JP2000202416A - Treatment of garbage/combustible refuse not by means of incineration - Google Patents
Treatment of garbage/combustible refuse not by means of incinerationInfo
- Publication number
- JP2000202416A JP2000202416A JP5132199A JP5132199A JP2000202416A JP 2000202416 A JP2000202416 A JP 2000202416A JP 5132199 A JP5132199 A JP 5132199A JP 5132199 A JP5132199 A JP 5132199A JP 2000202416 A JP2000202416 A JP 2000202416A
- Authority
- JP
- Japan
- Prior art keywords
- garbage
- methane
- treatment
- gas
- organic fertilizer
- 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
Links
- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 34
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 56
- 238000000034 method Methods 0.000 claims abstract description 22
- 238000000855 fermentation Methods 0.000 claims abstract description 18
- 230000004151 fermentation Effects 0.000 claims abstract description 16
- 238000002485 combustion reaction Methods 0.000 claims abstract description 12
- 239000003895 organic fertilizer Substances 0.000 claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 230000004720 fertilization Effects 0.000 claims abstract description 5
- 239000012535 impurity Substances 0.000 claims abstract description 5
- 239000000446 fuel Substances 0.000 claims abstract description 4
- 239000007787 solid Substances 0.000 claims abstract description 4
- 238000000197 pyrolysis Methods 0.000 claims description 23
- 239000010849 combustible waste Substances 0.000 claims description 22
- 239000000356 contaminant Substances 0.000 claims description 14
- 239000003337 fertilizer Substances 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 5
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 150000001247 metal acetylides Chemical class 0.000 claims description 5
- 239000002689 soil Substances 0.000 claims description 5
- 239000003516 soil conditioner Substances 0.000 abstract description 5
- 238000010792 warming Methods 0.000 abstract description 4
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract 1
- 239000002699 waste material Substances 0.000 description 9
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 7
- 239000004449 solid propellant Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 239000010850 non-combustible waste Substances 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 238000010564 aerobic fermentation Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000013067 intermediate product Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000010819 recyclable waste Substances 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000007033 dehydrochlorination reaction Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Processing Of Solid Wastes (AREA)
- Soil Conditioners And Soil-Stabilizing Materials (AREA)
- Fertilizers (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】この発明は焼却によらない生
ごみ・可燃ごみの処理方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating garbage and combustible waste without incineration.
【０００２】[0002]
【従来の技術】生ごみ・可燃ごみは従来ごみ焼却炉で焼
却し、焼却灰などの焼却残渣は最終処分場へ埋め立てら
れていた。2. Description of the Related Art Conventionally, garbage and combustible waste have been incinerated in a refuse incinerator, and incineration residues such as incineration ash have been landfilled at a final disposal site.
【０００３】近年、廃棄物を極力有効に利用する目的
で、生ごみを好気性発酵処理し有機肥料とし、その他の
可燃ごみは乾燥・成型して固形燃料化するか、生ごみ・
可燃ごみをまとめて固形燃料化する処理法が多くなり、
得られた固形燃料は燃焼炉によりエネルギー回収され、
燃焼残渣は埋め立てられる。[0003] In recent years, in order to utilize waste as effectively as possible, garbage is subjected to aerobic fermentation treatment to produce organic fertilizer, and other combustible refuse is dried and molded into solid fuel,
There are many treatment methods to convert combustible waste into solid fuel,
The obtained solid fuel is energy recovered by the combustion furnace,
Combustion residues are landfilled.
【０００４】最近、ダイオキシン対策および最終埋め立
て量削減対策などを目的に、生ごみ・可燃ごみのみでな
く不燃ごみをも加えて、高温燃焼し、燃焼残渣は溶融し
スラグとして回収、路盤材などに再利用する方法が開発
されている。Recently, for the purpose of measures against dioxin and reduction of the amount of final landfill, not only garbage and combustible waste but also non-combustible waste are added to burn at high temperature, and the combustion residue is melted and collected as slag, and used as roadbed material. Reuse methods have been developed.
【０００５】[0005]
【発明が解決しようとする課題】従来の方法は以下のの
ような地球環境上のいろいろな問題をかかえている。The conventional method has various problems on the global environment as follows.
