JPH11226553A - Method for decomposing solid organic substance in water by microorganism - Google Patents

Method for decomposing solid organic substance in water by microorganism

Info

Publication number
JPH11226553A
JPH11226553A JP3651698A JP3651698A JPH11226553A JP H11226553 A JPH11226553 A JP H11226553A JP 3651698 A JP3651698 A JP 3651698A JP 3651698 A JP3651698 A JP 3651698A JP H11226553 A JPH11226553 A JP H11226553A
Authority
JP
Japan
Prior art keywords
water
solid organic
organic matter
wood chips
microorganisms
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
JP3651698A
Other languages
Japanese (ja)
Inventor
Kiyonori Niino
清憲 新納
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.)
Clean World Kk
DAIRYUU KENSETSU KOGYO KK
NIPPON GIJUTSU KAIHATSU CENTER KK
Original Assignee
Clean World Kk
DAIRYUU KENSETSU KOGYO KK
NIPPON GIJUTSU KAIHATSU CENTER KK
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 Clean World Kk, DAIRYUU KENSETSU KOGYO KK, NIPPON GIJUTSU KAIHATSU CENTER KK filed Critical Clean World Kk
Priority to JP3651698A priority Critical patent/JPH11226553A/en
Publication of JPH11226553A publication Critical patent/JPH11226553A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/78Recycling of wood or furniture waste

Abstract

PROBLEM TO BE SOLVED: To decompose solid organic substances such as garbage efficiently with relatively small equipment costs and power consumption by packing water, the solid organic substances, and wood chips in which microorganisms effective for decomposing the organic substances are seeded in a treatment tank and fluidizing and agitating. SOLUTION: Each treatment tank 1a, 1b is formed from concrete, a synthetic resin, and others, and a prescribed amount water and wood chips 3b and 3c for supplying carbon which is a carrier for microorganisms and a nutrition source for raising microorganisms are packed respectively in the insides of the tanks 1a, 1b. Air diffusing pipes 2a and 2b are ranged in the bottom surface of each tank 1a and 1b, compressed air from a compressor is ejected from noises 2c and 2d, a circulating flow is generated in the tanks 1a, 1b so that the water, the solid organic substances, and the wood chips 3b and 3c are fluidized and agitated in the tanks 1a and 1b. In this way, the solid organic substances C can be oxidized and decomposed efficiently, and the residue can be treated extremely simply.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、一般家庭や商店よ
り排出される生ごみ等の固形有機物の分解処理に利用さ
れるものであり、微生物により固形有機物を臭気を発す
ることなく高能率で分解処理できるようにした、微生物
による固形有機物の水中分解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 is used for decomposing solid organic matter such as garbage discharged from households and shops, and decomposes solid organic matter with high efficiency without generating odor by microorganisms. The present invention relates to a method for decomposing solid organic matter in water by using a microorganism.

【0002】[0002]

【従来の技術】都市ごみ等の有機廃棄物は、通常焼却又
は醗酵により処理されている。ところで、生ごみ等は大
型の焼却炉で連続的に焼却する場合は別として、一般の
家庭や商店等で焼却処理することは殆んど不可能であ
る。また、生ごみ等を醗酵処理する場合であっても、醗
酵装置が大形になるうえ悪臭の発生を防止することが困
難で、都市部に於いては処理し難いと云う問題がある。
2. Description of the Related Art Organic waste such as municipal waste is usually treated by incineration or fermentation. By the way, it is almost impossible to incinerate garbage and the like in general households and shops, apart from the case where the garbage is continuously incinerated in a large incinerator. Further, even when fermenting garbage or the like, there is a problem that the fermentation apparatus becomes large and it is difficult to prevent the generation of offensive odor, and it is difficult to treat the garbage in an urban area.

