JP2004313957A - Disposal method and disposal apparatus for organic waste - Google Patents

Disposal method and disposal apparatus for organic waste Download PDF

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Publication number
JP2004313957A
JP2004313957A JP2003112240A JP2003112240A JP2004313957A JP 2004313957 A JP2004313957 A JP 2004313957A JP 2003112240 A JP2003112240 A JP 2003112240A JP 2003112240 A JP2003112240 A JP 2003112240A JP 2004313957 A JP2004313957 A JP 2004313957A
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Japan
Prior art keywords
organic waste
microorganisms
vessel
fermentation
heating
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Japanese (ja)
Inventor
Toyofusa Endo
豊房 遠藤
Sumio Ishikawa
住夫 石川
Masao Wada
正男 和田
Teruo Koyama
照雄 小山
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Nichizo Tech Inc
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Nichizo Tech Inc
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    • 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
    • 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
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • 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
    • Y02W30/40Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Abstract

<P>PROBLEM TO BE SOLVED: To provide a disposal apparatus of organic waste with simple constitution, performing respective disposal processes in optimum conditions. <P>SOLUTION: In the disposal apparatus 1, a microorganism group is mixed into the organic waste, agitated in a disposal vessel 4 to be fermented. The apparatus is provided with agitator blades 24 in the disposal vessel 4, a heating device 5 heating the organic waste charged in the vessel 4, and a decompression device 7 decompressing the vessel 4 by sucking gas inside the vessel 4. A mixture of aerobic microorganisms with anaerobic microorganisms is used as the microorganism group. The anaerobic microorganisms are activated by decompressing the vessel 4 by the decompression device 7 when drying the organic waste by heating, and the aerobic microorganisms are activated by bringing the vessel 4 to have atmospheric pressure, when fermenting the organic waste by heating after drying. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、有機性廃棄物の処理方法および処理装置に関するものである。
【0002】
【従来の技術】
近年、有機性廃棄物である生ごみの減量化および減容化を図るとともに肥料化などを図るための処理装置が、多数、製品化されている。
【0003】
この種の生ごみ処理装置は、攪拌翼が設けられた円筒状容器内に、破砕した生ごみを投入するとともに好気性微生物を加えた状態で、しかも所定の温度に加熱した状態で、上記攪拌翼により攪拌して生ごみを発酵させることにより、例えば肥料化を図るものであった。
【0004】
その中でも、生ごみなどの原料を発酵容器内で連続的に発酵させるものがあり、この装置においては、乾燥の効率化を図るために、発酵容器内を減圧させた状態で発酵を行うようにしたものがある(特許文献1参照)。
【0005】
【特許文献1】
特開2002−101865
【0006】
【発明が解決しようとする課題】
しかし、上記従来の処理装置によると、好気性微生物の存在下で且つ減圧した状態で加熱しつつ攪拌させて発酵を行うようにしたものであるため、微生物の作用(活性度)が低下するのを防止する上で、常時、発酵容器内の温度、湿度、減圧状態などを計測するとともに、適正な発酵状態が得られるように、減圧値、酸素量などが制御されており、したがってその制御が非常に面倒なものとなり、装置自体が高価になるという問題があり、さらに全ての工程が同じ減圧下で行われるため、乾燥工程および発酵工程について、それぞれ最適な条件下で行われないという問題もある。
