JP2572334B2 - Method and apparatus for microbiological reduction of excess sludge - Google Patents

Method and apparatus for microbiological reduction of excess sludge

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Publication number
JP2572334B2
JP2572334B2 JP4281037A JP28103792A JP2572334B2 JP 2572334 B2 JP2572334 B2 JP 2572334B2 JP 4281037 A JP4281037 A JP 4281037A JP 28103792 A JP28103792 A JP 28103792A JP 2572334 B2 JP2572334 B2 JP 2572334B2
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JP
Japan
Prior art keywords
sludge
reduction
solid
biological treatment
liquid separation
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.)
Expired - Lifetime
Application number
JP4281037A
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Japanese (ja)
Other versions
JPH06106198A (en
Inventor
泰典 遠矢
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.)
Ebara Corp
Ebara Research Co Ltd
Original Assignee
Ebara Corp
Ebara Research Co Ltd
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Priority to JP4281037A priority Critical patent/JP2572334B2/en
Publication of JPH06106198A publication Critical patent/JPH06106198A/en
Application granted granted Critical
Publication of JP2572334B2 publication Critical patent/JP2572334B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】本発明は、し尿、下水および/ま
たは有機性廃水などの汚水を微生物学的に処理する過程
において発生する余剰汚泥を、自然界に広く分布生息し
ている溶菌作用を有する粘液細菌により減量化する余剰
汚泥の微生物学的減量化法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention has a bacteriolytic action in which excess sludge generated in the process of microbiologically treating wastewater such as human waste, sewage and / or organic wastewater is widely distributed and inhabits in nature. The present invention relates to a method for microbiologically reducing excess sludge reduced by slime bacteria.

【0002】[0002]

【従来の技術】従来、し尿、下水および/または有機性
廃水の生物学的処理、その中でも特に好気的な生物処理
の工程から発生する余剰汚泥は、発生量が莫大であり、
その処理、処分に大量のエネルギーと資源の消費を余儀
なくされている。
2. Description of the Related Art Conventionally, the excess sludge generated from the biological treatment of human waste, sewage and / or organic wastewater, particularly aerobic biological treatment, is enormous,
Large amounts of energy and resources are being consumed for their processing and disposal.

【0003】現在、わが国にはし尿処理現場が約1,2
00ヶ所、下水処理場(都市下水)が800〜1,00
0ヶ所もあり、有機性廃水処理を別にしても、処理、処
分すべき余剰汚泥は莫大な量に達する。これら余剰汚泥
は一部有効利用されているが、その殆どの余剰汚泥は全
量を濃縮し、これに脱水用の助剤を添加して、機械的な
手段、方法によって脱水し水分80〜85%とした後、
焼却炉で焼却するという大量のエネルギーと資源を投入
して処理・処分されている。しかしながら、余剰汚泥量
の増加に伴い濃縮脱水のための施設は大型化せざるを得
ず、また脱水率にも限界があり焼却炉も大容量の処理を
要求されている。このため、各自治体では処理・処分に
要する経済的負担に苦慮しているだけでなく、大気汚
染、水質汚濁などの2次汚染や、地球温暖化への技術的
対応という観点からも、具体的な解決策をせまられてい
る。
At present, there are about 1,2 human waste treatment sites in Japan.
00 places, sewage treatment plant (urban sewage) 800-1,000
There are 0 places, and the amount of excess sludge to be treated and disposed of is enormous even if the organic wastewater treatment is separated. Although some of these excess sludges are effectively used, most of the excess sludge is concentrated in its entirety, and an auxiliary for dehydration is added thereto. And then
It is treated and disposed of by inputting large amounts of energy and resources for incineration. However, as the amount of excess sludge increases, the facilities for concentration and dewatering must be enlarged, and the dewatering rate is limited, so that incinerators are also required to process large volumes. For this reason, not only are local governments struggling with the economic burden required for treatment and disposal, but also from the perspective of technical response to secondary pollution such as air pollution and water pollution, and global warming. Solutions.