【0003】図2は、ビルや商店街に於いて使用するこ
とを目的として開発された従前の醗酵式有機廃棄物処理
装置の一例を示すものである(特開平8−309319
号)。当該処理装置では、破砕機20で粉砕した廃棄物
21をスクリュー式脱水器22で脱水したあと、醗酵処
理槽24内へ搬送し、醗酵処理槽24内でヒータ25に
より加熱すると共に攪拌装置26でもって攪拌すること
により、廃棄物21を醗酵させる。そして、重量及び容
量が夫々約10%程度に減少された醗酵物が堆肥等とし
て順次醗酵処理槽24外へ取り出されて行く。また、前
記醗酵処理槽24内で発生した高温排ガス27は、除湿
器28で除湿した醗酵処理槽24内へ戻され、更に、破
砕機20や脱水器22からの廃水29及び高温排ガス2
7の一部は、生物脱臭・排水処理槽30へ導入され、こ
こで生物脱臭処理をしたあと外部へ排出されて行く。
FIG. 2 shows an example of a conventional fermentation type organic waste treatment apparatus developed for use in a building or a shopping street (Japanese Patent Laid-Open No. Hei 8-309319).
issue). In the processing apparatus, the waste 21 crushed by the crusher 20 is dehydrated by the screw type dehydrator 22, and then conveyed into the fermentation tank 24, heated by the heater 25 in the fermentation tank 24, and stirred by the stirring device 26. The waste 21 is fermented by stirring. Then, the fermented products whose weight and volume have been reduced to about 10%, respectively, are sequentially taken out of the fermentation tank 24 as compost or the like. The high-temperature exhaust gas 27 generated in the fermentation processing tank 24 is returned to the fermentation processing tank 24 dehumidified by the dehumidifier 28, and further, the wastewater 29 from the crusher 20 and the dehydrator 22 and the high-temperature exhaust gas 2
A part of 7 is introduced into the biological deodorization / drainage treatment tank 30, where it is subjected to biological deodorization treatment and then discharged to the outside.

【0004】上記図2の有機廃棄物処理装置は、約50
kg/日程度の生ごみを連続的に処理することができる
うえ、悪臭の発生が殆んど無いためビル内へ設置するこ
ともでき、優れた実用的効用を奏するものである。
[0004] The organic waste treatment apparatus shown in FIG.
In addition to being able to continuously process garbage of about kg / day, it can be installed in a building because there is almost no foul odor, and it has excellent practical utility.

【0005】しかし、当該有機廃棄物処理装置は装置そ
のものが大形(醗酵処理槽24の内容積が約400l、
生物脱臭・排水処理槽30の内容積が約200l)にな
るうえ、ヒータ25や攪拌装置26の駆動用に相当の電
力を必要とし、設置場所の確保や処理コストの引下げの
点に大きな問題を抱かえている。また、当該有機廃棄物
処理装置では、減容及び減量されているとは云うものの
生ごみ量の1/10に相当する量の醗酵物(堆肥)Wo
が発生するため、その処分にも相当の費用がかかること
になり、設備費や保守管理費に費用がかかることとも相
俟って、実用化を促進し難いと云う問題がある。
However, the organic waste treatment apparatus itself is large (the inner volume of the fermentation treatment tank 24 is about 400 l,
The internal volume of the biological deodorization / drainage treatment tank 30 becomes about 200 l), and requires a considerable amount of electric power to drive the heater 25 and the stirring device 26. This poses a major problem in securing an installation place and reducing the treatment cost. I'm holding you. In the organic waste treatment apparatus, the fermented product (compost) Wo in an amount equivalent to 1/10 of the amount of garbage, although the volume is reduced and the volume is reduced.
Therefore, there is a problem that it is difficult to promote its practical use, in addition to the fact that the disposal thereof requires a considerable cost, and the facility cost and the maintenance management cost are expensive.

【0006】[0006]

【発明が解決しようとする課題】本願発明は、従前の醗
酵式固形有機廃棄物処理装置に於ける上述の如き問題、
即ち処理装置の設置に大きなスペースを必要とするう
え、装置の運転に相当の電力を消費すること、設備が
複雑なために設備費や保守管理費が増大し、生ごみの処
理コストの引下げを図れないこと等の問題を解決せんと
するものであり、比較的少ない設備費と消費電力でもっ
て生ごみ等の固形有機物を高能率で分解処理できるよう
にした微生物による固形有機物の水中分解処理方法を提
供するものである。
SUMMARY OF THE INVENTION The present invention relates to the above-mentioned problems in the conventional fermentation type solid organic waste treatment apparatus,
In other words, a large space is required for installation of the processing equipment, a considerable amount of power is consumed for the operation of the equipment, and equipment complexity and maintenance costs increase due to the complexity of the equipment. A method of decomposing solid organic matter in water using microorganisms, which is capable of efficiently decomposing solid organic matter such as garbage with relatively little equipment cost and power consumption. Is provided.