【0007】
そこで、本発明は、構成が簡単で且つ各処理工程が最適な条件下で行い得る有機性廃棄物の処理方法および処理装置を提供することを目的とする。
【0008】
【課題を解決するための手段】
上記課題を解決するために、本発明の請求項1に係る有機性廃棄物の処理方法は、有機性廃棄物に微生物群を混入させて処理容器内で攪拌して発酵させる際に、
上記微生物群として好気性微生物と嫌気性微生物とを混合させたものを用い、且つ有機性廃棄物を減圧下で加熱し嫌気性微生物を活性化させて乾燥を行った後、大気圧下で加熱し好気性微生物を活性化させて発酵を行う方法である。
【0009】
また、請求項2に係る有機性廃棄物の処理装置は、有機性廃棄物に微生物群を混入させて処理容器内で攪拌して発酵させる処理装置であって、
上記処理容器内に攪拌部材を設けるとともに当該処理容器内に投入された有機性廃棄物を加熱する加熱装置を設け、
上記処理容器内の気体を吸引して当該処理容器内を減圧する減圧装置を設け、さらに上記微生物群として好気性微生物と嫌気性微生物とを混合させたものを用い、且つ有機性廃棄物を加熱して乾燥させる際に、上記減圧装置により処理容器内を減圧させて嫌気性微生物を活性化させるとともに、乾燥後に加熱して発酵を行わせる際に、当該処理容器内を大気圧下にさせて好気性微生物を活性化させるようにしたものである。
【0010】
上記処理方法および処理装置の構成によると、生ごみなどの有機性廃棄物を例えば肥料化する際に、まず減圧下で微生物に悪影響を与えないような加熱温度の状態で攪拌させて有機性廃棄物を乾燥させるとともに嫌気発酵をさせた後、大気圧下で好気性微生物により発酵させるようにしたので、すなわち有機性廃棄物の減圧(乾燥)と大気圧の常圧(発酵)とで別個に活性化する微生物群で発酵させるようにしたので、例えば減圧下のみで乾燥および発酵を行うものに比べて、処理容器内の圧力、酸素量などを細かく制御する必要がないため、装置自体の構成を簡単に且つ安価なものにすることができる。
【0011】
特に、減圧下での乾燥時においても、嫌気性微生物の活性化により発酵が行われるため、全体として効率の良い肥料化などの処理を行い得る。
【0012】
【発明の実施の形態】
以下、本発明の実施の形態に係る有機性廃棄物の処理方法および処理装置を、図1〜図4に基づき説明する。
【0013】
まず、処理装置について説明すると、この処理装置は、有機性廃棄物、例えば破砕された調理残渣、残飯などの生ごみ(以下、被処理物ともいう)に微生物を混入させて処理容器内で発酵させて、例えば肥料化など(土壌改良材を得る場合でも良い)を図るためのものである。
【0014】
図1に示すように、この処理装置1は、大きく分けて、架台2上に、支持ブラケット3を介して支持されて被処理物を発酵させるための横置型円筒状の処理容器4と、この処理容器4内の被処理物を加熱するための加熱装置5と、上記処理容器4内に投入された被処理物を攪拌するための攪拌装置6と、上記処理容器4内の気体を吸引して減圧するための減圧装置(吸引装置または真空装置ともいう)7と、同じく上記処理容器4内を大気圧の状態(大気圧下である)に置いたときに空気の給排出が行われるが、この空気の排出時に、処理容器4内の気体を導き脱臭を行い大気に放出するためのエアレーション装置8とから構成されている。
【0015】
上記加熱装置5は、処理容器4の少なくとも下半部を覆うように設けられた加熱用ジャケット11と、この加熱用ジャケット11と処理容器4表面との間に形成された断面が半円状の加熱室12内に蒸気配管13を介して加熱用蒸気を供給するための蒸気発生器(ボイラである)14とから構成されている。
【0016】
また、上記攪拌装置6は、処理容器4の中心部を前後方向で水平に挿通されるとともにその前後端部がそれぞれ軸受21を介して処理容器4に回転自在に支持された回転軸体22と、処理容器4内の回転軸体22に所定間隔おきに且つ放射状に多数突設されたアーム体23と、これら各アーム体23の先端部および途中部分に設けられた攪拌翼24と、架台2上に固定されて上記回転軸体22を回転させるための回転駆動機(電動機が用いられる)25とから構成されている。なお、アーム体23と攪拌翼24とにより攪拌部材が構成される。
【0017】
また、上記減圧装置7は、脱臭用バイオ菌が混入された水が充填された水槽31と、途中に水ポンプ32およびエジェクタ33が設けられて上記水槽31内の水を底部から引き出すとともに上部に戻すための水循環管34と、上記処理容器4内の上部とエジェクタ33との間に設けられるとともに途中に電動式開閉弁35が設けられた気体吸引管36とから構成されている。
【0018】
また、上記気体吸引管36途中には、電動式開閉弁37が設けられた大気導入管38が接続されており、上記処理容器4内を大気圧下にする際に、当該電動式開閉弁37が開かれて大気(空気)が導入される。
【0019】
さらに、上記エアレーション装置8は、脱臭用バイオ菌が混入された水が充填されるとともに脱臭用活性炭41aが配置された水槽41と、途中に電動式開閉弁42が設けられて上記処理容器4内の上部と水槽41の底部とを接続するガス排出管43と、途中に排風機(排気ファン)44が設けられて上記水槽41内のガスを大気に放出するためのガス放出管45と、上記処理容器4の下部に接続されるとともに途中に電動式開閉弁46が設けられた空気供給管(実際には、複数箇所に設けられている)47とから構成されている。
【0020】
勿論、上記処理容器4の上壁部には被処理物の投入口4aが形成されるとともに、この投入口4aを開閉する開閉蓋26が例えばシリンダ装置27により開閉自在に設けられ、また処理容器4の底壁部には被処理物の排出口4bが形成されるとともに、この排出口4bを開閉する開閉蓋28が例えば手動ウインチ装置29により開閉自在に設けられている。
【0021】
次に、被処理物である生ごみの処理方法について説明する。
まず、開閉蓋26を開き投入口4aから処理容器4内に、破砕された生ごみ(例えば、含水率が70〜85%程度)を、嫌気性微生物(嫌気性細菌)および好気性微生物(好気性細菌)が混合培養された微生物群(細菌群)と共に投入した後、開閉蓋26を閉じる。
【0022】
次に、加熱装置5により生ごみの発酵に最適な温度に、例えば40〜70℃(好ましくは、60℃程度)に加熱した状態で且つ攪拌装置6を作動させて攪拌を行う。このとき、各開閉弁35,37,42,46は閉じられている。