【０００６】生ごみ・可燃ごみのごみ焼却炉による焼却
においては、多量の焼却残渣の埋め立て処分が必要であ
る。また、焼却時には有害物質であるダイオキシンを発
生する危険性があり、地球温暖化の原因であるＣＯ２が
多量発生する。In incineration of garbage and combustible waste by a refuse incinerator, it is necessary to landfill a large amount of incineration residues. Further, at the time of incineration there is a risk of generating dioxins are harmful substances, CO 2 is the cause of global warming a large amount occurs.
【０００７】固形燃料化する方法においても、固形燃料
は最終的には燃焼しエネルギー回収されるが、その際焼
却残渣が発生し埋め立て処分が必要であり、焼却時のダ
イオキシン発生の危険性および多量のＣＯ２発生が問題
である。In the method of converting to solid fuel, the solid fuel is finally burned and energy is recovered. At that time, incineration residues are generated and must be disposed of in a landfill. CO 2 generation is an issue of.
【０００８】高温燃焼・溶融法においてはダイオキシン
発生抑制、焼却残渣の再利用が可能であるが、多量のＣ
Ｏ２の発生は避けられない。加えて、処理するごみの必
要熱量が約１７００ｋｃａｌ／ｋｇ以上という制約があ
り、ごみの選別資源化の流れに反した面をかかえてい
る。In the high-temperature combustion / melting method, it is possible to suppress the generation of dioxin and to reuse incineration residues.
The generation of O 2 can not be avoided. In addition, there is a restriction that the required amount of heat of the refuse to be treated is about 1700 kcal / kg or more, which is inconsistent with the flow of refuse sorting resources.
【０００９】このように従来の生ごみ・可燃ごみの処理
方法では、多量のＣＯ２の発生、ダイオキシン発生の危
険性、多量の埋め立て処分など地球環境上の問題をかか
えている。本発明はこのような問題点の解決をはかるた
めになされたものである。As described above, the conventional methods for treating garbage and combustible waste have problems on the global environment such as generation of a large amount of CO 2 , danger of generating dioxin, and disposal of a large amount of landfill. The present invention has been made to solve such a problem.
【００１０】[0010]
【課題を解決するための手段】（イ）生ごみ（１）はメ
タン発酵装置（１Ａ）によりメタン発酵処理をおこな
い、処理残渣は肥料化装置（１Ｂ）により肥料化処理
後、夾雑物（１ｂ）を分離して有機肥料（１ａ）とす
る。 （ロ）生ごみ以外の可燃ごみ（２）は熱分解炉（２Ａ）
において熱分解処理し、固形物残渣から金属・ガレキな
どの夾雑物（２ｂ）を分離して炭化物（２ａ）とする。 （ハ）（イ）で得られる有機肥料（１ａ）と（ロ）で得
られる炭化物（２ａ）を混合し、性能の高い土壌改良材
（３）とする。 （ニ）メタン発酵装置（１Ａ）の加熱用温風（３ａ）お
よび熱分解炉（２Ａ）の加熱用熱風（３ｂ）の熱源は、
メタン発酵装置（１Ａ）で発生するメタン（１ｃ）およ
び熱分解炉（２Ａ）で発生する熱分解ガス（２ｃ）を燃
料とするガス燃焼炉（３Ａ）により供給される。Means for Solving the Problems (a) Garbage (1) is subjected to methane fermentation by a methane fermentation device (1A), and the treated residue is subjected to a fertilizer treatment by a fertilizer treatment device (1B), and then to a contaminant (1b). ) Is separated into an organic fertilizer (1a). (B) Combustible waste other than garbage (2) is pyrolysis furnace (2A)
, And the impurities (2b) such as metal and rubble are separated from the solid residue to form carbides (2a). (C) The organic fertilizer (1a) obtained in (a) and the carbide (2a) obtained in (b) are mixed to obtain a high-performance soil improving material (3). (D) The heat source of the hot air (3a) for heating of the methane fermentation apparatus (1A) and the hot air (3b) for heating of the pyrolysis furnace (2A) are as follows:
The gas is supplied from a gas combustion furnace (3A) using methane (1c) generated in the methane fermentation apparatus (1A) and pyrolysis gas (2c) generated in the pyrolysis furnace (2A) as fuel.
