JP2010149079A - Treatment method of waste containing highly hydrous waste and treatment device used for the same - Google Patents

Treatment method of waste containing highly hydrous waste and treatment device used for the same Download PDF

Info

Publication number
JP2010149079A
JP2010149079A JP2008332218A JP2008332218A JP2010149079A JP 2010149079 A JP2010149079 A JP 2010149079A JP 2008332218 A JP2008332218 A JP 2008332218A JP 2008332218 A JP2008332218 A JP 2008332218A JP 2010149079 A JP2010149079 A JP 2010149079A
Authority
JP
Japan
Prior art keywords
waste
melting furnace
furnace
treatment
methane fermentation
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
JP2008332218A
Other languages
Japanese (ja)
Inventor
Masaya Kurita
雅也 栗田
Yuichi Yoshimoto
雄一 吉本
Toshimi Nagata
俊美 永田
Yasuhiko Mori
泰彦 森
Morihiro Osada
守弘 長田
Keiji Nakazono
啓二 中園
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.)
Nippon Steel Engineering Co Ltd
Original Assignee
Nippon Steel Engineering 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 Nippon Steel Engineering Co Ltd filed Critical Nippon Steel Engineering Co Ltd
Priority to JP2008332218A priority Critical patent/JP2010149079A/en
Publication of JP2010149079A publication Critical patent/JP2010149079A/en
Pending legal-status Critical Current

Links

Images

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
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • 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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing
    • 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
    • Y02W30/20Waste processing or separation

Landscapes

  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a treatment method of waste containing highly hydrous waste collecting the heat of the waste without consuming it as evaporative latent heat of contained water, collecting energy that high-moisture waste has with high yield, and reducing a consumption amount of chemicals required for drainage treatment, and also to provide a treatment device used for the same. <P>SOLUTION: Organic biomass having high moisture content such as food waste or sludge is separated to methane gas, digested sludge and drain by methane fermentation treatment. The water content of the digestive sludge is reduced and then the digestive sludge is mixed with an organic waste so that the water content of the waste to be treated in a gasifying melted furnace is reduced. A whole amount or a part of the methane gas obtained from the methane fermentation is blown to the tuyere of the gasifying melted furnace together with oxygen, air added with oxygen, and combustible dust collected at the latter part of the gasifying melted furnace, and is used as a reducing agent in the furnace and a heat source for heating. So that a consumption amount of coke used as the fuel of the gasifying melted furnace, and a whole amount or a part of the drain generated as a by-product by the methane fermentation treatment is blown to a combustion furnace arranged at the latter part of the gasifying melted furnace and is detoxified. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、高含水廃棄物を含んだ廃棄物の処理方法および処理装置に関する。   The present invention relates to a processing method and a processing apparatus for waste containing high water content waste.

具体的には、食品廃棄物、汚泥、泥炭などのように、含水率が70%以上である廃棄物及び有機物を含んだ全体での水分が40%を超える廃棄物の処理方法および処理装置に関する。   Specifically, the present invention relates to a processing method and a processing apparatus for waste having a moisture content of 70% or more, such as food waste, sludge, peat, and the like, and waste having a total water content exceeding 40%. .

近年、京都議定書への批准を始め、CO2に対する削減要求は高く、バイオマス等の再生可能エネルギーの利用に関する要求が高まっていている。   In recent years, with the ratification of the Kyoto Protocol, the demand for CO2 reduction is high, and the demand for the use of renewable energy such as biomass is increasing.

特に、下水汚泥等、バイオマスの一部は水分を多く含んでおり、これらの廃棄物を熱として利用する場合、排ガス中の顕熱や水分の蒸発潜熱によって熱が十分に利用できないという問題点があった。   In particular, some biomass, such as sewage sludge, contains a lot of moisture, and when these wastes are used as heat, there is a problem that heat cannot be sufficiently utilized due to sensible heat in the exhaust gas or latent heat of vaporization of moisture. there were.

これらの未利用エネルギーを利用することにより、CO2排出量の低減と温暖化の防止に大きく寄与できる。   Utilizing these unused energy can greatly contribute to the reduction of CO2 emissions and the prevention of global warming.

高含水廃棄物の処理方法については、従来から種々の提案がなされている。   Various proposals have conventionally been made on methods for treating highly hydrous waste.

例えば、特許第3758513号公報(下記特許文献1)には、消化ガスでガスタービンを回し、ガスタービン、ガスエンジンの排熱を熱分解の熱源とする。しかし、ガスタービンの排気では温度が低く、十分な熱分解が得られないうえ、特許文献1の方式では廃棄物の灰分を溶融することはできず、リサイクル率が十分に得られないという問題点があった。
特許第3758513号公報
For example, in Japanese Patent No. 3758513 (Patent Document 1 below), a gas turbine is rotated with digestion gas, and exhaust heat of the gas turbine and gas engine is used as a heat source for thermal decomposition. However, the temperature of the exhaust gas from the gas turbine is low and sufficient thermal decomposition cannot be obtained, and the ash content of the waste cannot be melted by the method of Patent Document 1 and the recycling rate cannot be sufficiently obtained. was there.
Japanese Patent No. 3758513

本発明は、本発明は、水分の高い廃棄物をガス化、乾燥する際必要となる、廃棄物に含まれる水の蒸発潜熱による熱の消費を抑制し、高水分廃棄物のもつエネルギーを高効率で回収することができるうえ、排水処理に必要な薬品類の消費量を低減できる高含水廃棄物を含んだ廃棄物の処理方法および処理装置を提供することを課題とする。   The present invention suppresses heat consumption due to the latent heat of evaporation of water contained in waste, which is necessary when gasifying and drying waste with high moisture content, and increases the energy of high moisture waste. It is an object of the present invention to provide a treatment method and a treatment apparatus for waste containing a highly water-containing waste that can be efficiently recovered and reduce the consumption of chemicals necessary for wastewater treatment.