【0004】このため発生する余剰汚泥を減量化する方
法が模索されてきた。例えば下水処理などにおいて、余
剰汚泥と最初沈殿池(以下初沈という)汚泥を、それぞ
れ濃縮した後に発生比率で混合し、メタン醗酵(嫌気性
消化)処理して余剰汚泥を減量化する方法が採られてい
る。しかしながら、余剰汚泥は言わば活性汚泥微生物の
余剰菌体であるため、通常のメタン醗酵処理では菌体の
細胞壁や細胞膜の分解率が悪く、約20〜30日間の消
化日数が必要であり、設備の整備に過大な投資を必要と
する。
For this reason, a method for reducing the amount of excess sludge generated has been sought. For example, in sewage treatment, excess sludge and first sedimentation basin (hereinafter referred to as “first sedimentation”) sludge are concentrated, then mixed at a generation ratio, and treated by methane fermentation (anaerobic digestion) to reduce excess sludge. Have been. However, since the excess sludge is a surplus of activated sludge microorganisms, the degradation rate of the cell wall and cell membrane of the bacterial cells is poor in the ordinary methane fermentation treatment, and the digestion time of about 20 to 30 days is required. Requires excessive investment in maintenance.

【0005】一方消化によらず、菌体の細胞壁や細胞膜
を破壊する微生物学的方法が検討されている。例えば特
開昭61−129098号公報によれば、汚水の生物処
理によって発生した汚泥にバクテリオファージを添加
し、その溶菌作用によって汚泥を減量化する方法が提案
されている。しかしながら、バクテリオファージは宿主
特異性が極めて強く、ある特定のバクテリオファージは
特定の細菌にだけ寄生し溶解する。従って、活性汚泥の
ような多菌種混合培養系の汚泥をバクテリオファージに
よって減量化しようとすると、実用上活性汚泥に生息し
ている菌種と同数種類のバクテリオファージを自然界か
らスクリーニングし、製剤化しなければならず、汚泥減
量化へのこの方法の適用は困難である。
On the other hand, microbiological methods for destroying cell walls and cell membranes of bacterial cells without using digestion have been studied. For example, Japanese Patent Application Laid-Open No. 112998/1986 proposes a method of adding bacteriophage to sludge generated by biological treatment of wastewater and reducing the amount of sludge by bacteriolysis. However, bacteriophages have extremely high host specificity, and certain bacteriophages are parasitized and lysed only by certain bacteria. Therefore, in order to reduce the amount of multi-bacteria mixed culture sludge such as activated sludge by bacteriophage, the same number of bacteriophages as the number of bacterial species that actually inhabit the activated sludge are screened from nature and formulated. It is difficult to apply this method to sludge reduction.

【0006】さらに、破壊された細菌内容物は水中に放
出されるため、新たな有機汚濁を生じる。前記特許公報
では放出される有機物はバクテリオファージとなってい
るようだが、バクテリオファージを含むビールスは古く
はろ過性病原体と呼んだように、コロイド程度の極めて
微小な粒子であって、固液分離による除去は容易ではな
い。該特許公報では固液分離された分離水は放流される
が、この中に多数のバクテリオファージが含まれ、これ
が新たな汚濁物となることは明らかである。これに対し
何らかの浄化装置を導入することは容易に考え至るが、
生物処理工程に返送することはその際極めて濃厚な溶菌
力をもつバクテリオファージ溶液を活性汚泥に接種して
しまうことになり、処理に障害をきたす恐れがある。
[0006] In addition, the destroyed bacterial contents are released into the water, resulting in new organic pollution. In the patent publication, the released organic matter seems to be bacteriophage, but viruses containing bacteriophage are very small particles, such as colloids, as they were called filterable pathogens in the old days. Removal is not easy. In this patent publication, the separated water subjected to solid-liquid separation is discharged, and it is clear that a large number of bacteriophages are contained in the separated water, which becomes new pollutants. On the other hand, it is easy to think about introducing a purifying device,
Returning to the biological treatment step would inoculate the activated sludge with a bacteriophage solution having a very high lytic power at that time, which may hinder the treatment.

