FIG. 1 is a block diagram of a main part of an embodiment of the present invention.

【符号の説明】 1 有機性廃棄物 2 熱分解装置 3、4 脱塩素処理 5 異物除去処理 6 アキュームレータ 7 暖房 8 貯留タンク 9 ガスバーナ 10 オイルバーナ 11 燃焼器 12 輸送用タンク 13 輸送用容器[Description of Signs] 1 Organic waste 2 Pyrolyzer 3, 4 Dechlorination treatment 5 Foreign matter removal treatment 6 Accumulator 7 Heating 8 Storage tank 9 Gas burner 10 Oil burner 11 Combustor 12 Transport tank 13 Transport container

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C10K 1/12 C10K 1/12 4H060 C10L 1/00 C10L 1/00 5/48 5/48 (72)発明者 林 静男 神奈川県川崎市川崎区田辺新田1番1号 富士電機株式会社内 Fターム(参考) 4F301 AA13 AA17 CA25 CA52 CA68 CA71 4H012 HB01 HB09 4H013 AA02 AA03 4H015 AA02 AA17 AB01 BA12 BB03 CB01 4H029 CA01 CA11 CA14 4H060 AA01 BB03 BB23 CC04 DD13 FF04 GG08 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI theme coat ゛ (Reference) C10K 1/12 C10K 1/12 4H060 C10L 1/00 C10L 1/00 5/48 5/48 (72) Invention Person Shizuo Hayashi 1-1-1 Tanabeshinda, Kawasaki-ku, Kawasaki-shi, Kanagawa Prefecture F-term in Fuji Electric Co., Ltd. 4H060 AA01 BB03 BB23 CC04 DD13 FF04 GG08

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】有機性廃棄物を無酸素状態で熱分解して、
可燃ガス、凝縮液、および炭化物を生成し、該可燃ガ
ス、および凝縮液、炭化物を脱塩素処理した後、燃焼熱
を利用した用途の熱源として利用することを特徴とする
有機性廃棄物の利用方法。
An organic waste is pyrolyzed in an oxygen-free state.
Use of organic waste, characterized in that combustible gas, condensate, and carbide are generated, and the combustible gas, condensate, and carbide are dechlorinated and then used as a heat source for applications utilizing combustion heat. Method.
【請求項2】請求項1記載の有機性廃棄物の利用方法に
おいて、有機性廃棄物を熱分解する装置は、開閉可能な
蓋、および可燃ガス引出し口を有し、内部を不活性ガス
雰囲気に保持する密閉式の加熱室と、該加熱室を外側か
ら誘導加熱する誘導コイルとで構成することを特徴とす
る有機性廃棄物の利用方法。
2. The method for utilizing organic waste according to claim 1, wherein the apparatus for thermally decomposing the organic waste has an openable and closable lid and a combustible gas outlet, and has an inert gas atmosphere inside. A method of utilizing organic waste, comprising: a closed-type heating chamber for holding the heating chamber, and an induction coil for induction-heating the heating chamber from the outside.
【請求項3】請求項1記載の有機性廃棄物の利用方法に
おいて、有機性廃棄物の熱分解は間欠操業とし、熱分解
中に発せする可燃ガスは即時熱源として利用し、凝縮
液、および炭化物は熱分解停止中に熱源として利用して
熱源の供給が終日連続するようにしたことを特徴とする
有機性廃棄物の利用方法。
3. The method of claim 1, wherein the pyrolysis of the organic waste is an intermittent operation, and the combustible gas generated during the pyrolysis is used as an immediate heat source, and the condensate, A method of using organic waste, wherein the carbide is used as a heat source during the stop of thermal decomposition so that the supply of the heat source is continued throughout the day.
【請求項4】請求項1ないし請求項3のいずれかに記載
の有機性廃棄物の利用方法において、有機性廃棄物を熱
分解して得られる可燃ガスを回収する際に、可燃ガス中
に含有される塩素を除去する脱塩処理を行い、脱塩後の
可燃ガスをアキュームレータで平均化して後段に供給す
るようにしたことを特徴とする有機性廃棄物の利用方
法。
4. The method for utilizing organic waste according to claim 1, wherein the combustible gas obtained by thermally decomposing the organic waste is recovered. A method for utilizing organic waste, comprising performing a desalination treatment for removing chlorine contained therein, and averaging a combustible gas after desalination with an accumulator and supplying the combustible gas to a subsequent stage.
【請求項5】請求項1または請求項4に記載の有機性廃
棄物からの利用方法において、有機性廃棄物を熱分解し
て得られる凝縮液を貯留タンクに回収する際に、凝縮液
中に含有される塩素を除去する脱塩処理を行うことを特
徴とする有機性廃棄物の利用方法。
5. The method according to claim 1, wherein the condensate obtained by thermally decomposing the organic waste is collected in a storage tank. A method for utilizing organic waste, comprising performing a desalination treatment for removing chlorine contained in water.
JP2000284609A 2000-09-20 2000-09-20 Method for utilizing organic waste Pending JP2002088372A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000284609A JP2002088372A (en) 2000-09-20 2000-09-20 Method for utilizing organic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000284609A JP2002088372A (en) 2000-09-20 2000-09-20 Method for utilizing organic waste

Publications (1)

Publication Number Publication Date
JP2002088372A true JP2002088372A (en) 2002-03-27

Family

ID=18768792

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000284609A Pending JP2002088372A (en) 2000-09-20 2000-09-20 Method for utilizing organic waste

Country Status (1)

Country Link
JP (1) JP2002088372A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007169484A (en) * 2005-12-22 2007-07-05 Saitama Univ Pulverized fuel of biomass-coal blend from coal powder and/or carbonized material from wastes and powder of vegetable-derived polymer organic material, combustible gas, and process for producing combustible and char

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007169484A (en) * 2005-12-22 2007-07-05 Saitama Univ Pulverized fuel of biomass-coal blend from coal powder and/or carbonized material from wastes and powder of vegetable-derived polymer organic material, combustible gas, and process for producing combustible and char

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