本発明は、前述の課題を解決するために鋭意検討の結果、なされたものであり、その要旨とするところは特許請求の範囲に記載したとおりの下記内容である。
(1)一般廃棄物を含む有機性廃棄物をガス化溶融炉で処理する廃棄物の処理方法において、食品廃棄物や汚泥等の含水率の高い有機性バイオマスとその他の廃棄物とを分離し、含水率の高い有機性バイオマスをメタン発酵処理によりメタンガスと消化汚泥および排水に分離し、前記消化汚泥は水分を低減した上でその他の有機性廃棄物と混合することによりガス化溶融炉にて処理する廃棄物の水分量を低減し、前記メタン発酵によって得られたメタンガスの全量もしくは一部を酸素もしくは酸素付加空気およびガス化溶融炉の後段で採取された可燃性ダストと共にガス化溶融炉の羽口に吹き込むと共に、前記メタン発効処理によって副生する排水の全量もしくは一部をガス化溶融炉の後段に設置する燃焼炉に吹き込んで無害化することを特徴とする、高含水廃棄物を含んだ廃棄物の処理方法。
(2)前記ガス化溶融炉をシャフト式ガス化炉とし、前記メタン発酵によって得られたメタンガスを可燃性ガスと共に羽口に吹き込むとともに、余剰分をガスエンジンで発電する若しくはガス化溶融炉の廃熱ボイラ発電システムに付随する外部過熱器の熱源として利用することを特徴とする、(1)に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(3)前記ガス化溶融炉をシャフト式ガス化炉とし、該ガス化炉へ投入する水分量を10から40%に調整することを特徴とする、(1)または(2)に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(4)前記消化汚泥の含水率の低減方法として好気性発酵を用いることを特徴とする、(1)〜(3)のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(5)前記高含水廃棄物のうち、メタンガスの発生率の高い厨芥類をメタン発酵し、メタンガス発生率の低い下水汚泥、し尿汚泥とメタン発酵残渣のいずれかを好気性発酵による熱で乾燥させることを特徴とする、(1)〜(4)のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(6)ごみピットの底部に滞留するごみ汚水をメタン発酵の原料若しくはメタン発酵処理に必要な添加水として利用することを特徴とする、(1)〜(5)のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(7)前記ガス化溶融炉から出る排水をメタン発酵に必要な添加水として利用することを特徴とする、(1)〜(6)のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(8)前記メタン発酵処理にて発生する排水を1次処理し、ガス化溶融炉から発生する排水と混合して排水処理することを特徴とする、(1)〜(7)のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(9)前記メタン発酵に必要な熱源をガス化溶融炉の排熱を利用して得ることを特徴とする、(1)〜(8)のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(10)前記排熱が蒸気タービン排気であることを特徴とする、(9)に記載の高含水廃棄物を含んだ廃棄物の処理方法。
(11)(1)〜(10)のいずれか一項に記載の高含水廃棄物の処理方法に用いるガス化溶融炉およびメタン発酵処理装置を有することを特徴とする、高含水廃棄物を含んだ廃棄物の処理装置。
<作用>
The present invention has been made as a result of intensive studies in order to solve the above-mentioned problems, and the gist of the present invention is the following contents as described in the claims.
(1) In a waste treatment method in which organic waste including general waste is treated in a gasification melting furnace, organic biomass with a high water content such as food waste and sludge is separated from other waste. The organic biomass with a high water content is separated into methane gas, digested sludge and wastewater by methane fermentation treatment, and the digested sludge is mixed with other organic waste after reducing moisture in a gasification melting furnace. Reduce the amount of water in the waste to be treated, and add all or part of the methane gas obtained by the methane fermentation together with oxygen or oxygenated air and combustible dust collected after the gasification melting furnace. In addition to blowing into the tuyere, all or part of the wastewater produced as a by-product of the methane effecting treatment is blown into a combustion furnace installed downstream of the gasification melting furnace to make it harmless. And the processing method of waste containing a high water content waste.
(2) The gasification melting furnace is a shaft type gasification furnace, and the methane gas obtained by the methane fermentation is blown into the tuyere together with the combustible gas, and the surplus is generated by the gas engine or the gasification melting furnace is discarded. The method for treating waste containing high water content waste according to (1), characterized in that it is used as a heat source for an external superheater associated with a thermal boiler power generation system.
(3) The gasification and melting furnace is a shaft type gasification furnace, and the amount of water charged into the gasification furnace is adjusted to 10 to 40%. The high value according to (1) or (2) A method for treating waste containing hydrous waste.
(4) Aerobic fermentation is used as a method for reducing the moisture content of the digested sludge, and the treatment of the waste containing the highly water-containing waste according to any one of (1) to (3) Method.
(5) Among the highly water-containing wastes, methane fermentation is performed with a high methane gas generation rate, and either sewage sludge, human waste sludge, or methane fermentation residue with a low methane gas generation rate is dried with heat from aerobic fermentation. The processing method of the waste containing the highly water-containing waste as described in any one of (1)-(4) characterized by the above-mentioned.
(6) The waste sewage staying at the bottom of the waste pit is used as a raw material for methane fermentation or as additional water necessary for methane fermentation treatment, as described in any one of (1) to (5) A method for treating waste containing highly water-containing waste.
(7) The highly water-containing waste according to any one of (1) to (6) is used, characterized in that wastewater discharged from the gasification melting furnace is used as additive water necessary for methane fermentation. Waste disposal method.
(8) Any one of (1) to (7), characterized in that the wastewater generated in the methane fermentation treatment is subjected to primary treatment and mixed with wastewater generated from a gasification melting furnace to perform wastewater treatment. The disposal method of the waste containing the high water content waste as described in a term.
(9) The highly water-containing waste according to any one of (1) to (8), wherein the heat source necessary for the methane fermentation is obtained using exhaust heat of a gasification melting furnace. Waste disposal methods.
(10) The method for treating waste containing high water content waste according to (9), wherein the exhaust heat is steam turbine exhaust.
(11) A high water content waste characterized by having a gasification melting furnace and a methane fermentation treatment device used in the method for processing a high water content waste according to any one of (1) to (10). Waste disposal equipment.
<Action>