【0007】従って、バクテリオファージの処理手段を
設けねばならないが、前記のように該ビールスはコロイ
ドレベルの大きさであり、通常の沈殿分離が不可能であ
ることは勿論、通常のろ過法によっても分離は困難で、
限外ろ過乃至は逆浸透ろ過設備により分離する必要があ
る。あるいは、不活性化・殺菌手段を設けねばならな
ず、場合によってはそれに用いる殺菌剤の除害装置をも
必要とする。かくして、付帯施設は膨大化し、到底実用
には供し難い現状である。
Therefore, it is necessary to provide a means for treating bacteriophage. However, as described above, the virus has a colloidal level and, as a matter of course, cannot be separated by ordinary sedimentation. Separation is difficult,
It is necessary to separate by ultrafiltration or reverse osmosis filtration equipment. Alternatively, inactivation / sterilization means must be provided, and in some cases, a disinfectant abatement device used for the device is required. Thus, the number of incidental facilities has become enormous, making it hardly practical for practical use.

【0008】[0008]

【発明が解決しようとする課題】本発明は、特別の付帯
設備を必要としない、微生物の溶菌作用と再資化による
汚泥減量化方法とそれに適する汚泥減量化装置を開発す
ることを目的とする。
SUMMARY OF THE INVENTION An object of the present invention is to develop a sludge reduction method and a sludge reduction apparatus suitable for the method, which do not require special auxiliary equipment, by bacteriolysis and recycling of microorganisms. .

【0009】[0009]

【課題を解決するための手段】発明者らは汚泥減量化の
目的を達成するために、自然界に極く一般的に分布生息
している粘液細菌が菌体外に生産する溶菌酵素によって
余剰汚泥中の主構成細菌であるBOD資化細菌などの菌
体を溶菌し、自己細胞構築に資化する作用に着目して本
発明に至った。すなわち、上記課題は本発明の余剰汚泥
の微生物学的減量化方法ならびに装置の開発によって達
成される。 1)汚水の生物処理工程より排出される余剰汚泥に溶菌
作用を有する粘液細菌の単一菌株または複数菌株を接種
し、好気条件下で作用させることを特徴とする余剰汚泥
の微生物学的減量化方法。 2)汚水の生物処理工程より排出される余剰汚泥に溶菌
作用を有する粘液細菌の単一菌株または複数菌株を接種
し、好気条件下で作用させる減量化工程と、減量化工程
より排出される減量化汚泥を固液分離する工程を有する
と共に、固液分離された分離汚泥の一部を前記減量化工
程に循環返送することを特徴とする余剰汚泥の微生物学
的減量化方法。 3)汚水の生物処理工程より排出される余剰汚泥に溶菌
作用を有する粘液細菌の単一菌株または複数菌株を接種
し、好気条件下で作用させる減量化工程と、減量化工程
より排出される減量化汚泥を固液分離する工程を有する
と共に、固液分離された分離汚泥の一部を前記減量化工
程に循環返送し、分離液を生物処理工程に導くことを特
徴とする余剰汚泥の微生物学的減量化方法。ならびに、 4)酸素含有気体の導入手段を有する汚泥減量化槽と、
汚泥減量化槽より排出される減量化汚泥を固液分離する
固液分離装置を備えると共に、固液分離された分離汚泥
の一部を前記汚泥減量化槽に導く手段と、分離液を生物
処理装置に導く手段を有することを特徴とする余剰汚泥
の微生物学的減量化装置。である。
Means for Solving the Problems In order to achieve the object of sludge reduction, the present inventors have found that sludge bacterium, which is extremely commonly distributed and inhabiting the natural world, has surplus sludge produced by lytic enzymes produced outside the cells. The present invention has been achieved by focusing on the action of lysing bacterial cells such as BOD-utilizing bacteria, which are the main constituent bacteria, and assimilating into self-cell construction. That is, the above object is achieved by the development of the method and apparatus for microbiologically reducing excess sludge of the present invention. 1) Microbial weight loss of surplus sludge characterized by inoculating surplus sludge discharged from a biological treatment process of sewage with a single strain or multiple strains of myxobacteria having a bacteriolytic action and allowing them to act under aerobic conditions. Method. 2) Excess sludge discharged from the biological treatment process of sewage is inoculated with a single strain or multiple strains of lytic bacteria having a bacteriolytic action, and is reduced under aerobic conditions; A method for microbiologically reducing excess sludge, comprising a step of solid-liquid separation of reduced sludge and circulating and returning a part of the separated sludge subjected to solid-liquid separation to the reduction step. 3) Excess sludge discharged from the biological treatment process of sewage is inoculated with a single strain or multiple strains of myxobacteria having a bacteriolytic action, and is reduced under aerobic conditions, and discharged from the reduction process. Microorganisms of excess sludge having a step of solid-liquid separation of the reduced sludge, circulating a part of the separated sludge solid-liquid separated back to the reduction step, and leading the separated liquid to a biological treatment step Biological weight loss method. And 4) a sludge reduction tank having means for introducing an oxygen-containing gas,
A solid-liquid separation device for solid-liquid separation of the reduced sludge discharged from the sludge reduction tank, means for leading a part of the separated sludge separated into solid and liquid to the sludge reduction tank, An apparatus for microbiologically reducing excess sludge, comprising means for leading to an apparatus. It is.