【0023】
次に、気体吸引管36に設けられている開閉弁35を開き、減圧装置7を作動させて、処理容器4内の空気を吸引して所定の負圧、例えば118Torr程度に減圧し、所定時間(例えば12時間程度)でもって且つ所定の含水率(例えば、50〜65%程度)となるように、生ごみの乾燥を行う。このように、減圧下で加熱して乾燥を行うようにしているので、水分が多く含まれている生ごみを短時間で乾燥することができるとともに、乾燥時である減圧下においても、好熱性・嫌気性微生物、例えば繊維素熱分解菌により、難分解性有機物の発酵(分解)が促進されており、短時間で効率の良い乾燥および発酵(分解)が行われる。なお、この乾燥時においては、処理容器4内が所定の減圧下となるように、常に、開閉弁35が開かれている。
【0024】
乾燥が終了すると、開閉弁35を閉じた後、大気導入管38の開閉弁37を開き大気に連通させ、再び、開閉弁37を閉じる。
処理容器4内が大気圧下になると、開閉弁42および46を開くとともに排風機44を作動させて、処理容器4内に外気(空気)を供給する。
【0025】
そして、引き続き、加熱温度を50〜70℃(好ましくは、60℃程度)に維持しながら、攪拌翼24を回転させて、好気性微生物の活性化により発酵が行われる。勿論、この大気圧下での発酵についても、所定時間(例えば、12時間程度)行われる。なお、ガス放出管43より大気に放出される処理容器4内のガス(気体)はエアレーション装置8の水槽41内を通過する際に、バイオ菌が混入された水および活性炭41aにより、悪臭分などが除去される。
【0026】
すなわち、減圧下で効率良く乾燥および発酵(分解)された生ごみを、大気圧下で活性化した好気性微生物と共に攪拌することにより、好気性微生物を最良の状態で生ごみに作用させることができ、一層効率良く肥料化を図ることができる。
【0027】
上述したように、生ごみを肥料化する際に、まず減圧下で嫌気性微生物が活性化した状態で、しかも当該微生物群に悪影響を与えないような加熱温度の状態で攪拌させて生ごみを乾燥させるようにしたので、発酵を伴った効率の良い乾燥を行うことができ、さらに乾燥後においては、大気圧下で好気性微生物を活性化させて通常の発酵を行うようにしたので、乾燥時(乾燥工程)および発酵時(発酵工程)のそれぞれにおいても最適な条件下で処理を行わせることができ、すなわち微生物の活性度を低下させることなく、短時間で効率の良い発酵により、肥料化を行うことができる。
【0028】
ところで、上記実施の形態において、加熱装置として、蒸気を用いたものについて説明したが、例えば電気式ヒータなどを用いたものであっても良い。
また、減圧装置として、エジェクタにより空気を排出するものについて説明したが、例えば真空ポンプを用いたものであっても良い。
【0029】
さらに、上記実施の形態において、有機性廃棄物が生ごみである場合について説明したが、その他、家畜排泄物、下水汚泥などであっても良い。
【0030】
【発明の効果】
以上のように本発明の有機性廃棄物の処理方法および処理装置の構成によると、生ごみなどの有機性廃棄物を例えば肥料化する際に、まず減圧下で微生物に悪影響を与えないような加熱温度の状態で攪拌させて有機性廃棄物を乾燥させるとともに嫌気発酵をさせた後、大気圧下で好気性微生物により発酵させるようにしたので、すなわち有機性廃棄物の乾燥と発酵とを同一の処理容器内にて別個の条件下で行わせるようにしたので、例えば減圧下で乾燥および発酵を行うものに比べて、処理容器内の圧力、酸素量などを細かく制御する必要がないため、装置自体の構成を簡単に且つ安価なものにすることができる。
【0031】
特に、減圧下での乾燥時においても、嫌気性微生物の活性化により発酵が行われるため、全体として効率の良い肥料化などの処理を行うことができる。
【図面の簡単な説明】
【図1】本発明の実施の形態に係る有機性廃棄物の処理装置の概略構成を示す一部切欠側面図である。
【図2】同処理装置の側面図である。
【図3】図2のA−A矢視図である。
【図4】同処理装置の断面図である。
【符号の説明】
1 処理装置
4 処理容器
4a 投入口
4b 取出口
5 加熱装置
6 攪拌装置
7 減圧装置
8 脱臭装置
14 蒸気発生器
24 攪拌翼
26 開閉蓋
28 開閉蓋
35 電動式開閉弁
36 気体吸引管
42 電動式開閉弁
43 ガス排出管
46 電動式開閉弁
47 空気供給管
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method and an apparatus for treating organic waste.
[0002]
[Prior art]
2. Description of the Related Art In recent years, a large number of processing apparatuses for reducing the volume and volume of garbage, which is an organic waste, and for converting the waste into fertilizer have been commercialized.
[0003]
This kind of garbage processing apparatus is characterized in that, in a cylindrical container provided with stirring blades, the crushed garbage is charged and aerobic microorganisms are added, and the garbage is heated to a predetermined temperature. The garbage was fermented by stirring with wings, for example, to produce fertilizer.
[0004]
Among them, there are those in which raw materials such as garbage are continuously fermented in a fermentation vessel.In this apparatus, in order to improve drying efficiency, fermentation is performed in a state where the pressure in the fermentation vessel is reduced. (See Patent Document 1).