廃棄物を焼却その他の熱処理にて処理し、得られる熱をボイラ等で熱回収し、発電その他の方法により熱を利用する施設において、被処理対象物の含水率が高い場合、焼却によって生じる熱は廃棄物に含まれる水分の蒸発に消費され、熱として回収することが困難である。
(1)の発明によれば、シャフト式ガス化溶融炉では還元剤としてコークスを使用するが、水分が多い場合、乾燥にエネルギーを消費され、コークス使用量が多くなることがある。水分の高い廃棄物をメタン発酵処理することで水分の分離が可能となり、ガス化炉に投入される水分を抑制することができる。また、得られたメタンガスを羽口に吹き込むことによりコークス使用量の削減を図ることができる。また、分離された水分は有機性排水であるため、放流には排水処理が必要となるが、排水処理には薬品が膨大に必要になり、経済的に好ましくなく、薬剤を消費することで環境への負荷も高くなる。しかしながら排水を燃焼炉に吹き込むことで、ガス化溶融炉でのコークスへの影響を与えることなく有機排水の処理が可能となる。シャフト以外のガス化溶融炉においても溶融炉での水分バイパス処理が可能となり灯油、重油等の補助燃料の消費量が削減できる。また、メタンガスを羽口に吹き込む際には、溶融炉の後段で回収されたダストと共に吹き込むことで効果が大きくなる。
(2)の発明によれば、余剰のメタンガスを用いてガスエンジン発電することで高い発電効率を得ることができる。羽口に吹き込むことで全量ガスエンジン発電する場合に比べ、1次エネルギーとして利用するためエネルギーの利用効率が高い。また、メタンガスは燃焼しても腐食性ガスを発生させないことから、従来腐食の問題等で温度を上げられず、効率の上がらない廃棄物発電の効率を向上させることができる。
(3)の発明によれば、有機性廃棄物の分別割合を調整することでガス化溶融炉に投入される水分の割合を調整することができる。また、好気性発酵で発生する臭気は燃焼空気として燃焼室に吹き込むことで臭気を分解することもできる。
(4)の発明によれば、好気性発酵の発酵熱を利用することで新たにエネルギーを消費することなく水分を除去することが可能となる。
(5)の発明によれば、発酵効率の高い廃棄物に限定してメタン発酵処理をすることで、発酵設備のコンパクト化を図ることができ、2次発酵熱で下水汚泥を乾燥させることで、下水汚泥のもつエネルギーを水分蒸発に消費されることなく廃棄物発電に利用することが可能となる。
(6)の発明によれば、ピットからはごみから出た水分が回収されるが、有機性排水であるため、排水にはコストがかかる。メタン発酵と同時に処理することで低コスト名処理が可能となる。
(7)の発明によれば、雑排水等をメタン発酵処理の添加水として利用することで上水の使用量を削減することが可能となる。
(8)の発明によれば、排水処理を実施する場合、溶融処理から出る排水とメタン発酵処理で発生する排水とで同一の処理工程を混合処理することで排水処理設備のコンパクト化を図ることができる。
(9)の発明によれば、メタン発酵に必要な熱源をガス化溶融炉の排熱を利用することで全体の熱効率の向上を図ることができる。
(10)の発明によれば、タービン排気は他に利用することができないため、プラント全体の熱効率を上げるためにはタービン排気熱の利用が効果的である。
(11)の発明によれば、ガス化溶融炉およびメタン発酵処理装置を有することにより、(1)〜(10)に記載の高含水廃棄物を含んだ廃棄物の処理方法を実現する処理装置を提供することができる。
In facilities where waste is treated by incineration or other heat treatment, the heat obtained is recovered by a boiler, etc., and heat is used by power generation or other methods, heat generated by incineration when the moisture content of the object to be treated is high Is consumed by the evaporation of water contained in the waste and is difficult to recover as heat.
According to the invention of (1), coke is used as a reducing agent in the shaft type gasification melting furnace. However, when there is a lot of moisture, energy is consumed for drying, and the amount of coke used may increase. Moisture separation can be achieved by subjecting waste with high water content to methane fermentation, and water supplied to the gasifier can be suppressed. Further, the amount of coke used can be reduced by blowing the obtained methane gas into the tuyere. In addition, because the separated water is organic wastewater, wastewater treatment is required for discharge, but wastewater treatment requires a huge amount of chemicals, which is economically undesirable and consumes chemicals. The load on is also high. However, by blowing wastewater into the combustion furnace, it becomes possible to treat organic wastewater without affecting coke in the gasification melting furnace. Even in gasification melting furnaces other than the shaft, moisture bypass processing in the melting furnace is possible, and consumption of auxiliary fuel such as kerosene and heavy oil can be reduced. In addition, when methane gas is blown into the tuyere, the effect is increased by blowing it together with dust collected at the subsequent stage of the melting furnace.
According to the invention of (2), high power generation efficiency can be obtained by performing gas engine power generation using surplus methane gas. Compared to the case where all gas engine power is generated by blowing into the tuyere, it is used as primary energy, so the energy utilization efficiency is high. Further, since methane gas does not generate corrosive gas even if it is burned, the efficiency of waste power generation that does not increase the temperature due to the problem of conventional corrosion and does not increase efficiency can be improved.
According to invention of (3), the ratio of the water | moisture content thrown into a gasification melting furnace can be adjusted by adjusting the fraction of organic waste. Moreover, the odor generated by aerobic fermentation can be decomposed by blowing it into the combustion chamber as combustion air.
According to the invention of (4), it becomes possible to remove moisture without newly consuming energy by using the fermentation heat of aerobic fermentation.
According to the invention of (5), the fermentation equipment can be made compact by carrying out methane fermentation treatment limited to waste with high fermentation efficiency, and by drying sewage sludge with secondary fermentation heat. The energy of sewage sludge can be used for waste power generation without being consumed for water evaporation.
According to the invention of (6), the water discharged from the trash is recovered from the pit, but since it is organic wastewater, drainage is costly. By processing at the same time as methane fermentation, low cost name processing becomes possible.
According to invention of (7), it becomes possible to reduce the usage-amount of clean water by using miscellaneous wastewater etc. as additional water of a methane fermentation process.
According to the invention of (8), when wastewater treatment is carried out, the wastewater treatment facility can be made compact by mixing and treating the same treatment process with wastewater from the melting treatment and wastewater generated by the methane fermentation treatment. Can do.
According to the invention of (9), it is possible to improve the overall thermal efficiency by utilizing the exhaust heat of the gasification melting furnace as a heat source necessary for methane fermentation.
According to the invention of (10), since the turbine exhaust cannot be used elsewhere, the use of the turbine exhaust heat is effective for increasing the thermal efficiency of the entire plant.
According to the invention of (11), a processing apparatus for realizing the waste processing method including the highly water-containing waste described in (1) to (10) by having a gasification melting furnace and a methane fermentation processing apparatus. Can be provided.

本発明によれば、食品廃棄物、汚泥、泥炭などの含水率の高い廃棄物に含まれる水の蒸発潜熱を回収し、高水分廃棄物のもつエネルギーを高効率で回収することができるうえ、排水処理に必要な薬品類の消費量を低減できる高含水廃棄物を含んだ廃棄物の処理方法および処理装置を提供することができるなど、産業上有用な著しい効果を奏する。   According to the present invention, it is possible to recover the latent heat of evaporation of water contained in food waste, sludge, peat and other high water content waste, and to recover the energy of high moisture waste with high efficiency. It is possible to provide a processing method and a processing apparatus for waste containing high water content waste that can reduce the consumption of chemicals necessary for wastewater treatment, and the present invention has significant industrially useful effects.

本発明を実施するための最良の形態について図1〜図7を用いて詳細に説明する。   The best mode for carrying out the present invention will be described in detail with reference to FIGS.