【0007】[0007]

【課題を解決するための手段】請求項1の発明は、処理
槽内へ水と固形有機物と有機物を分解する有効微生物を
殖種した木材チップを充填し、処理槽内の水と固形有機
物と木材チップを流動攪拌させることにより、固形有機
物を水中で分解させることを発明の基本構成とするもの
である。
According to the first aspect of the present invention, a processing tank is filled with wood chips sown with water, solid organic matter, and effective microorganisms capable of decomposing organic substances, and water and solid organic matter in the processing tank are filled with the wood chips. The basic constitution of the invention is to decompose solid organic matter in water by fluidly stirring wood chips.

【0008】請求項2の発明は、請求項1の発明に於い
て有効微生物を好気性微生物とすると共に、処理槽の底
部に配設した散気管からの噴出空気により、水と固形有
機物と木材チップを流動攪拌させるようにしたものであ
る。
According to a second aspect of the present invention, there is provided a method according to the first aspect, wherein the effective microorganisms are aerobic microorganisms, and water, solid organic matter, and wood are blown by air blown out from an air diffuser provided at the bottom of the treatment tank. The chips are made to flow and agitate.

【0009】請求項3の発明は、請求項1の発明に於い
て、木材チップを好気性又は嫌気性微生物を殖種した粒
径が1〜10mmの杉材とすると共に、処理槽内へ浸積
した水中ポンプにより水と固形有機物と木材チップを流
動攪拌させるようにしたものである。
According to a third aspect of the present invention, in the first aspect of the present invention, the wood chips are made of cedar wood having a particle diameter of 1 to 10 mm cultivated with aerobic or anaerobic microorganisms, and are immersed in a treatment tank. The water, the solid organic matter, and the wood chips are fluidized and agitated by the stacked submersible pump.

【0010】[0010]

【発明の実施の形態】以下、図面に基づいて本発明の実
施の形態を説明する。図1は本発明の実施に用いる固形
有機物の水中分解処理装置の縦断面概要図であり、図1
に於いて1a・1bは処理槽、2a・2bは散気管、3
a・3bは木材チップ、4a・4bは水供給口、5は生
ごみ供給口、6はポンプ、7は処理液排出口、8は処理
液供給口、9は汚泥排出口、10は排水口、11a・1
1bは発生ガス排出口である。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic longitudinal sectional view of a solid organic matter underwater decomposition treatment apparatus used for carrying out the present invention.
1a and 1b are treatment tanks, 2a and 2b are air diffusers, 3
a · 3b is a wood chip, 4a · 4b is a water supply port, 5 is a garbage supply port, 6 is a pump, 7 is a treatment liquid discharge port, 8 is a treatment liquid supply port, 9 is a sludge discharge port, and 10 is a drain port. , 11a-1
1b is a generated gas discharge port.

【0011】生ごみ等の固形有機物Cは、予かじめ破砕
機等(図示省略)により適宜の大きさ例えば10mm×
10mm×10mm〜50mm×50mm×50mmの
大きさに破砕され、生ごみ供給口5から第1処理槽1a
内へ投入される。尚、一般家庭等から排出される生ごみ
等は破砕機を通さずに直接そのまま処理槽1a内へ投入
してもよいことは勿論である。
The solid organic matter C such as garbage can be appropriately sized, for example, 10 mm × by a pre-crusher or the like (not shown).
It is crushed to a size of 10 mm × 10 mm to 50 mm × 50 mm × 50 mm, and is supplied from the garbage supply port 5 to the first treatment tank 1 a.
It is thrown in. It is needless to say that garbage and the like discharged from households and the like may be directly introduced into the processing tank 1a without passing through a crusher.