【００１１】[0011]
【発明の実施形態】本発明の実施形態は図１の処理フロ
ーに示すとおりである。DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention is as shown in the processing flow of FIG.
【００１２】[0012]
【実施例】本発明による生ごみ・可燃ごみの具体的な処
理方法の例を図２により説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An example of a specific method for treating garbage and combustible waste according to the present invention will be described with reference to FIG.
【００１３】生ごみ（１）はメタン発酵装置（１Ａ）に
より嫌気性発酵処理され、メタン（１ｃ）が発生し回収
される。生ごみの嫌気性発酵は５５〜６５℃の高温発酵
が望ましい。The garbage (1) is subjected to an anaerobic fermentation treatment by a methane fermentation apparatus (1A) to generate and collect methane (1c). For anaerobic fermentation of garbage, high-temperature fermentation at 55 to 65 ° C is desirable.
【００１４】また、生ごみのメタン発酵を促進するた
め、生ごみに下水汚泥（４）ほかの有機性汚泥などを混
合することも可能である。In order to promote methane fermentation of garbage, garbage can be mixed with sewage sludge (4) and other organic sludge.
【００１５】メタン発酵後の生ごみ類は肥料化装置（１
Ｂ）により肥料化処理される。肥料化処理は好気性発酵
または乾燥工程を含み、得られる中間製品は水分がおよ
そ２０％以下となる。The garbage after methane fermentation is converted into a fertilizer (1)
B) is fertilized. The fertilization process involves an aerobic fermentation or drying step, and the resulting intermediate product has less than about 20% moisture.
【００１６】中間製品は生ごみに混入した夾雑物（１
ｂ）を含んでおり、これを選別分離して有機肥料（１
ａ）が得られる。Intermediate products are contaminants (1.
b), which is separated and separated into organic fertilizers (1).
a) is obtained.
【００１７】夾雑物（１ｂ）に含まれたプスチック片な
どの可燃物（１ｂ１）は熱分解炉（２Ａ）へ装入され、
少量発生するガレキ（１ｂ２）は最終処分場（５）へ埋
め立てられる。The combustibles (1b 1 ) such as plastic pieces contained in the contaminants (1b) are charged into the pyrolysis furnace (2A),
A small amount of rubble (1b 2 ) is landfilled at the final disposal site (5).
【００１８】生ごみ以外の可燃ごみ（２）は熱分解炉
（２Ａ）により熱分解される。熱分解炉では無酸素の状
態で５００℃以下の温度で処理される。Combustible waste (2) other than garbage is pyrolyzed by a pyrolysis furnace (2A). In a pyrolysis furnace, treatment is performed at a temperature of 500 ° C. or less in an oxygen-free state.
【００１９】可燃ごみ中のガス化成分は熱分解ガス（２
ｃ）となり、その他の炭素分の大部分は炭化物となる。
熱分解後の固形残渣中には可燃ごみに混入した夾雑物
（２ｂ）が含まれるが、これを選別分離して炭化物（２
ａ）が得られる。The gasification component in the combustible waste is pyrolysis gas (2
c), and most of the other carbon components are carbides.
The solid residue after pyrolysis contains impurities (2b) mixed in combustible waste, which are separated and separated into carbides (2b).
a) is obtained.
【００２０】夾雑物中の金属類（２ｂ１）は非酸化、非
溶融状態であり、資源物（６）として回収され、夾雑物
中の少量のガレキ（２ｂ２）は最終処分場（５）へ埋め
立てられる。The metals (2b 1 ) in the contaminants are in a non-oxidized and non-molten state and are recovered as resources (6), and a small amount of rubble (2b 2 ) in the contaminants is disposed at the final disposal site (5). To landfill.
【００２１】得られる有機肥料（１ａ）と炭化物（２
ａ）を混合し、土壌改良材（３）とする。The obtained organic fertilizer (1a) and charcoal (2
a) is mixed to obtain a soil conditioner (3).
【００２２】この土壌改良材（３）は有機肥料（１ａ）
の肥料効果はもちろん、炭化物（２ａ）により土中の保
水性、肥料成分の保持性が良く、微生物の活性がはから
れ、さらに有機肥料の悪臭が抑制されるため極めて性能
の高い土壌改良材である。The soil conditioner (3) is an organic fertilizer (1a)
Not only the fertilizer effect of soil, but also carbon (2a) has good water retention in soil and good retention of fertilizer components, enhances the activity of microorganisms, and suppresses offensive odor of organic fertilizers. It is.