図1〜図7において、1は高含水バイオマス、2は前処理装置、3はメタン発酵装置、4は脱水装置、5は乾燥装置、6は有機排水処理、7はガス処理、8は廃棄物、9は、ガス化溶融炉、9´はガス化炉、10は燃焼炉、10´は2次燃焼炉、11はボイラ、12は節炭器、13は減温塔、14は脱気器、5はバグフィルタ、16は誘引通風機、17は触媒反応塔、18は煙突、19は過熱器、19´は独立過熱器、20は蒸気タービン、21は復水器、22は復水タンクを示し、同じ要素については同じ記号を用いることにより説明の重複を避ける。   1 to 7, 1 is a high water content biomass, 2 is a pretreatment device, 3 is a methane fermentation device, 4 is a dehydration device, 5 is a drying device, 6 is an organic wastewater treatment, 7 is a gas treatment, and 8 is a waste product. , 9 is a gasification melting furnace, 9 'is a gasification furnace, 10 is a combustion furnace, 10' is a secondary combustion furnace, 11 is a boiler, 12 is a economizer, 13 is a temperature reducing tower, and 14 is a deaerator. 5 is a bag filter, 16 is an induction fan, 17 is a catalytic reaction tower, 18 is a chimney, 19 is a superheater, 19 'is an independent superheater, 20 is a steam turbine, 21 is a condenser, and 22 is a condensate tank. In order to avoid duplication of explanation, the same symbols are used for the same elements.

図1は、本発明の高含水廃棄物を含んだ廃棄物の処理方法におけるガス化溶融炉とメタン発酵の組み合わせを例示する図である。   FIG. 1 is a diagram illustrating a combination of a gasification melting furnace and methane fermentation in a method for treating waste containing high water content waste according to the present invention.

廃棄物を溶融処理する方法には、例えばシャフト炉式廃棄物溶融炉が使用される。これは図1に示すように、ガス化溶融炉9の上部から処理対象となる廃棄物8や助燃料としてのコークス、塩基度調整剤としての石灰石等を装入し、装入された廃棄物8は、溶融炉9の上層から乾燥・予熱帯(約300〜400℃)、熱分解帯(約300〜1000℃)、燃焼・溶融帯(約1700〜1800℃)を通過して溶融処理される。   As a method for melting the waste, for example, a shaft furnace type waste melting furnace is used. As shown in FIG. 1, the waste material 8 is charged from the upper part of the gasification melting furnace 9 with the waste 8 to be treated, coke as auxiliary fuel, limestone as the basicity adjusting agent, and the like. 8 is melt-processed from the upper layer of the melting furnace 9 through a dry / pre-tropical zone (about 300 to 400 ° C.), a thermal decomposition zone (about 300 to 1000 ° C.), and a combustion / melting zone (about 1700 to 1800 ° C.). The

また、高温の燃焼排ガスは、ガス化溶融炉9内の廃棄物の充填層を対向流として上昇し、溶融炉上部の排ガス管から可燃ガスとして燃焼炉10へ導入されて燃焼され、燃焼排ガスは、排ガス管を通ってボイラ11に導入されて節炭器12により熱交換されて廃熱が回収された後、減温塔13で温度を調整してバグフィルタ15にて除塵され、更には、触媒反応塔17で公害物質が除去された後、煙突18から排出される。   Further, the high-temperature combustion exhaust gas rises as a counterflow through the waste packed bed in the gasification melting furnace 9, is introduced into the combustion furnace 10 as a combustible gas from the exhaust gas pipe at the upper part of the melting furnace, and is combusted. Then, after being introduced into the boiler 11 through the exhaust gas pipe and heat exchanged by the economizer 12, the waste heat is recovered, the temperature is adjusted by the temperature reducing tower 13, and the dust is removed by the bag filter 15, After the pollutant is removed in the catalytic reaction tower 17, it is discharged from the chimney 18.

なお、図1に示すように、ボイラ11により回収された熱を蒸気タービン20の動力として用いることにより発電した電力は、補助動力、販売用電力として用いることができる。   In addition, as shown in FIG. 1, the electric power generated by using the heat | fever collect | recovered by the boiler 11 as motive power of the steam turbine 20 can be used as auxiliary power and electric power for sale.

しかし、従来の一般の廃棄物溶融炉では廃棄物を溶融するとともに、廃棄物に含まれる水分も処理する。このときに燃焼熱が水分の乾燥に消費され、熱として回収利用できないという問題点があった。   However, in a conventional general waste melting furnace, the waste is melted and moisture contained in the waste is also treated. At this time, there is a problem that the combustion heat is consumed for drying the moisture and cannot be recovered and used as heat.

そこで、本発明は、一般廃棄物を含む有機性廃棄物8をガス化溶融炉9で処理する廃棄物の処理方法において、食品廃棄物や汚泥等の含水率が例えば70%以上と高い有機性バイオマス1をメタン発酵装置3によりメタンガスと消化汚泥に分離し、前記消化汚泥は脱水装置4で水分を低減し、さらに乾燥装置5で水分を低減した上で有機性廃棄物と混合することによりガス化溶融炉にて処理する廃棄物の水分量を低減し、前記メタン発酵装置3によって得られたメタンガスの全量もしくは一部を酸素もしくは酸素付加空気およびガス化溶融炉の後段で採取された可燃性ダストと共にガス化溶融炉の羽口に吹き込み、炉内還元剤、加熱用の熱源として利用することにより、ガス化溶融炉の燃料として使用するコークスの消費量を抑制するとともに、前記メタン発酵処理によって副生する排水の全量もしくは一部をガス化溶融炉の後段に設置する燃焼炉に吹き込んで無害化することにより、排水処理に必要な薬品類の消費量を低減できることを特徴とする。   Therefore, the present invention is a waste treatment method in which organic waste 8 containing general waste is treated in the gasification melting furnace 9, and the water content of food waste, sludge, etc. is as high as 70% or higher. Biomass 1 is separated into methane gas and digested sludge by a methane fermentation device 3, and the digested sludge is gas-reduced by reducing moisture with a dehydrating device 4 and further reducing moisture with a drying device 5 and mixing with organic waste. The amount of water in the waste to be treated in the gasification and melting furnace is reduced, and all or part of the methane gas obtained by the methane fermentation apparatus 3 is combusted by oxygen or oxygen-added air and after the gasification and melting furnace. By blowing into the tuyere of the gasification and melting furnace together with dust and using it as a reducing agent in the furnace and a heat source for heating, the consumption of coke used as fuel for the gasification and melting furnace is suppressed. The amount of chemicals required for wastewater treatment can be reduced by blowing all of the wastewater produced as a by-product of the methane fermentation treatment into a combustion furnace installed downstream of the gasification melting furnace to make it harmless. Features.