【0012】前記各処理槽1a・1bはコンクリートや
合成樹脂等により形成されており、その内部には所定量
の水と、微生物の担体であり且つ微生物の生育用栄養源
である炭素を供給するため木材チップ3b・3cとが夫
々充填されている。即ち、当該木材チップ3b・3cは
粒径が1〜10mm程度に選定されており、有機物を酸
化分解するための有効菌(嫌気性又は好気性微生物)
が、予かじめ充填前の木材チップ3b・3cに殖種され
ている。尚、殖種する有効菌は好気性のものに限られ
ず、後述するように処理槽1a・1b内を嫌気性に保持
する場合には、嫌気性微生物を用いることは勿論であ
り、酵母菌、糸状菌等の種々の水棲性微生物が使用され
る。
Each of the treatment tanks 1a and 1b is made of concrete, synthetic resin, or the like, and supplies a predetermined amount of water and carbon, which is a carrier of microorganisms and a nutrient source for growing microorganisms, to the inside thereof. Therefore, wood chips 3b and 3c are filled respectively. That is, the wood chips 3b and 3c are selected to have a particle size of about 1 to 10 mm, and are effective bacteria (anaerobic or aerobic microorganisms) for oxidatively decomposing organic substances.
Has been bred in advance in the wood chips 3b and 3c before filling. The effective bacteria to be bred are not limited to aerobic ones. When the insides of the treatment tanks 1a and 1b are kept anaerobic as described later, it is needless to say that anaerobic microorganisms are used. Various aquatic microorganisms such as filamentous fungi are used.

【0013】また、前記木材チップ3b・3cの充填量
は処理槽1a・1bの内容積の10〜30%程度に選定
されており、処理槽1a・1bの作動時には水中に均等
に浮遊した状態となっている。更に、前記木材チップ3
b・3cの材質としては、杉、桧、樫その他如何なるも
のであっても良いが、本実施態様では杉材が使用されて
いる。
The filling amount of the wood chips 3b and 3c is selected to be about 10 to 30% of the inner volume of the processing tanks 1a and 1b, and the wood chips 3b and 3c are uniformly suspended in water when the processing tanks 1a and 1b are operated. It has become. Further, the wood chips 3
The material of b · 3c may be cedar, cypress, oak or any other material, but in this embodiment, cedar is used.

【0014】前記散気管2a・2bは各処理槽1a・1
bの底面に配設されており、コンプレッサー(図示省
略)からの圧縮空気Aがノズル2c・2dから噴射され
ることにより、処理槽1a・1b内に循環回流が起生さ
れ、これにより水と固形有機物と木材チップ3b・3c
は処理槽1a・1b内で流動攪拌されることになる。
The air diffusers 2a and 2b are connected to the respective processing tanks 1a and 1
b, and compressed air A from a compressor (not shown) is injected from the nozzles 2c and 2d to generate a circulating flow in the processing tanks 1a and 1b. Solid organic matter and wood chips 3b / 3c
Is fluidized and stirred in the processing tanks 1a and 1b.

【0015】尚、図1の実施態様に於いては、有効菌と
して好気性微生物を用い、散気管2a・2bから空気A
を噴出することにより、処理槽1a・1b内の水及び木
材チップ3b・3cを流動攪拌するようにしているが、
有効菌として嫌気性微生物を利用する場合には散気管2
a・2bに代えて攪拌羽根を処理槽1a・1b内に設
け、当該攪拌羽根によって水及び木材チップ3b・3c
を流動攪拌させるようにする。また、前記攪拌羽根等に
替えて水中ポンプを設け、該水中ポンプによって処理槽
1a・1b内に循環水流を形成するようにしてもよい。
In the embodiment of FIG. 1, an aerobic microorganism is used as an effective bacterium, and air A is supplied from the air diffusers 2a and 2b.
The water in the processing tanks 1a and 1b and the wood chips 3b and 3c are fluidized and stirred by ejecting water.
When using anaerobic microorganisms as effective bacteria, diffuser tube 2
a and 2b are provided in the processing tanks 1a and 1b in place of the water and wood chips 3b and 3c.
Is caused to flow under stirring. Further, a submersible pump may be provided in place of the stirring blade or the like, and the submersible pump may form a circulating water flow in the processing tanks 1a and 1b.