[0005]
[Patent Document 1]
JP-A-2002-101865
[0006]
[Problems to be solved by the invention]
However, according to the above-mentioned conventional processing apparatus, the fermentation is performed by stirring while heating in the presence of aerobic microorganisms and under reduced pressure, so that the action (activity) of the microorganisms is reduced. In order to prevent this, the temperature, humidity, decompression state, etc. in the fermentation vessel are constantly measured, and the decompression value, oxygen amount, etc. are controlled so that an appropriate fermentation state is obtained. There is a problem that it becomes very troublesome and the apparatus itself becomes expensive.In addition, since all the steps are performed under the same reduced pressure, there is also a problem that the drying step and the fermentation step are not performed under optimal conditions. is there.
[0007]
Accordingly, an object of the present invention is to provide a method and an apparatus for treating organic waste, which have a simple structure and can perform each treatment step under optimal conditions.
[0008]
[Means for Solving the Problems]
In order to solve the above-mentioned problems, the method for treating organic waste according to claim 1 of the present invention comprises mixing microorganisms into organic waste, stirring the mixture in a treatment vessel, and performing fermentation.
A mixture of aerobic microorganisms and anaerobic microorganisms is used as the microorganism group, and the organic waste is heated under reduced pressure to activate the anaerobic microorganisms, dried, and then heated under atmospheric pressure. This is a method in which fermentation is performed by activating aerobic microorganisms.
[0009]
Further, the organic waste treatment apparatus according to claim 2 is a treatment apparatus for mixing microorganisms into the organic waste and agitating the fermentation in a treatment container,
A stirrer is provided in the processing container and a heating device for heating the organic waste put in the processing container is provided,
A decompression device is provided to reduce the pressure in the processing container by sucking the gas in the processing container, and further, a mixture of aerobic microorganisms and anaerobic microorganisms is used as the microorganism group, and the organic waste is heated. When drying and activating the anaerobic microorganisms by depressurizing the inside of the processing vessel by the above-described decompression device, when heating and fermenting after drying, the inside of the processing vessel is brought to atmospheric pressure. An aerobic microorganism is activated.