即ち、本発明においては、シャフト式ガス化溶融炉では還元剤としてコークスを使用するが、水分が多い場合、乾燥にエネルギーを消費され、コークス使用量が多くなることがある。水分の高い廃棄物をメタン発酵処理することで水分の分離が可能となり、ガス化炉に投入される水分を抑制することができる。   That is, in the present invention, coke is used as a reducing agent in the shaft type gasification melting furnace. However, when there is a lot of moisture, energy is consumed for drying, and the amount of coke used may increase. Moisture separation can be achieved by subjecting waste with high water content to methane fermentation, and water supplied to the gasifier can be suppressed.

また、得られたメタンガスにガス処理7を施して成分調整した後、ガス化溶融炉9の羽口に吹き込むことによりコークス使用量の削減を図ることができる。また、分離された水分は有機性排水であるため、放流には排水処理が必要となるが、排水処理には薬品が膨大に必要になり、経済的に好ましくなく、薬剤を消費することで環境への負荷も高くなる。しかしながら排水を燃焼炉10に吹き込むことで、ガス化溶融炉9でのコークスへの影響を与えることなく有機排水の処理が可能となる。シャフト以外のガス化溶融炉においても溶融炉での水分バイパス処理が可能となり灯油、重油等の補助燃料の消費量が削減できる。   In addition, after the gas treatment 7 is applied to the obtained methane gas to adjust the components, the amount of coke used can be reduced by blowing into the tuyere of the gasification melting furnace 9. In addition, because the separated water is organic wastewater, wastewater treatment is required for discharge, but wastewater treatment requires a huge amount of chemicals, which is economically undesirable and consumes chemicals. The load on is also high. However, by blowing the waste water into the combustion furnace 10, it becomes possible to treat organic waste water without affecting the coke in the gasification melting furnace 9. Even in gasification melting furnaces other than the shaft, moisture bypass processing in the melting furnace is possible, and consumption of auxiliary fuel such as kerosene and heavy oil can be reduced.

排水は全量燃焼炉に吹き込まない場合でも運転に最適な量を吹込み、残りを排水処理し、放流することで、排水処理のコストを抑制することができる。燃焼炉に吹き込む量が過剰に多い場合、炉の安定運転に影響を与える恐れがある。   Even when the entire amount of waste water is not blown into the combustion furnace, the optimum amount for operation is blown, the remaining waste water is treated and discharged, and the cost of waste water treatment can be suppressed. If the amount blown into the combustion furnace is excessively large, stable operation of the furnace may be affected.

本発明において、高含水廃棄物とは廃棄物に含まれる水分が70%以上のものをいう。   In the present invention, the highly water-containing waste means one having a water content of 70% or more.

また、乾燥装置としては流動層、キルン好気発酵等が利用可能であり、廃棄物を乾燥する場合、密閉式の乾燥炉を用い、臭気の拡散を防止することが望ましい。   In addition, a fluidized bed, kiln aerobic fermentation, or the like can be used as a drying device. When drying waste, it is desirable to use an enclosed drying furnace to prevent odor diffusion.

また、乾燥後の凝縮水を放流する際には排水基準等の条件に応じて下水道処理場もしくは有機排水処理6を設け、排水基準を満たすように無害化した上で下水放流することが好ましい。   In addition, when discharging the condensed water after drying, it is preferable to provide a sewerage treatment plant or an organic wastewater treatment 6 according to the conditions such as the drainage standard, detoxify so as to satisfy the drainage standard, and then discharge the sewage.

図2は、本発明の高含水廃棄物を含んだ廃棄物の処理方法におけるメタンガスその他の利用方法を例示する図である。   FIG. 2 is a diagram exemplifying a method of using methane gas and the like in the method for treating waste containing high water content waste according to the present invention.

前記メタン発酵によって得られたメタンガスをガス化溶融炉9の羽口に吹き込むとともに、余剰分をガスエンジンで発電する若しくはガス化溶融炉9の外部過熱器の熱源として利用することにより、余剰のメタンガスを用いてガスエンジン発電することで高い発電効率を得ることができる。羽口に吹き込むことで全量ガスエンジン発電する場合に比べ、1次エネルギーとして利用するためエネルギーの利用効率が高い。また、メタンガスは燃焼しても腐食性ガスを発生させないことから、従来腐食の問題等で温度を上げられず、効率の上がらない廃棄物発電の効率を向上させることができる。   The methane gas obtained by the methane fermentation is blown into the tuyere of the gasification melting furnace 9, and surplus methane gas is generated by generating a surplus with a gas engine or as a heat source for an external superheater of the gasification melting furnace 9. A high power generation efficiency can be obtained by generating a gas engine using the power. Compared to the case where all gas engine power is generated by blowing into the tuyere, it is used as primary energy, so the energy utilization efficiency is high. Further, since methane gas does not generate corrosive gas even if it is burned, the efficiency of waste power generation that does not increase the temperature due to the problem of conventional corrosion and does not increase efficiency can be improved.

図3は、本発明の高含水廃棄物を含んだ廃棄物の処理方法における下水汚泥の分離処理を例示する図である。   FIG. 3 is a diagram exemplifying the separation treatment of sewage sludge in the waste treatment method including a highly water-containing waste according to the present invention.

前記高含水廃棄物のうち、メタンガスの発生率の高い厨芥類をメタン発酵し、メタンガス発生率の低い下水汚泥、し尿汚泥等を好気性発酵による熱で乾燥させることにより、発酵効率の高い廃棄物に限定してメタン発酵処理をすることで、発酵設備のコンパクト化を図ることができ、2次発酵熱で下水汚泥を乾燥させることで、下水汚泥のもつエネルギーを廃棄物発電に利用することが可能となる。   Among the highly water-containing wastes, methane fermentation is performed on moss with high methane gas generation rate, and waste with high fermentation efficiency is obtained by drying sewage sludge, human waste sludge, etc. with low methane gas generation rate with heat from aerobic fermentation. It is possible to reduce the size of the fermentation equipment by performing the methane fermentation treatment only, and to use the energy of the sewage sludge for waste power generation by drying the sewage sludge with the secondary fermentation heat. It becomes possible.

図4は、本発明の高含水廃棄物を含んだ廃棄物の処理方法における排水の利用を例示する図である。   FIG. 4 is a diagram illustrating the use of wastewater in the method for treating waste containing high water content waste according to the present invention.