【００２３】生ごみ（１）のメタン発酵処理で発生する
メタン（１ｃ）は脱硫処理され、可燃ごみ（２）の熱分
解処理で発生する熱分解ガス（２ｃ）は脱硫、脱塩化水
素処理される。The methane (1c) generated in the methane fermentation of the garbage (1) is desulfurized, and the pyrolysis gas (2c) generated in the pyrolysis of the combustible waste (2) is desulfurized and dehydrochlorinated. You.
【００２４】脱硫処理されたメタン（１ｃ）および脱
硫、脱塩化水素処理された熱分解ガス（２ｃ）を燃料と
したガス燃焼炉（３Ａ）によって、メタン発酵用の温風
（３ａ）および熱分解用の熱風（３ｂ）を加熱する。Hot air (3a) for methane fermentation and pyrolysis are produced by a gas combustion furnace (3A) using methane (1c) subjected to desulfurization treatment and pyrolysis gas (2c) subjected to desulfurization and dehydrochlorination treatment as fuel. Heating hot air (3b).
【００２５】ガス燃焼炉（３Ａ）で得られるの余剰エネ
ルギーはコージェネレーションなどの熱利用が可能であ
る。The surplus energy obtained in the gas combustion furnace (3A) can be used for heat such as cogeneration.
【００２６】この実施例においては、生ごみ・可燃ごみ
中の炭素分の多くは、地球温暖化の原因であるＣＯ２に
ならずに、炭化物および有機肥料となり最終的には土壌
改良材として土中に長期保存される。したがって、実施
例のＣＯ２発生総量は従来の処理法に比べて著しく少な
い。In this embodiment, much of the carbon content in garbage and combustible waste is converted into carbides and organic fertilizers, instead of CO 2 , which causes global warming. It is stored for a long time. Therefore, the total amount of generated CO 2 in Examples is significantly smaller than that of the conventional treatment method.
【００２７】熱分解炉（２Ａ）は無酸素状態で操業する
ためダイオキシンの発生の危険性は低い。ガス燃焼炉
（３Ａ）は燃焼管理が容易であり、Ｃｕなどの触媒活性
な金属を含むダストの存在もなく、ダイオキシン抑制が
しやすい。Since the pyrolysis furnace (2A) operates in an oxygen-free state, the risk of dioxin generation is low. In the gas combustion furnace (3A), combustion management is easy, there is no dust containing a catalytically active metal such as Cu, and dioxin can be easily suppressed.
【００２８】肥料化装置（１Ｂ）からの夾雑物（１ｂ）
中のガレキ（１ｂ２）および熱分解炉（２Ａ）からの夾
雑物（２ｂ）中のガレキ（２ｂ２）は埋め立てられる
が、その量は従来の処理法に比べて大幅に減少してい
る。Contaminants (1b) from the fertilizer (1B)
The rubble (1b 2 ) in the inside and the rubble (2b 2 ) in the contaminants (2b) from the pyrolysis furnace (2A) are landfilled, but the amount is greatly reduced as compared with the conventional treatment method.
【００２９】また、これら少量のガレキを小型炉で溶融
処理し資源化することもできる。Further, these small amounts of rubble can be melted in a small furnace and recycled.
【００３０】本発明の生ごみ・可燃ごみの処理法によれ
ば、ごみ焼却炉は不用である。According to the method for treating food waste and combustible waste according to the present invention, a waste incinerator is unnecessary.
【００３１】図３はごみ全体の処理において本発明を組
み込んだ例である。生ごみ・可燃ごみの処理法は上述の
実施例と同様である。FIG. 3 shows an example in which the present invention is incorporated in the entire refuse processing. The method of treating garbage and combustible waste is the same as in the above-described embodiment.
【００３２】不燃ごみ・粗大ごみ・資源ごみ（７）は資
源化センター（７Ａ）へ搬入し、修理・破砕・選別工程
を経て、家具、家電品などの再使用可能な品物（７ａ）
は再使用（８）される。The non-combustible waste, oversized waste and recyclable waste (7) are transported to the Recycling Center (7A), undergo repair, crushing, and sorting processes, and can be reused (furniture, home appliances, etc.) (7a).