[0010]
According to the processing method and the configuration of the processing apparatus, when organic waste such as garbage is converted into fertilizer, for example, the organic waste is first stirred under reduced pressure at a heating temperature that does not adversely affect microorganisms. After drying and anaerobic fermentation, the fermentation is carried out by aerobic microorganisms under atmospheric pressure, that is, the organic waste is decompressed (dry) and atmospheric pressure is normal pressure (fermentation) separately. Since the fermentation is performed using a group of activated microorganisms, it is not necessary to finely control the pressure in the processing vessel, the amount of oxygen, and the like as compared with, for example, a method in which drying and fermentation are performed only under reduced pressure. Can be made simple and inexpensive.
[0011]
In particular, even during drying under reduced pressure, the fermentation is performed by activating the anaerobic microorganisms, so that a process such as efficient fertilization can be performed as a whole.
[0012]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, a method and an apparatus for treating organic waste according to an embodiment of the present invention will be described with reference to FIGS.
[0013]
First, the processing apparatus will be described. This processing apparatus mixes microorganisms with organic waste, for example, garbage such as crushed cooking residues and garbage (hereinafter, also referred to as an object to be processed) and fermentation in a processing vessel. This is for the purpose of, for example, turning into fertilizer (even when obtaining a soil improvement material).
[0014]
As shown in FIG. 1, the processing apparatus 1 is roughly divided into a horizontal cylindrical processing vessel 4 supported on a gantry 2 via a support bracket 3 for fermenting an object to be processed. A heating device 5 for heating the processing object in the processing container 4, a stirring device 6 for stirring the processing object charged in the processing container 4, and a gas in the processing container 4 A pressure reducing device (also referred to as a suction device or a vacuum device) 7 for reducing the pressure, and air is supplied and discharged when the processing container 4 is placed in the atmospheric pressure state (at atmospheric pressure). And an aeration device 8 for guiding the gas in the processing container 4 for deodorization and discharge to the atmosphere when the air is discharged.
[0015]
The heating device 5 includes a heating jacket 11 provided so as to cover at least a lower half of the processing container 4, and a cross section formed between the heating jacket 11 and the surface of the processing container 4 having a semicircular shape. A steam generator (which is a boiler) 14 for supplying heating steam into the heating chamber 12 via a steam pipe 13.
[0016]
The agitating device 6 includes a rotating shaft 22 that is horizontally inserted through the center of the processing container 4 in the front-rear direction, and whose front and rear ends are rotatably supported by the processing container 4 via bearings 21. A plurality of arms 23 radially protruding from the rotating shaft 22 in the processing vessel 4 at predetermined intervals and radially; a stirring blade 24 provided at a tip end and an intermediate portion of each arm 23; And a rotation driving device (electric motor is used) 25 that is fixed above and rotates the rotation shaft body 22. The arm 23 and the stirring blade 24 constitute a stirring member.
[0017]
In addition, the decompression device 7 has a water tank 31 filled with water mixed with deodorizing bio-germs, and a water pump 32 and an ejector 33 provided on the way to draw water in the water tank 31 from a bottom portion and at the top. It comprises a water circulation pipe 34 for returning, and a gas suction pipe 36 provided between the upper part in the processing vessel 4 and the ejector 33 and provided with an electric on-off valve 35 in the middle.
[0018]
An air introduction pipe 38 provided with an electric open / close valve 37 is connected in the middle of the gas suction pipe 36. When the inside of the processing container 4 is brought to the atmospheric pressure, the electric open / close valve 37 is connected. Is opened and the atmosphere (air) is introduced.
[0019]
Further, the aeration apparatus 8 is provided with a water tank 41 filled with water mixed with deodorizing bio-germs and an activated carbon 41a for deodorization, and an electric open / close valve 42 provided in the middle of the water tank 41, and A gas discharge pipe 43 connecting the upper part of the water tank 41 to the bottom part of the water tank 41; a gas discharge pipe 45 provided with an exhaust fan (exhaust fan) 44 on the way to discharge the gas in the water tank 41 to the atmosphere; An air supply pipe (actually provided at a plurality of locations) 47 connected to the lower part of the processing container 4 and provided with an electrically operated on-off valve 46 on the way.