【0010】(発明の機能)本発明の優れた機能および
作用効果を図1に基づいて以下に説明する。ただし本発
明の実施態様はこれに限定するものではない。図1にお
いて、減量化の対象となる生物処理槽1からの余剰汚泥
4を余剰汚泥濃縮槽2に導入し、余剰汚泥濃度20,0
00〜30,000mg/リットル程度にまで濃縮した
後、汚泥減量化槽3に移送する。一方、余剰菌体の減量
化に使用する粘液細菌は自然界から独自の菌株を1種類
以上増量培養して、汚泥の減量化の種菌に供すると良
い。また、溶菌作用の優れた菌株を保存機関の分譲株中
より選出し、これを用いることも良い。
(Functions of the Invention) The excellent functions and effects of the present invention will be described below with reference to FIG. However, embodiments of the present invention are not limited to this. In FIG. 1, the excess sludge 4 from the biological treatment tank 1 to be reduced is introduced into the excess sludge concentration tank 2 and the excess sludge concentration is set to 20,0.
After concentrating to about 00 to 30,000 mg / liter, it is transferred to the sludge reduction tank 3. On the other hand, as for myxobacteria used for the reduction of surplus cells, it is preferable to increase and culture one or more kinds of unique strains from the natural world and use them as seeds for sludge reduction. It is also possible to select a strain having an excellent lytic action from the stocks of a preservation institution and use it.

【0011】汚泥減量化槽3に接種する粘液細菌12
は、液状の混合培養体を使用してもよいし、また粘液細
菌を液体培地および/または固形培地で培養した後菌体
を通常の手段で分離濃縮し、これを凍結乾燥した所謂乾
燥菌体を使用してもよい。さらに両種菌体の併用も本発
明を妨げるものではない。これらの接種菌体12はシャ
ワー、スプレー、インジェクターあるいは単なる配管な
ど任意の手段により汚泥減量化槽3に接種混合される。
しかして、通常25℃前後で3〜5日間好気条件下で作
用させ、余剰汚泥を溶菌し、粘液細菌体へと資化再構築
し、呼吸などに伴うロスに拠って汚泥を減量化する。
Myxobacteria 12 to be inoculated into the sludge reduction tank 3
A liquid mixed culture may be used, or a so-called dry cell obtained by culturing myxobacteria in a liquid medium and / or a solid medium, separating and concentrating the cells by ordinary means, and freeze-drying the cells. May be used. Furthermore, the combined use of both types of cells does not hinder the present invention. These inoculum cells 12 are inoculated and mixed into the sludge reduction tank 3 by any means such as shower, spray, injector or simple piping.
Thus, it is usually allowed to act under aerobic conditions at about 25 ° C. for 3 to 5 days to lyse excess sludge, assimilate and reassemble into myxobacteria, and reduce the amount of sludge due to loss accompanying respiration and the like. .

【0012】なおかつ残存する汚泥は、活性汚泥の分解
残分と粘液細菌の再増殖分である。これらは、濃縮装置
7に導き、適当な濃度にまで濃縮し、必要により有機お
よび/または無機凝集剤を注入してから、通常使用され
ている脱水機8により残存汚泥を脱水し、脱水ケーキを
得る。濃縮装置7および脱水機8は従来の生物処理汚泥
用の装置がいずれも使用できる。また、残存汚泥を脱水
するに先立ち、濃縮初沈汚泥14および/または凝集汚
泥15と混合してから脱水すれば効果的である。上記固
液分離手段は勿論他の手段によることができる。
[0012] The remaining sludge is a residue of decomposition of activated sludge and a regrowth of slime bacteria. These are led to a concentration device 7, concentrated to an appropriate concentration, and if necessary, an organic and / or inorganic coagulant is injected. Then, the remaining sludge is dewatered by a commonly used dehydrator 8, and the dewatered cake is dried. obtain. As the concentrating device 7 and the dehydrating device 8, any conventional device for biologically treated sludge can be used. Further, it is effective to mix the concentrated sludge 14 and / or the coagulated sludge 15 and then dehydrate the remaining sludge before dehydrating the remaining sludge. The solid-liquid separation means can be of course another means.