Are reused (8).
【００３３】再利用の条件をみたす缶類・ビン類・紙・
プラスチックなどの資源化可能品（７ｂ）は資源物
（６）とし回収される。[0033] Cans, bottles, paper,
Recyclable products (7b) such as plastics are collected as recyclables (6).
【００３４】木片類、再利用の条件をみたさない廃プラ
スチック類・紙類などの可燃物（７ｃ）は熱分解炉（２
Ａ）へ装入される。Combustibles (7c) such as wood chips and waste plastics and papers which do not meet the conditions for reuse are converted to a pyrolysis furnace (2).
A).
【００３５】最後に残るガレキ（７ｄ）は最終処分場へ
埋め立てられる。The last rubble (7d) is landfilled at the final disposal site.
【００３６】このごみ全体の処理法の例においても本発
明の生ごみ・可燃ごみの処理法を組み込んだ結果、ごみ
焼却炉は不用であり、ＣＯ２発生総量の削減、ダイオキ
シン発生の抑制、埋め立て量の減少がはかられている。As a result of incorporating the method for treating garbage and combustible waste according to the present invention also in the example of the method for treating waste as a whole, a waste incinerator is unnecessary, reducing the total amount of generated CO 2 , suppressing the generation of dioxin, and landfilling. The amount has been reduced.
【００３７】[0037]
【発明の効果】以上説明したように本発明による焼却に
よらない生ごみ・可燃ごみの処理法によれば、ごみ焼却
炉は不用であり、ごみ中の炭素分の多くは有機肥料およ
び炭化物となり、地球温暖化の原因となるＣＯ２となら
ずに土中に保存され、土壌改良材として作用する。As described above, according to the method for treating garbage and combustible waste which is not incinerated according to the present invention, a waste incinerator is unnecessary, and most of the carbon content in the waste is converted into organic fertilizer and carbide. However, it is stored in the soil without becoming CO 2 causing global warming, and acts as a soil conditioner.
【００３８】本法によればＣＯ２総発生量は従来の方法
に比べ著しく少ない。According to this method, the total amount of generated CO 2 is significantly smaller than that of the conventional method.
【００３９】本法によればダイオキシン抑制も可能であ
る。According to the present method, dioxin can be suppressed.
【００４０】本法によれば最終処分場への埋め立ての量
も大幅に減少する。According to the present method, the amount of landfill at the final disposal site is also greatly reduced.
【００４１】このように本発明の方法により、生ごみ・
可燃ごみ処理による環境への負荷を著しく低減すること
ができる。As described above, according to the method of the present invention, garbage
The burden on the environment due to combustible waste disposal can be significantly reduced.
【図１】本発明による焼却によらない生ごみ・可燃ごみ
の処理フローFIG. 1 is a flow chart of processing garbage and combustible waste without incineration according to the present invention.
【図２】本発明による焼却によらない生ごみ・可燃ごみ
の処理方法の具体的な例FIG. 2 is a specific example of a method of treating garbage and combustible waste without incineration according to the present invention.
【図３】ごみ全体の処理において本発明を組み込んだ例FIG. 3 shows an example in which the present invention is incorporated in the entire garbage disposal.