【0016】次に、本発明に係る有機廃棄物処理装置の
作動について説明する。処理槽1a・1b内へ水W及び
有効菌(好気性微生物)を殖種した木材チップを所定量
入れ、一定時間(例えば1〜2日間)空気Aを供給しつ
つ各処理槽1a・1b内の水及び木材チップ3b・3c
を循環流動させる。これにより、各処理槽1a・1b内
の木材チップ3b・3cの外表面や水中懸濁物の外表面
には、大量の好気性微生物が付着・生育することにな
る。
Next, the operation of the organic waste treatment apparatus according to the present invention will be described. A predetermined amount of water W and wood chips inoculated with effective bacteria (aerobic microorganisms) are put into the processing tanks 1a and 1b, and the air A is supplied for a certain time (for example, 1 to 2 days). Water and wood chips 3b / 3c
Is circulated. As a result, a large amount of aerobic microorganisms adhere to and grow on the outer surfaces of the wood chips 3b and 3c and the underwater suspension in each of the processing tanks 1a and 1b.

【0017】生ごみ供給口5から、適宜の大きさの固形
有機物C(例えば野菜くず等)が第1処理槽1a内へ投
入されると、処理槽1a内で繁殖した好気性微生物がこ
れら固形有機物に付着すると共に生育し、固形有機物そ
のものを所謂消化分解(又は酸化分解)することにな
る。尚、処理槽1a内へ投入された固形有機物Cは、木
材チップ3aと共に処理槽内を流動攪拌される過程で機
械的応力を受けるため、比較的短期間内に分解されて細
片となると共に、水中に浮遊する好気性微生物(所謂活
性汚泥)と接触することにより、順次消化分解(酸化分
解)されることになり、水と炭酸ガス等に変換されるこ
とになる。
When solid organic matter C (for example, vegetable waste) of an appropriate size is introduced into the first treatment tank 1a from the garbage supply port 5, the aerobic microorganisms propagated in the treatment tank 1a are subjected to the solid organic matter C. It attaches to organic matter and grows, so that solid organic matter itself is digested and decomposed (or oxidatively decomposed). The solid organic matter C introduced into the processing tank 1a receives mechanical stress in the process of flowing and agitating in the processing tank together with the wood chips 3a, so that the solid organic matter C is decomposed in a relatively short period of time into small pieces. By contact with aerobic microorganisms (so-called activated sludge) floating in water, they are sequentially digested and decomposed (oxidatively decomposed), and are converted into water and carbon dioxide.

【0018】処理槽1a内に於ける固形有機物の分解処
理が進行すると、ポンプ6によって処理液排出口7から
処理液13が抜き出され、第2処理槽1b内へ供給され
る。尚、第2処理槽1b内へ供給された処理液13は、
前記第1処理槽1a内の場合と同様に、好気性微生物に
よって引き続き消化分解され、最終的には水とCO 2
転換される。
Decomposition treatment of solid organic matter in treatment tank 1a
As the processing progresses, the processing liquid is discharged from the processing liquid outlet 7 by the pump 6.
The processing liquid 13 is withdrawn and supplied to the second processing tank 1b.
You. The processing liquid 13 supplied into the second processing tank 1b is
As in the case of the first treatment tank 1a, aerobic microorganisms
Therefore, it is continuously digested and decomposed, and eventually water and CO TwoTo
Is converted.

【0019】尚、第2処理槽1bの散気管2bの下方に
溜った汚泥D等は、汚泥排出口9を定期的に開放するこ
とにより処理槽外へ排出される。また、発生したCO2
やメタン等のガスはガス排出口11a・11bから適宜
に槽外へ排出される。更に、第2処理槽1b内の処理液
13は適宜の間隔で排水口10から排出水Woとして排
出される。
The sludge D and the like collected below the air diffuser 2b of the second treatment tank 1b are discharged out of the treatment tank by periodically opening the sludge discharge port 9. Also, the generated CO 2
Gases such as gas and methane are discharged from the gas outlets 11a and 11b to the outside of the tank as appropriate. Further, the processing liquid 13 in the second processing tank 1b is discharged as drain water Wo from the drain port 10 at appropriate intervals.