【0013】この分離液10(余水)中には、若干の粘
液細菌と粘液細菌によって溶菌された余剰汚泥中の菌体
内容物が一部資化されずに溶存している。菌体内容物は
主に易分解性有機物であり、引いてはBOD成分となる
ので余水分配管9によって系外に取り出し、し尿、下水
あるいは有機性排水の生物処理装置1に合流せしめて処
理すると効率的であり好ましい。あるいは、別個に独立
して設けられた生物処理工程11に導入し、前記BOD
成分を分解してから外部に放流すればよい。これらの生
物処理工程1および11としては、通常の活性汚泥処
理、担体投入型の流動床式生物膜処理など既往の生物処
理方法が適宜適用できる。また、生物処理によらない方
法で分離液10の処理を行うことも妨げない。
In this separated liquid 10 (spill water), some mucous bacteria and the cell content in excess sludge lysed by the mucus bacteria are dissolved without being partially utilized. Since the cell content is mainly an easily decomposable organic substance and becomes a BOD component, it is taken out of the system through the residual water pipe 9 and is combined with the biological treatment apparatus 1 for night soil, sewage or organic waste water to be treated. Efficient and preferred. Alternatively, the BOD is introduced into the biological treatment step 11 provided separately and independently,
The components may be decomposed and then discharged to the outside. As these biological treatment steps 1 and 11, existing biological treatment methods such as ordinary activated sludge treatment and fluidized-bed type biofilm treatment with a carrier input can be appropriately applied. In addition, the treatment of the separation liquid 10 by a method not based on biological treatment is not prevented.

【0014】なお、余水中に若干含まれる粘液細菌は、
活性汚泥中のBOD資化菌などに比較すると増殖速度が
かなり遅いことなどにより、活性汚泥の運用に何ら支障
をきたさないが、運転状態の悪化が懸念されるようであ
れば通常のMF膜程度で除去すればよい。近年進歩が著
しい膜分離型活性汚泥法に適用すれば、特に好ましいシ
ステムが構築できる。
[0014] The myxobacteria slightly contained in the sewage are:
It does not hinder the operation of activated sludge at all due to the fact that its growth rate is much slower than that of BOD-utilizing bacteria in activated sludge. Should be removed with. A particularly preferable system can be constructed by applying the method to a membrane separation type activated sludge method which has remarkably progressed in recent years.

【0015】一方、分離汚泥中には濃縮された粘液細菌
が存在するので、返送配管によって減量化槽に返送すれ
ば繰り返し使用でき、これが種菌として安定するに至れ
ば、新たな粘液細菌の接種は不要となる。ただし、初期
の増菌培養や、何らかの事故による粘液細菌の減少に備
えるため、粘液細菌の培養設備を本発明の施設近傍に設
けたり、外部からの移送手段を用意することは好ましい
配慮であり、これを妨げるものではない。
On the other hand, since the separated sludge contains concentrated myxobacteria, it can be used repeatedly if it is returned to the reduction tank via a return pipe. If this becomes stable as a seed, inoculation of new myxobacteria is not possible. It becomes unnecessary. However, in order to prepare for the initial enrichment culture or the reduction of myxobacteria due to some accident, it is preferable to provide a myxobacterium culture facility near the facility of the present invention, or to prepare an external transfer means, It does not prevent this.