ごみピットの底部に滞留するごみ汚水をメタン発酵の原料若しくはメタン発酵処理に必要な添加水として利用することにより、ピットからはごみから出た水分が回収されるが、有機性排水であるため、排水にはコストがかかる。メタン発酵と同時に処理することで低コスト処理が可能となる。   By using waste sewage accumulated at the bottom of the waste pit as a raw material for methane fermentation or as additional water required for methane fermentation treatment, moisture from the pit is recovered, but because it is organic wastewater, Drainage is costly. Processing at the same time as methane fermentation enables low-cost processing.

また、前記ガス化溶融炉から出る排水をメタン発酵に必要な添加水として利用することにより、雑排水等をメタン発酵処理の添加水として利用することで上水の使用量を削減することが可能となる。   In addition, by using wastewater from the gasification melting furnace as additional water necessary for methane fermentation, it is possible to reduce the amount of water used by using miscellaneous wastewater as additional water for methane fermentation treatment. It becomes.

図5は、本発明の高含水廃棄物を含んだ廃棄物の処理方法における排水処理の共用を例示する図である。   FIG. 5 is a diagram illustrating common use of wastewater treatment in the method for treating waste containing high water content waste according to the present invention.

前記メタン発酵処理装置3にて発生する排水を1次処理し、ガス化溶融炉9から発生する排水と混合して排水処理することにより、排水処理を実施する場合、溶融処理から出る排水とメタン発酵処理装置3で発生する排水とで同一の処理工程を混合処理することで排水処理設備のコンパクト化を図ることができる。   When the wastewater generated in the methane fermentation treatment apparatus 3 is subjected to primary treatment and mixed with wastewater generated from the gasification melting furnace 9 for wastewater treatment, wastewater discharged from the melt treatment and methane The wastewater treatment facility can be made compact by mixing the same treatment process with the wastewater generated in the fermentation treatment apparatus 3.

図6は、本発明の高含水廃棄物を含んだ廃棄物の処理方法における余熱利用を例示する図である。   FIG. 6 is a diagram illustrating the use of residual heat in the method for treating waste containing high water content waste according to the present invention.

前記メタン発酵に必要な熱源をガス化溶融炉9の排熱を利用して得ることにより、全体の熱効率の向上を図ることができる。なお、余熱として、ボイラ排ガス顕熱、タービン抽気、タービン排気等が挙げられる。   By obtaining the heat source necessary for the methane fermentation using the exhaust heat of the gasification melting furnace 9, the overall thermal efficiency can be improved. The residual heat includes boiler exhaust gas sensible heat, turbine extraction, turbine exhaust, and the like.

タービン排気は他に利用することができないため、プラント全体の熱効率を上げるためにはタービン排気の利用が効果的である。   Since turbine exhaust cannot be used elsewhere, use of turbine exhaust is effective in increasing the thermal efficiency of the entire plant.

また、本発明のの高含水廃棄物の処理方法に用いるガス化溶融炉9およびメタン発酵処理装置3を有することにより、本発明の高含水廃棄物を含んだ廃棄物の処理方法を実現する処理装置を提供することができる。   Moreover, the process which implement | achieves the processing method of the waste containing the high water content waste of this invention by having the gasification melting furnace 9 and the methane fermentation processing apparatus 3 used for the processing method of the high water content waste of this invention An apparatus can be provided.

図1に示すシャフト炉式の廃棄物ガス化溶融炉9に水分が70質量%のバイオマス1を30質量%まで乾燥した乾燥廃棄物とその他の廃棄物8を混合し、成型コークス、石灰石を装入し、上段羽口から空気を、下段送風口から酸素富化空気を吹込んで廃棄物を溶融処理した。いずれも上段送風量(空気)350Nm3/h、下段送風量(空気)250Nm3/h、酸素を富化するために、下段送酸量(純酸素)60Nm3/hとし、下段羽口での送風は酸素濃度36.3%の一定条件、また、高炉コークス及び中空筒状炭化物の使用量を40kg/廃棄物tとした。尚、廃棄物は、K市で排出される一般都市ごみを使用した。   The shaft furnace waste gasification and melting furnace 9 shown in Fig. 1 is mixed with dry waste obtained by drying biomass 1 with a moisture content of 70% by mass to 30% by mass and other wastes 8, and then formed with coke and limestone. The waste was melted by blowing air from the upper tuyere and oxygen-enriched air from the lower vent. In all cases, the upper air flow rate (air) 350Nm3 / h, the lower air flow rate (air) 250Nm3 / h, and the oxygen content in the lower air flow (pure oxygen) 60Nm3 / h to enrich the oxygen. Constant conditions with an oxygen concentration of 36.3%, and the amount of blast furnace coke and hollow cylindrical carbide used were 40 kg / waste t. As waste, general municipal waste discharged in K city was used.

試験の結果、本発明の高含水廃棄物を含んだ廃棄物の処理方法によれば水分が70質量%の食品廃棄物、汚泥、泥炭などの含水率の高い廃棄物に含まれる水の蒸発潜熱を回収し、高水分廃棄物のもつエネルギーを高効率で回収することができるうえ、排水処理に必要な薬品類の消費量を低減できることが確認できた。   As a result of the test, according to the method for treating a waste containing a high water content waste according to the present invention, the latent heat of evaporation of water contained in a high water content waste such as food waste, sludge, peat and the like having a moisture content of 70% by mass It was confirmed that the energy of high-moisture waste can be recovered with high efficiency and the consumption of chemicals necessary for wastewater treatment can be reduced.

なお、本実施例は充填層式の廃棄物溶融炉について述べたが、流動式のコークスベッド式溶融炉やキュポラ等コークスを使う溶融炉への適用も可能である。また、コークス以外の燃料(LPG、天然ガス、灯油等)を溶融熱源として使用する炉への適用も妨げない。   In this embodiment, the packed bed type waste melting furnace has been described. However, the present invention can be applied to a fluid type coke bed type melting furnace and a melting furnace using coke such as a cupola. Further, application to a furnace that uses fuel other than coke (LPG, natural gas, kerosene, etc.) as a melting heat source is not hindered.