１ 生ごみ １Ａ メタン発酵装置 １Ｂ 肥料化装置 １ａ 有機肥料 １ｂ 夾雑物（肥料化後） １ｂ１ 夾雑物中の可燃物 １ｂ２ 夾雑物中のガレキ １ｃ メタン ２ 可燃ごみ ２Ａ 熱分解炉 ２ａ 炭化物 ２ｂ 夾雑物（炭化後） ２ｂ１ 夾雑物中の金属類 ２ｂ２ 夾雑物中のガレキ ２ｃ 熱分解ガス ３ 土壌改良材 ３Ａ ガス燃焼炉 ３ａ メタン発酵装置用温風 ３ｂ 熱分解炉用熱風 ４ 下水汚泥 ５ 最終処分場 ６ 資源物 ７ 不燃ごみ、粗大ごみ、資源ごみ ７Ａ 資源化センター ７ａ 資源化センターからの再使用品 ７ｂ 資源化センターからの資源化可能品 ７ｃ 資源化センターからの可燃物 ７ｄ 資源化センターからのガレキ ８ 再利用1 Garbage 1A Methane fermenter 1B Fertilizer 1a Organic fertilizer 1b Contaminants (after fertilization) 1b 1 Combustibles in contaminants 1b 2 Garbage in contaminants 1c Methane 2 Combustible garbage 2A Pyrolysis furnace 2a Carbonized 2b Contaminants Material (after carbonization) 2b 1 Metals in contaminants 2b 2 Rubble in contaminants 2c Pyrolysis gas 3 Soil conditioner 3A Gas combustion furnace 3a Hot air for methane fermentation equipment 3b Hot air for pyrolysis furnace 4 Sewage sludge 5 Final Disposal site 6 Recyclable materials 7 Non-combustible waste, oversized waste, recyclable waste 7A Recycling center 7a Reusable products from the recycling center 7b Recyclable products from the recycling center 7c Combustible materials from the recycling center 7d From the recycling center Rubble 8 reuse
───────────────────────────────────────────────────── 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） // Ｃ０９Ｋ 101:00 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) // C09K 101: 00
Claims (1)
Ａ）によりメタン発酵処理をおこない、処理残渣は肥料
化装置（１Ｂ）により肥料化処理後、夾雑物（１ｂ）を
分離して有機肥料（１ａ）とする。 （ロ）生ごみ以外の可燃ごみ（２）は熱分解炉（２Ａ）
において熱分解処理し、固形物残渣から金属・ガレキな
どの夾雑物（２ｂ）を分離して炭化物（２ａ）とする。 （ハ）（イ）で得られる有機肥料（１ａ）と（ロ）で得
られる炭化物（２ａ）を混合し、性能の高い土壌改良材
（３）とする。 （ニ）メタン発酵装置（１Ａ）の加熱用温風（３ａ）お
よび熱分解炉（２Ａ）の加熱用熱風（３ｂ）の熱源は、
メタン発酵装置（１Ａ）で発生するメタン（１ｃ）およ
び熱分解炉（２Ａ）で発生する熱分解ガス（２ｃ）を燃
料とするガス燃焼炉（３Ａ）により供給される。 以上のごとく構成された焼却によらない生ごみ・可燃ご
みの処理方法。(1) Garbage (1) is a methane fermentation device (1)
The methane fermentation treatment is performed according to A), and the treatment residue is subjected to the fertilization treatment by the fertilizer treatment device (1B), and then the contaminant (1b) is separated into the organic fertilizer (1a). (B) Combustible waste other than garbage (2) is pyrolysis furnace (2A)
, And the impurities (2b) such as metal and rubble are separated from the solid residue to form carbides (2a). (C) The organic fertilizer (1a) obtained in (a) and the carbide (2a) obtained in (b) are mixed to obtain a high-performance soil improving material (3). (D) The heat source of the hot air (3a) for heating of the methane fermentation apparatus (1A) and the hot air (3b) for heating of the pyrolysis furnace (2A) are as follows:
The gas is supplied from a gas combustion furnace (3A) using methane (1c) generated in the methane fermentation apparatus (1A) and pyrolysis gas (2c) generated in the pyrolysis furnace (2A) as fuel. The disposal method of garbage and combustible waste not based on incineration, configured as described above.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5132199A JP2000202416A (en) | 1999-01-19 | 1999-01-19 | Treatment of garbage/combustible refuse not by means of incineration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5132199A JP2000202416A (en) | 1999-01-19 | 1999-01-19 | Treatment of garbage/combustible refuse not by means of incineration |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000202416A true JP2000202416A (en) | 2000-07-25 |
Family
ID=12883662
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5132199A Pending JP2000202416A (en) | 1999-01-19 | 1999-01-19 | Treatment of garbage/combustible refuse not by means of incineration |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000202416A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002263617A (en) * | 2001-03-07 | 2002-09-17 | Ryoichi Okamoto | Waste treatment equipment |
| WO2003016434A2 (en) * | 2001-08-16 | 2003-02-27 | Hans-Joachim Boltersdorf | Method for depleting carbon dioxide and for extracting energy |
| JP2009520481A (en) * | 2005-12-21 | 2009-05-28 | ソレイン セッチニ アムビエンテ スカ ソシエタ ペル アチオニ | A method for obtaining biologically stabilized forestland substrate from an integrated cycle of municipal solid waste treatment |
| CN100586593C (en) * | 2008-04-01 | 2010-02-03 | 同济大学 | Method for inhibiting consumer waste filling field methane discharging with calcium carbide |