【0020】前記図1の実施態様に於いては、生ごみC
を間欠的に第1処理槽1a内へ供給し、所謂バッチ方式
により固形有機物Cを処理するようにしているが、生ご
みCを所定量づつ連続的に供給し、これを連続処理する
ようにしてもよいことは勿論であり、この場合にはポン
プ6及び排水弁10a等の作動は所定のシーケンスに従
って自動的に行なわれる。
In the embodiment of FIG. 1, the garbage C
Is intermittently supplied into the first treatment tank 1a, and the solid organic matter C is treated by a so-called batch method. However, the garbage C is continuously supplied by a predetermined amount, and the garbage C is continuously treated. Needless to say, in this case, the operations of the pump 6, the drain valve 10a, and the like are automatically performed according to a predetermined sequence.

【0021】また、図1の実施態様では、処理槽として
第1処理槽1a及び第2処理槽1bを設けると共に、散
気管2a・2bからの噴出空気により処理液13を流動
攪拌させるようにしているが、処理槽は1基だけであっ
てもよくまた、処理槽内の処理水13を水中ポンプや攪
拌羽根によって攪拌流動させるようにしてもよいことは
勿論である。更に、木材チップ3a・3bは、時間の経
過と共に有効微生物によって若干分解されることになる
が、その分解量は生ごみ等に比較して極く僅かである。
従って、木材チップ3a・3bの補充は10〜12ケ月
に1回位でよく且つその補充量も全木材チップ3a・3
b量の10〜20wt%程度で十分であり、且つ有効微
生物の殖種は全く不要である。
In the embodiment shown in FIG. 1, a first processing tank 1a and a second processing tank 1b are provided as processing tanks, and the processing liquid 13 is caused to flow and agitate by air jetted from the diffusion tubes 2a and 2b. However, it is needless to say that only one treatment tank may be used, and the treatment water 13 in the treatment tank may be agitated and flown by a submersible pump or a stirring blade. Further, the wood chips 3a and 3b are slightly decomposed by effective microorganisms with the passage of time, but the amount of decomposition is extremely small as compared with garbage and the like.
Therefore, the replenishment of the wood chips 3a and 3b may be performed only once every 10 to 12 months, and the replenishment amount may be all the wood chips 3a and 3b.
About 10 to 20 wt% of the amount b is sufficient, and no breeding of effective microorganisms is required at all.

【0022】次に、本発明に係る処理方法を用いた固形
有機物の水中分解試験の結果について説明する。先ず、
処理槽1a・1bとして内容積1m3 のコンクリート製
処理槽1a・1bを、また木材チップ3b・3cとして
約5mm×5mmの杉材(各槽当り0.2m3 )を、更
に有効菌として好気性微生物を夫々用い、各散気管2a
・2bからの噴出空気(約20l/min)Aによっ
て、処理液13及び木材チップ3a・3bを流動攪拌さ
せるようにした処理装置を製作し、当該処理装置の第1
処理槽内へ1日当り50kgの生ごみ(平均寸法100
mm×50mm、水分約90%)を1回/日の割合で投
入した。尚、ポンプ6は1回/日の割合で運転し、約5
0l/日の細かな固形有機物を含有する処理液13を第
2処理槽1bへ移送した。同様に、第2処理槽1b内か
らは、約50l/日の割合で処理液13を排水口10及
びオーバーフロー排水口12bから排出した。
Next, the results of an underwater decomposition test of solid organic matter using the treatment method according to the present invention will be described. First,
Concrete treatment tanks 1a and 1b each having an internal volume of 1 m 3 as treatment tanks 1a and 1b, cedar wood of about 5 mm x 5 mm (0.2 m 3 for each tank) as wood chips 3b and 3c are preferable as effective bacteria. Each aerating tube 2a using aerobic microorganisms
A processing device is manufactured in which the processing liquid 13 and the wood chips 3a and 3b are caused to flow and agitate by the jet air (about 20 l / min) A from the second processing device 2b.
50kg of garbage per day (average size 100)
(mm × 50 mm, water content: about 90%) at a rate of once / day. The pump 6 operates at a rate of once a day, and is
The processing liquid 13 containing 0 l / day of fine solid organic matter was transferred to the second processing tank 1b. Similarly, the processing liquid 13 was discharged from the second processing tank 1b from the drain port 10 and the overflow drain port 12b at a rate of about 50 l / day.