[0020]
Of course, an input port 4a for an object to be processed is formed in the upper wall portion of the processing container 4, and an opening / closing lid 26 for opening and closing the input port 4a is provided to be openable and closable by, for example, a cylinder device 27. A discharge port 4b for the object to be processed is formed in the bottom wall portion of the workpiece 4, and an opening / closing lid 28 for opening and closing the discharge port 4b is provided so as to be openable and closable by, for example, a manual winch device 29.
[0021]
Next, a method of treating garbage as an object to be treated will be described.
First, the opening / closing lid 26 is opened, and crushed garbage (for example, having a water content of about 70 to 85%) is introduced into the processing container 4 from the input port 4a by anaerobic microorganisms (anaerobic bacteria) and aerobic microorganisms (aerobic microorganisms). After the aerial bacteria) are introduced together with the microorganism group (bacteria group) mixed and cultured, the opening / closing lid 26 is closed.
[0022]
Next, stirring is performed by operating the stirrer 6 while the heater 5 is heated to a temperature optimal for fermentation of garbage, for example, 40 to 70 ° C. (preferably about 60 ° C.). At this time, the on-off valves 35, 37, 42, 46 are closed.
[0023]
Next, the opening / closing valve 35 provided in the gas suction pipe 36 is opened, and the pressure reducing device 7 is operated to suck air in the processing container 4 to reduce the pressure to a predetermined negative pressure, for example, about 118 Torr, and then reduce the pressure for a predetermined time. (For example, about 12 hours) and the garbage is dried so as to have a predetermined moisture content (for example, about 50 to 65%). As described above, since heating and drying are performed under reduced pressure, garbage containing a large amount of water can be dried in a short time, and thermophilicity can be obtained even under reduced pressure during drying. -Fermentation (decomposition) of hardly decomposable organic substances is promoted by anaerobic microorganisms, for example, fibrous pyrolysis bacteria, and efficient drying and fermentation (decomposition) are performed in a short time. During the drying, the on-off valve 35 is always open so that the inside of the processing container 4 is kept at a predetermined reduced pressure.
[0024]
When the drying is completed, the on-off valve 35 is closed, the on-off valve 37 of the air introduction pipe 38 is opened to communicate with the atmosphere, and the on-off valve 37 is closed again.
When the inside of the processing container 4 becomes under the atmospheric pressure, the open / close valves 42 and 46 are opened and the exhaust fan 44 is operated to supply outside air (air) into the processing container 4.
[0025]
Then, while maintaining the heating temperature at 50 to 70 ° C. (preferably about 60 ° C.), the stirring blade 24 is rotated to activate the aerobic microorganisms, thereby performing fermentation. Of course, the fermentation under the atmospheric pressure is also performed for a predetermined time (for example, about 12 hours). When the gas (gas) in the processing container 4 discharged to the atmosphere from the gas discharge pipe 43 passes through the water tank 41 of the aeration apparatus 8, the gas and the activated carbon 41a mixed with the bio-bacterium cause the gas (gas) to emit a bad odor. Is removed.
[0026]
In other words, by stirring the garbage efficiently dried and fermented (decomposed) under reduced pressure together with the activated aerobic microorganisms under atmospheric pressure, the aerobic microorganisms can act on the garbage in the best condition. It is possible to make fertilizer more efficiently.
[0027]
As described above, when turning garbage into fertilizer, first, anaerobic microorganisms are activated under reduced pressure, and the garbage is stirred at a heating temperature that does not adversely affect the microorganisms. Since it was made to dry, efficient drying with fermentation can be performed, and after drying, aerobic microorganisms are activated under atmospheric pressure to perform normal fermentation. It is possible to carry out the treatment under the optimal conditions at each of the time (drying step) and the fermentation (fermentation step), that is, the fermentation can be carried out efficiently in a short time without reducing the activity of the microorganisms. Can be performed.
[0028]
By the way, in the above-described embodiment, a heating device using steam has been described. However, for example, a heating device using an electric heater or the like may be used.
In addition, as the depressurizing device, a device for discharging air by an ejector has been described, but a device using a vacuum pump may be used.
[0029]
Further, in the above-described embodiment, the case where the organic waste is garbage has been described, but other than that, livestock excrement, sewage sludge, or the like may be used.