本発明の高含水廃棄物を含んだ廃棄物の処理方法におけるガス化溶融炉とメタン発酵の組み合わせを例示する図である。It is a figure which illustrates the combination of the gasification melting furnace and methane fermentation in the processing method of the waste containing the highly water-containing waste of this invention. 本発明の高含水廃棄物を含んだ廃棄物の処理方法におけるメタンガスのその他の利用方法を例示する図である。It is a figure which illustrates the other utilization method of the methane gas in the processing method of the waste containing the highly water-containing waste of this invention. 本発明の高含水廃棄物を含んだ廃棄物の処理方法における下水汚泥の分離処理を例示する図である。It is a figure which illustrates the separation process of the sewage sludge in the processing method of the waste containing the highly water-containing waste of this invention. 本発明の高含水廃棄物を含んだ廃棄物の処理方法における排水の利用を例示する図である。It is a figure which illustrates utilization of the waste_water | drain in the processing method of the waste containing the highly water-containing waste of this invention. 本発明の高含水廃棄物を含んだ廃棄物の処理方法における排水処理の共用を例示する図である。It is a figure which illustrates sharing of the waste_water | drain process in the processing method of the waste containing the highly water-containing waste of this invention. 本発明の高含水廃棄物を含んだ廃棄物の処理方法における余熱利用を例示する図である。It is a figure which illustrates the utilization of the residual heat in the processing method of the waste containing the highly water-containing waste of this invention.

符号の説明Explanation of symbols

1 高含水バイオマス
2 前処理装置
3 メタン発酵装置
4 脱水装置
5 乾燥装置
6 有機排水処理
7 ガス処理
8 廃棄物
9 ガス化溶融炉
9´ガス化炉
10 燃焼炉
10´2次燃焼炉
11 ボイラ
12 節炭器
13 減温塔
14 脱気器
15 バグフィルタ
16 誘引通風機
17 触媒反応塔
18 煙突
19 過熱器
19´独立過熱器
20 蒸気タービン
21 復水器
22 復水タンク
1 High water content biomass
2 Pre-treatment device 3 Methane fermentation device 4 Dehydration device 5 Drying device 6 Organic wastewater treatment 7 Gas treatment 8 Waste 9 Gasification melting furnace 9 'Gasification furnace 10 Combustion furnace 10' Secondary combustion furnace 11 Boiler 12 Carbon-saving device 13 Decooler 14 Deaerator 15 Bag filter 16 Induction fan 17 Catalytic reactor 18 Chimney 19 Superheater 19 ′ Independent superheater 20 Steam turbine 21 Condenser 22 Condensate tank

Claims (11)

一般廃棄物を含む有機性廃棄物をガス化溶融炉で処理する廃棄物の処理方法において、
食品廃棄物や汚泥等の含水率の高い有機性バイオマスとその他の廃棄物とを分離し、含水率の高い有機性バイオマスをメタン発酵処理によりメタンガスと消化汚泥および排水に分離し、
前記消化汚泥は水分を低減した上でその他の有機性廃棄物と混合することによりガス化溶融炉にて処理する廃棄物の水分量を低減し、
前記メタン発酵によって得られたメタンガスの全量もしくは一部を酸素もしくは酸素付加空気およびガス化溶融炉の後段で採取された可燃性ダストと共にガス化溶融炉の羽口に吹き込むと共に、前記メタン発効処理によって副生する排水の全量もしくは一部をガス化溶融炉の後段に設置する燃焼炉に吹き込んで無害化することを特徴とする、高含水廃棄物を含んだ廃棄物の処理方法。
In a waste processing method of processing organic waste including general waste in a gasification melting furnace,
Separate organic biomass with high water content such as food waste and sludge from other waste, separate organic biomass with high water content into methane gas, digested sludge and wastewater by methane fermentation treatment,
The digested sludge reduces the moisture content of the waste to be treated in the gasification melting furnace by mixing with other organic waste after reducing the moisture,
The whole or part of the methane gas obtained by the methane fermentation is blown into the tuyere of the gasification melting furnace together with oxygen or oxygen-added air and combustible dust collected after the gasification melting furnace, and by the methane effecting treatment A method for treating waste containing highly water-containing waste, characterized in that all or part of the wastewater produced as a by-product is blown into a combustion furnace installed downstream of the gasification melting furnace to make it harmless.
前記ガス化溶融炉をシャフト式ガス化炉とし、前記メタン発酵によって得られたメタンガスを可燃性ガスと共に羽口に吹き込むとともに、余剰分をガスエンジンで発電する若しくはガス化溶融炉の廃熱ボイラ発電システムに付随する外部過熱器の熱源として利用することを特徴とする、請求項1に記載の高含水廃棄物を含んだ廃棄物の処理方法。   The gasification melting furnace is a shaft type gasification furnace, and the methane gas obtained by the methane fermentation is blown into the tuyere together with the combustible gas, and the surplus is generated by a gas engine, or the waste heat boiler power generation of the gasification melting furnace 2. The method for treating waste containing highly water-containing waste according to claim 1, wherein the waste is used as a heat source of an external superheater attached to the system. 前記ガス化溶融炉をシャフト式ガス化炉とし、該ガス化炉へ投入する水分量を10から40%に調整することを特徴とする、請求項1または請求項2に記載の高含水廃棄物を含んだ廃棄物の処理方法。   The highly water-containing waste according to claim 1 or 2, wherein the gasification melting furnace is a shaft type gasification furnace, and the amount of water input to the gasification furnace is adjusted to 10 to 40%. Waste disposal method. 前記消化汚泥の含水率の低減方法として好気性発酵を用いることを特徴とする、請求項1〜3のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。   An aerobic fermentation is used as a method for reducing the moisture content of the digested sludge. The method for treating waste containing a highly water-containing waste according to any one of claims 1 to 3. 前記高含水廃棄物のうち、メタンガスの発生率の高い厨芥類をメタン発酵し、メタンガス発生率の低い下水汚泥、し尿汚泥とメタン発酵残渣のいずれかを好気性発酵による熱で乾燥させることを特徴とする、請求項1〜4のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。   Among the high water-containing wastes, methane fermentation is performed on moss having a high methane gas generation rate, and any one of sewage sludge, human waste sludge and methane fermentation residue having a low methane gas generation rate is dried by heat from aerobic fermentation. The processing method of the waste containing the highly water-containing waste as described in any one of Claims 1-4. ごみピットの底部に滞留するごみ汚水をメタン発酵の原料若しくはメタン発酵処理に必要な添加水として利用することを特徴とする、請求項1〜5のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。   The highly water-containing waste according to any one of claims 1 to 5, wherein the waste sewage staying at the bottom of the waste pit is used as a raw material for methane fermentation or as additional water necessary for methane fermentation treatment. Disposal method of included waste. 前記ガス化溶融炉から出る排水をメタン発酵に必要な添加水として利用することを特徴とする、請求項1〜6のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。   The wastewater discharged from the gasification melting furnace is used as an additional water necessary for methane fermentation, The method for treating waste containing highly water-containing waste according to any one of claims 1 to 6, . 前記メタン発酵処理にて発生する排水を1次処理し、ガス化溶融炉から発生する排水と混合して排水処理することを特徴とする、請求項1〜7のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。       The effluent generated in the methane fermentation treatment is subjected to a primary treatment, mixed with the effluent generated from a gasification melting furnace, and treated as a effluent. A method for treating waste containing hydrous waste. 前記メタン発酵に必要な熱源をガス化溶融炉の排熱を利用して得ることを特徴とする、請求項1〜8のいずれか一項に記載の高含水廃棄物を含んだ廃棄物の処理方法。   The treatment of waste containing high water content waste according to any one of claims 1 to 8, wherein a heat source necessary for the methane fermentation is obtained by using exhaust heat of a gasification melting furnace. Method. 前記排熱が蒸気タービン排気であることを特徴とする、請求項9に記載の高含水廃棄物を含んだ廃棄物の処理方法。   10. The method for treating waste containing highly water-containing waste according to claim 9, wherein the exhaust heat is steam turbine exhaust. 請求項1〜10のいずれか一項に記載の高含水廃棄物の処理方法に用いるガス化溶融炉およびメタン発酵処理装置を有することを特徴とする、高含水廃棄物を含んだ廃棄物の処理装置。   It has a gasification melting furnace used for the processing method of the highly water-containing waste as described in any one of Claims 1-10, and a methane fermentation processing apparatus, The processing of the waste containing the high water-containing waste characterized by the above-mentioned. apparatus.
JP2008332218A 2008-12-26 2008-12-26 Treatment method of waste containing highly hydrous waste and treatment device used for the same Pending JP2010149079A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008332218A JP2010149079A (en) 2008-12-26 2008-12-26 Treatment method of waste containing highly hydrous waste and treatment device used for the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008332218A JP2010149079A (en) 2008-12-26 2008-12-26 Treatment method of waste containing highly hydrous waste and treatment device used for the same