【0023】上述の如き運転を3日間連続した後、排水
口10からの排出水WoのBOD濃度及び第1処理槽1
a及び第2処理槽1b内の固形有機物の状態を検査し
た。その結果、第2処理槽1bからの排水WoのBOD
濃度は、約20mmg/l程度に下降しており、固形有
機物Cは水中でほぼ完全に分解消化されていることが判
った。また、第1処理槽1aの処理液排出口7から引き
抜いた処理液13の内部には、分解途中の細かな固形有
機物が若干残留するが、当該処理液13をそのまま処理
槽外へ排出しても、悪臭や環境汚損を生じる恐れの無い
ことが判明した。尚、この場合には、第2処理槽1bは
不要であり、第1処理槽1aのみで固形有機物Cの分解
処理が達成される。
After the operation as described above is continued for three days, the BOD concentration of the effluent water Wo from the drain port 10 and the first treatment tank 1
a and the state of the solid organic matter in the second processing tank 1b were inspected. As a result, the BOD of the wastewater Wo from the second treatment tank 1b
The concentration dropped to about 20 mmg / l, indicating that the solid organic matter C was almost completely decomposed and digested in water. Further, inside the processing liquid 13 pulled out from the processing liquid discharge port 7 of the first processing tank 1a, a small amount of fine solid organic matter during decomposition remains, but the processing liquid 13 is discharged out of the processing tank as it is. It was also found that there was no risk of generating bad smell and environmental pollution. In this case, the second treatment tank 1b is unnecessary, and the decomposition treatment of the solid organic matter C is achieved only by the first treatment tank 1a.

【0024】[0024]

【発明の効果】本発明に於いては、処理槽内へ水と固形
有機物と有効微生物を殖種した木材チップを投入し、こ
れ等三者を一定時間流動攪拌させるだけで固形有機物を
効率よく酸化分解させることができ、しかも分解生成物
は主として水と炭酸ガスであるため、処理残査も極めて
簡単に処理することができる。また、処理槽内の水と固
形有機物と木材チップを流動攪拌させるだけで、複雑な
処理操作や処理装置を全く必要としないため、固形有機
物をより安価に分解処理することができる。本発明は上
述の通り優れた実用効果を奏するものである。
According to the present invention, wood chips in which water, solid organic matter and effective microorganisms have been bred are introduced into a treatment tank, and the solid organic matter is efficiently produced only by flowing and stirring these three members for a certain period of time. Since it can be oxidatively decomposed and the decomposition products are mainly water and carbon dioxide, the processing residue can be treated very easily. In addition, since only complicated stirring operation and a processing device are not required at all just by stirring and stirring water, solid organic matter and wood chips in the processing tank, the solid organic matter can be decomposed at lower cost. The present invention has excellent practical effects as described above.

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

【図1】本発明の実施態様に係る固形有機物の水中分解
処理装置の縦断面図である。
FIG. 1 is a longitudinal sectional view of an apparatus for decomposing solid organic matter in water according to an embodiment of the present invention.

【図2】従前の醗酵式固形有機性廃棄物処理装置の一例
を示すものである。
FIG. 2 shows an example of a conventional fermentation type solid organic waste treatment apparatus.

【符号の説明】[Explanation of symbols]

Cは生ごみ等(固形有機物)、Wは供給水、Woは排
水、Aは空気、Dは汚泥、1a・1bは処理槽、2a・
2bは散気管、2c・2dはノズル、3b・3cは木材
チップ、4a・4bは水供給口、5は生ごみ供給口、6
はポンプ、7は処理液排出口、7aはスクリーン、8は
処理液供給口、9は汚泥排出口、10は排水口、10a
はスクリーン、10 は排水弁、11a・11bは発生
ガス排出口、12a・12bはオーバーフロー排水口、
13は処理液。
C is garbage (solid organic matter), W is supply water, Wo is drainage, A is air, D is sludge, 1a and 1b are treatment tanks, 2a.
2b is an air diffuser, 2c and 2d are nozzles, 3b and 3c are wood chips, 4a and 4b are water supply ports, 5 is garbage supply port, 6
Is a pump, 7 is a processing liquid discharge port, 7a is a screen, 8 is a processing liquid supply port, 9 is a sludge discharge port, 10 is a drain port, 10a
Is a screen, 10 is a drain valve, 11a and 11b are generated gas outlets, 12a and 12b are overflow drains,
13 is a processing solution.