[0030]
【The invention's effect】
As described above, according to the configuration of the organic waste treatment method and the treatment apparatus of the present invention, when organic waste such as garbage is converted into fertilizer, for example, the microorganism is not adversely affected under reduced pressure first. After the organic waste was dried by stirring at the heating temperature and subjected to anaerobic fermentation, the fermentation was carried out by aerobic microorganisms under atmospheric pressure, that is, the drying and fermentation of the organic waste were the same. Because it was performed under different conditions in the processing vessel of, compared to, for example, drying and fermenting under reduced pressure, because there is no need to finely control the pressure in the processing vessel, the amount of oxygen, etc. The configuration of the device itself can be made simple and inexpensive.
[0031]
In particular, even during drying under reduced pressure, the fermentation is performed by activating the anaerobic microorganisms, so that a process such as efficient fertilization can be performed as a whole.
[Brief description of the drawings]
FIG. 1 is a partially cutaway side view showing a schematic configuration of an organic waste treatment apparatus according to an embodiment of the present invention.
FIG. 2 is a side view of the processing apparatus.
FIG. 3 is a view taken along the line AA of FIG. 2;
FIG. 4 is a sectional view of the processing apparatus.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Processing device 4 Processing container 4a Inlet 4b Outlet 5 Heating device 6 Stirrer 7 Decompression device 8 Deodorizer 14 Steam generator 24 Stirrer blade 26 Opening lid 28 Opening lid 35 Electric open / close valve 36 Gas suction pipe 42 Electric open / close Valve 43 Gas exhaust pipe 46 Electric open / close valve 47 Air supply pipe

Claims (2)

有機性廃棄物に微生物群を混入させて処理容器内で攪拌して発酵させる際に、
上記微生物群として好気性微生物と嫌気性微生物とを混合させたものを用い、
且つ有機性廃棄物を減圧下で加熱し嫌気性微生物を活性化させて乾燥を行った後、大気圧下で加熱し好気性微生物を活性化させて発酵を行うことを特徴とする有機性廃棄物の処理方法。
When mixing microorganisms into organic waste and agitating in the processing vessel for fermentation,
Using a mixture of aerobic microorganisms and anaerobic microorganisms as the microorganism group,
And organic waste is heated under reduced pressure to activate anaerobic microorganisms and dried, and then heated under atmospheric pressure to activate aerobic microorganisms and perform fermentation. How to handle things.
有機性廃棄物に微生物群を混入させて処理容器内で攪拌して発酵させる処理装置であって、
上記処理容器内に攪拌部材を設けるとともに当該処理容器内に投入された有機性廃棄物を加熱する加熱装置を設け、
上記処理容器内の気体を吸引して当該処理容器内を減圧する減圧装置を設け、
さらに上記微生物群として好気性微生物と嫌気性微生物とを混合させたものを用い、且つ有機性廃棄物を加熱して乾燥させる際に、上記減圧装置により処理容器内を減圧させて嫌気性微生物を活性化させるとともに、乾燥後に加熱して発酵を行わせる際に、当該処理容器内を大気圧下にさせて好気性微生物を活性化させるようにしたことを特徴とする有機性廃棄物の処理装置。
A processing device for mixing microorganisms into organic waste and stirring and fermenting in a processing vessel,
A stirrer is provided in the processing vessel and a heating device is provided for heating the organic waste put in the processing vessel,
Providing a decompression device for sucking gas in the processing container and depressurizing the processing container,
Further, a mixture of an aerobic microorganism and an anaerobic microorganism is used as the microorganism group, and when the organic waste is heated and dried, the inside of the processing vessel is depressurized by the decompression device to remove the anaerobic microorganism. An organic waste treatment apparatus characterized in that, when activated and heated for fermentation after drying, the inside of the treatment container is brought to atmospheric pressure to activate the aerobic microorganisms. .
JP2003112240A 2003-04-17 2003-04-17 Disposal method and disposal apparatus for organic waste Pending JP2004313957A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107892592A (en) * 2017-11-28 2018-04-10 上海海和实业有限公司 A kind of reclaiming organic waste handling process
WO2019172745A1 (en) * 2018-03-08 2019-09-12 Gec Integration Sdn Bhd An aerobic composting apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107892592A (en) * 2017-11-28 2018-04-10 上海海和实业有限公司 A kind of reclaiming organic waste handling process
WO2019172745A1 (en) * 2018-03-08 2019-09-12 Gec Integration Sdn Bhd An aerobic composting apparatus

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