【0016】(作用)本発明の微生物による余剰汚泥の
減量化法は、微生物、例えばミクソコッカス(Myxo
coccus)属やスティグマテラ(Stigmate
lla)属、シストバクター(Cystobacte
r)属、メリタンギウム(Melittangium)
属を含む粘液細菌が好気的な条件で菌体外に溶菌酵素を
分泌し、粘液細菌の菌体の周辺に存在する他の生菌体を
溶菌し、自己の栄養源として利用して増殖することに着
目した全く新規の余剰汚泥の減量化法である。本発明に
用いる粘液細菌の特徴は、捕食に関する特異性は低く、
菌外に生産する溶菌酵素によって汚泥中に存在する広い
範囲の微生物に作用し溶解するため確実に汚泥の減量化
が達成される。
(Action) The method of the present invention for reducing excess sludge using microorganisms is carried out by using microorganisms such as Myxococcus (Myxococcus).
genus or Stigmate
lla) genus, Cystobacter
r) genus, Melittangium
Myxobacteria including the genus secrete lytic enzymes outside of the cells under aerobic conditions, lyse other viable cells around the myxobacteria, and use them as their own nutrient sources for growth This is a completely new method of reducing excess sludge, which focuses on doing so. The characteristics of the slime bacteria used in the present invention have low specificity regarding predation,
The lytic enzyme produced outside the bacteria acts on and dissolves a wide range of microorganisms present in the sludge, so that the sludge can be reliably reduced.

【0017】他の余剰汚泥中の細菌は、外部に利用でき
る有機物が枯渇した状態のため増殖できないが、本発明
に利用する粘液細菌は上記の作用により、この様な条件
下でも他種菌体を有機物源として増殖するのである。ま
た、粘液細菌は複雑な生活環をもっているためにエネル
ギー効率が低く、利用した食源の菌体転換率が低い。従
って、有機物が粘液細菌の菌体として再構築される際の
歩留りが悪く、減量化の効果が大きい。本発明により最
終的な余剰汚泥量を1/2量以下とすることができ、従
来の厄介な汚泥処理から解放される。
The bacteria in other surplus sludge cannot be proliferated due to the depletion of organic substances available to the outside. However, the slime bacteria used in the present invention cannot be grown under the above-mentioned conditions even under such conditions. Grow as a source of organic matter. In addition, since slime bacteria have a complicated life cycle, their energy efficiency is low, and the conversion rate of used food sources is low. Therefore, the yield when organic matter is reconstructed as mycelial bacteria is poor, and the effect of weight reduction is large. According to the present invention, the final excess sludge amount can be reduced to half or less, and the conventional troublesome sludge treatment is released.

【0018】[0018]

【実施例】以下、本発明を実施例により具体的に説明す
るが、本発明はこれに限定されるものではない。
EXAMPLES The present invention will be described below in more detail with reference to examples, but the present invention is not limited to these examples.

【0019】(実施例1)下記表2に示す供試した粘液
細菌6種類の菌株のそれぞれについて溶菌作用および機
能の確認を行った。し尿の硝化脱窒素プロセスから排出
される余剰活性汚泥(汚泥濃度約7,000mg/リッ
トル)を0.5リットルの丸底フラスコに取り、これに
表1の二員培養培地で増量培養した表2に示す各粘液細
菌の液状培養体を3cc/リットル加え、作用させた。
培養温度25℃、培養時間5日で振盪培養したところ、
それぞれの菌株によって若干の差異は認められたが、余
剰活性汚泥の菌体の細胞壁はほぼ完全に溶解され、液側
に吐出された菌体内容液は粘液細菌によって資化される
ことが認められた。
(Example 1) The lytic activity and function of each of the six strains of the myxobacteria shown in Table 2 below were confirmed. Excess activated sludge (sludge concentration of about 7,000 mg / liter) discharged from the nitrification and denitrification process of night soil was placed in a 0.5-liter round-bottom flask, and increased in volume in the two-membered culture medium in Table 1 to Table 2. 3 cc / liter of a liquid culture of each of the myxobacteria shown in (1) was added and allowed to act.
After shaking culture at a culture temperature of 25 ° C. and a culture time of 5 days,
Although there was a slight difference between each strain, it was found that the cell walls of the cells of the excess activated sludge were almost completely lysed, and the bacterial cell liquid discharged to the liquid side was assimilated by the slime bacteria. Was.

【0020】[0020]

【表1】 [Table 1]

【0021】*上記培地に加える生菌は大腸菌エシェリ
キア・コリ(Escherichiacoli)を用い
てもよいし、生物処理工程から餌菌を得ても良い。
* Escherichia coli (Escherichia coli) may be used as a live bacterium added to the above-mentioned medium, or a bait bacterium may be obtained from a biological treatment step.