───────────────────────────────────────────────────── フロントページの続き (71)出願人 598022598 村上 建夫 大阪府大阪市阿倍野区北畠1丁目2番19号 (72)発明者 新納 清憲 大阪府大阪市中央区高麗橋1丁目3番3号 株式会社日本技術開発センター内 ──────────────────────────────────────────────────続 き Continuation of the front page (71) Applicant 598022598 Tatsuo Murakami 1-2-19 Kitahata, Abeno-ku, Osaka-shi, Osaka (72) Inventor Kiyonori Shinno 1-3-3, Komyo-bashi, Chuo-ku, Osaka-shi, Osaka Co., Ltd. Inside the Japan Technology Development Center

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 処理槽内へ水と固形有機物と有機物を分
解する有効微生物を殖種した木材チップを充填し、処理
槽内の水と固形有機物と木材チップを流動攪拌させるこ
とにより、固形有機物を水中で分解させることを特徴と
する微生物による固形有機物の水中分解処理方法。
1. A processing vessel is filled with wood chips sown with water, solid organic matter, and effective microorganisms that decompose organic matter, and the water, the solid organic matter, and the wood chips in the processing vessel are fluidly stirred to obtain solid organic matter. A method for decomposing solid organic matter in water using microorganisms, comprising decomposing water in water.
【請求項2】 有効微生物を好気性微生物とすると共
に、処理槽の底部に配設した散気管からの噴出空気によ
り、水と固形有機物と木材チップを流動攪拌させるよう
にした請求項1に記載の微生物による固形有機物の水中
分解処理方法。
2. The method according to claim 1, wherein the effective microorganisms are aerobic microorganisms, and the water, the solid organic matter, and the wood chips are flow-stirred by air blown out from an air diffuser disposed at the bottom of the treatment tank. A method for decomposing solid organic matter in water using microorganisms.
【請求項3】 木材チップを好気性又は嫌気性微生物を
殖種した粒径が1〜10mmの杉材とすると共に、処理
槽内へ浸積した水中ポンプにより水と固形有機物と木材
チップを流動攪拌させるようにした請求項1に記載の微
生物による固形有機物の水中分解処理方法。
3. The wood chips are made of cedar wood having a particle size of 1 to 10 mm in which aerobic or anaerobic microorganisms have been bred, and water, solid organic matter and wood chips are flown by a submerged pump immersed in a treatment tank. The method for decomposing solid organic matter in water by a microorganism according to claim 1, wherein the stirring is performed.
JP3651698A 1998-02-19 1998-02-19 Method for decomposing solid organic substance in water by microorganism Pending JPH11226553A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3651698A JPH11226553A (en) 1998-02-19 1998-02-19 Method for decomposing solid organic substance in water by microorganism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3651698A JPH11226553A (en) 1998-02-19 1998-02-19 Method for decomposing solid organic substance in water by microorganism

Publications (1)

Publication Number Publication Date
JPH11226553A true JPH11226553A (en) 1999-08-24

Family

ID=12471994

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3651698A Pending JPH11226553A (en) 1998-02-19 1998-02-19 Method for decomposing solid organic substance in water by microorganism

Country Status (1)

Country Link
JP (1) JPH11226553A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006122876A (en) * 2004-11-01 2006-05-18 Nishihara Environment Technology Inc Apparatus for treating water
JP2006326386A (en) * 2005-05-23 2006-12-07 Waki Sangyo:Kk Organic sludge water treatment method
JP2007260549A (en) * 2006-03-28 2007-10-11 Dowa Holdings Co Ltd Water cleaning method and apparatus
US20100326904A1 (en) * 2007-09-14 2010-12-30 Bionest Technologies Inc. Wastewater treatment

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006122876A (en) * 2004-11-01 2006-05-18 Nishihara Environment Technology Inc Apparatus for treating water
JP2006326386A (en) * 2005-05-23 2006-12-07 Waki Sangyo:Kk Organic sludge water treatment method
JP2007260549A (en) * 2006-03-28 2007-10-11 Dowa Holdings Co Ltd Water cleaning method and apparatus
US20100326904A1 (en) * 2007-09-14 2010-12-30 Bionest Technologies Inc. Wastewater treatment

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