Publications (1)

Publication Number Publication Date
JP2010149079A true JP2010149079A (en) 2010-07-08

Family

ID=42568779

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2008332218A Pending JP2010149079A (en) 2008-12-26 2008-12-26 Treatment method of waste containing highly hydrous waste and treatment device used for the same

Country Status (1)

Country Link
JP (1) JP2010149079A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101209855B1 (en) 2011-01-19 2012-12-20 에이치투더블유티이 주식회사 Steam generation and waste gas treating apparatus using waste material
KR101334954B1 (en) * 2011-01-19 2013-11-29 에이치투더블유티이 주식회사 Steam supply and recovery system of boiler in sludge treating apparatus
JP2018108540A (en) * 2016-12-28 2018-07-12 株式会社神鋼環境ソリューション Waste treatment system and waste treatment method
JP2019214028A (en) * 2018-06-14 2019-12-19 三菱日立パワーシステムズ株式会社 Hydrothermal treatment apparatus, biomass fuel production plant, hydrothermal treatment method, and biomass fuel production method
CN115490411A (en) * 2022-11-21 2022-12-20 广东昕旺环保科技发展有限公司 Sludge treatment agent and sludge treatment process

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003275722A (en) * 2002-03-25 2003-09-30 Takuma Co Ltd System and method for treating waste
JP2007167782A (en) * 2005-12-22 2007-07-05 Nippon Steel Engineering Co Ltd Waste treatment method
JP2008212860A (en) * 2007-03-06 2008-09-18 Kawasaki Plant Systems Ltd Waste disposal facility
JP2008253963A (en) * 2007-04-09 2008-10-23 Kawasaki Plant Systems Ltd Treating method and treatment facility of waste and sewage

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003275722A (en) * 2002-03-25 2003-09-30 Takuma Co Ltd System and method for treating waste
JP2007167782A (en) * 2005-12-22 2007-07-05 Nippon Steel Engineering Co Ltd Waste treatment method
JP2008212860A (en) * 2007-03-06 2008-09-18 Kawasaki Plant Systems Ltd Waste disposal facility
JP2008253963A (en) * 2007-04-09 2008-10-23 Kawasaki Plant Systems Ltd Treating method and treatment facility of waste and sewage

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101209855B1 (en) 2011-01-19 2012-12-20 에이치투더블유티이 주식회사 Steam generation and waste gas treating apparatus using waste material
KR101334954B1 (en) * 2011-01-19 2013-11-29 에이치투더블유티이 주식회사 Steam supply and recovery system of boiler in sludge treating apparatus
JP2018108540A (en) * 2016-12-28 2018-07-12 株式会社神鋼環境ソリューション Waste treatment system and waste treatment method
JP2019214028A (en) * 2018-06-14 2019-12-19 三菱日立パワーシステムズ株式会社 Hydrothermal treatment apparatus, biomass fuel production plant, hydrothermal treatment method, and biomass fuel production method
CN115490411A (en) * 2022-11-21 2022-12-20 广东昕旺环保科技发展有限公司 Sludge treatment agent and sludge treatment process

Similar Documents

Publication Publication Date Title
USRE45869E1 (en) Slurry dewatering and conversion of biosolids to a renewable fuel
US20060260190A1 (en) Method and apparatus for treating organic matter
JP2009028672A (en) Treatment method of high water-content waste and treatment apparatus
JP4081102B2 (en) Waste complex treatment facility
JP2007167782A (en) Waste treatment method
JPH10156314A (en) Method of recovering energy from waste
JP2005272530A (en) Biomass power generation system
JP2009045612A (en) Waste recycling method and recycling facility
JP2008212860A (en) Waste disposal facility
JP2005319373A (en) Method and apparatus for converting sludge into fuel
JP2010149079A (en) Treatment method of waste containing highly hydrous waste and treatment device used for the same
JP2006348302A (en) Method and apparatus for converting sludge into fuel
JP2008221142A (en) Treatment method of waste and treatment equipment thereof
JP5036608B2 (en) Gasification generator
JP2004051745A (en) System of gasifying biomass
JP2012107110A (en) Method for treating gas-treatment drainage, gasification apparatus of carbonaceous material, and method for treating carbonaceous material
JP2007002825A (en) Waste power generation method
TW202308750A (en) Hydrogen production system
JP2010247111A (en) Sludge drying system
CN1863738A (en) Method and apparatus for treating organic matter
JP4089079B2 (en) Waste treatment method and waste treatment system
JP2008104973A (en) Method and system for treating waste biomass
JP3748157B2 (en) Waste treatment system
CN216584888U (en) Garbage carbonization treatment system based on thermal cracking
Peltola et al. An advanced process for thermal treatment of municipal sewage sludge

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20110502

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20111209

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20120131

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20120612