| CN106077052A (en) * | 2016-08-19 | 2016-11-09 | 佛山市凯特科科技有限公司 | Life refuse processing method |
| CN109226213A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
| CN109226172A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
| CN109226171A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
| CN109226173A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
-
1999
- 1999-01-19 JP JP5132199A patent/JP2000202416A/en active Pending
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002263617A (en) * | 2001-03-07 | 2002-09-17 | Ryoichi Okamoto | Waste treatment equipment |
| WO2003016434A2 (en) * | 2001-08-16 | 2003-02-27 | Hans-Joachim Boltersdorf | Method for depleting carbon dioxide and for extracting energy |
| WO2003016434A3 (en) * | 2001-08-16 | 2003-05-15 | Hans-Joachim Boltersdorf | Method for depleting carbon dioxide and for extracting energy |
| JP2009520481A (en) * | 2005-12-21 | 2009-05-28 | ソレイン セッチニ アムビエンテ スカ ソシエタ ペル アチオニ | A method for obtaining biologically stabilized forestland substrate from an integrated cycle of municipal solid waste treatment |
| CN100586593C (en) * | 2008-04-01 | 2010-02-03 | 同济大学 | Method for inhibiting consumer waste filling field methane discharging with calcium carbide |
| CN106077052A (en) * | 2016-08-19 | 2016-11-09 | 佛山市凯特科科技有限公司 | Life refuse processing method |
| CN109226213A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
| CN109226172A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
| CN109226171A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
| CN109226173A (en) * | 2017-07-10 | 2019-01-18 | 湖南万容科技股份有限公司 | A kind of domestic garbage comprehensive recycling processing method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Hong et al. | Life cycle assessment of BMT-based integrated municipal solid waste management: Case study in Pudong, China | |
| CN101713304B (en) | Method for cycle power generation by carrying out wet decomposition pretreatment, dry distillation and gasification on domestic garbage | |
| Moharir et al. | Waste treatment processes/technologies for energy recovery | |
| CN1769397A (en) | Device and method for suppressing refuse end gas injurant using pyrolysis and aerification technology | |
| US7302897B2 (en) | MSW disposal process and apparatus using gasification | |
| CN107699294B (en) | Green island type urban and rural organic waste harmless recycling treatment process | |
| Wilson et al. | A comparative assessment of commercial technologies for conversion of solid waste to energy | |
| WO2008040396A1 (en) | Renewable energy recovery from msw and other wastes | |
| CN106433799A (en) | System and method for disposing household garbage | |
| JP2000202416A (en) | Treatment of garbage/combustible refuse not by means of incineration | |
| CN101829671A (en) | Clean energy utilization method for municipal solid wastes | |
| Reddy | Municipal solid waste–waste to energy conversion in India: an overview | |
| Dar et al. | Enhanced Landfill Mining Waste Valorization Techniques: A Methodological Review | |
| JP2001220274A (en) | Method for treating garbage and burnable trash | |
| Mohod et al. | Technological developments in the energy generation from municipal solid waste (landfill gas capture, combustion, pyrolysis and gasification) | |
| Dalal | Disambiguation of Municipal solid waste to Syngas in Ujjain District by Plasma Gasification Technique | |
| JP2005349392A (en) | Waste treatment system | |
| CN206143142U (en) | System for handle domestic waste | |
| JPH1130410A (en) | Disposing method for waste utilizing waste plastic gasification/ash melting | |
| CN111485049A (en) | Method for carrying out double-base reduction on DRI by using organic garbage as reducing agent | |
| WO2018185782A1 (en) | Gasifier for gasification of municipal solid waste | |
| Kazemi et al. | WASTE COGENERATION IN THE MIROSLAVA COMMUNE, IASI COUNTY-ROMANIA. | |
| JP2007216168A (en) | Method and apparatus for treating organic waste | |
| Filin et al. | Plasma Technologies as the Basis for the Development of Russian Waste Processing | |
| JP2004136184A (en) | Waste treatment system |