【0022】[0022]

【表2】 [Table 2]

【0023】(実施例2)粘液細菌による減量化の対象
として、硝化液循環型の硝化脱窒素プロセスから排出さ
れる余剰活性汚泥を使用した。この余剰汚泥の一般的な
組成を表3に示す。
(Example 2) Excess activated sludge discharged from a nitrification liquid circulation type nitrification denitrification process was used as an object of weight reduction by slime bacteria. Table 3 shows the general composition of the excess sludge.

【0024】[0024]

【表3】 [Table 3]

【0025】一方、余剰汚泥を溶菌減量化する粘液細菌
としては、ミクソコッカス・キサンサスMyxococ
cus xanthus ATCC25232を選定し
た。微生物菌株保存機関(ATCC)より入手した細菌
の食餌生菌として市販のパン酵母を使用し、表1に示し
た二員培養用の培地を1リットルの丸底フラスコに50
0cc張り込み、該菌を2白金耳培養液に接種し、30
℃で5日間振盪培養(好気的に増量培養)した。
On the other hand, myxococcus xanthus myxococ is a slime bacterium that lytically reduces excess sludge.
cus xanthus ATCC 25232 was selected. Commercial baker's yeast was used as a dietary bacterium of the bacteria obtained from the Microbial Strain Conservation Agency (ATCC), and the medium for two-member culture shown in Table 1 was placed in a 1-liter round bottom flask.
0 cc, inoculate the bacteria into two platinum loop cultures,
Shaking culture (aerobic increasing culture) was performed at 5 ° C. for 5 days.

【0026】さらに、供試余剰活性汚泥として表3の試
料(1)を選び、1リットルの丸底フラスコ2個(A,
B)にそれぞれ500ccづつ張り込み、Aには前記の
ミクソコッカス・キサンサスの培養液を5cc、Bは対
照として25℃(常温)で5日間振盪培養し、5日後の
振盪培養液(A)、(B)について余剰汚泥中の有機物
濃度とその減少率を求めた。その結果を表4に示す。
Further, a sample (1) shown in Table 3 was selected as a test excess activated sludge, and two 1-liter round bottom flasks (A,
B) were filled with 500 cc each, and 5 cc of the culture solution of Myxococcus xanthus was used for A, and B was shake-cultured at 25 ° C. (normal temperature) for 5 days as a control. After 5 days, the shake culture solution (A), ( Regarding B), the concentration of organic matter in the excess sludge and the reduction rate thereof were determined. Table 4 shows the results.

【0027】[0027]

【表4】 [Table 4]

【0028】表4を見てもわかるように、粘液細菌ミク
ソコッカス・キサンサスによるし尿系余剰活性汚泥の減
量化は極めて顕著であった。
As can be seen from Table 4, the reduction of the excess activated sludge of the human waste system by the myxobacterium Myxococcus xanthus was extremely remarkable.

【0029】(実施例3)工場排水を実質的に含まない
団地下水を標準活性汚泥法で処理した余剰活性汚泥を選
定し、2種の粘液細菌を接種して減量化を実施した。先
ず、標準活性汚泥施設の曝気槽から活性汚泥混合液を1
0リットル採取し、通常の重力沈殿法で1.5時間静置
し、底部に沈殿濃縮された活性汚泥を供試試料とした。
この試料の分析値を表5に示す。
(Example 3) Excess activated sludge was prepared by treating the groundwater that had substantially no industrial wastewater by the standard activated sludge method, and inoculated with two kinds of slime bacteria to reduce the amount. First, 1 volume of the activated sludge mixture was supplied from the aeration tank of the standard activated sludge facility.
0 liter was collected, and left standing for 1.5 hours by a normal gravity sedimentation method, and activated sludge precipitated and concentrated at the bottom was used as a test sample.
Table 5 shows the analysis values of this sample.

【0030】[0030]

【表5】 [Table 5]

【0031】この濃縮余剰汚泥を1リットルの丸底フラ
スコ2個(A)、(B)に500ccづつ分注し、
(A)には前記の粘液細菌から下記(a)、(b)2種
を選定して増量培養液をそれぞれ2.5ccづつ接種
し、(B)は対象として菌株液を添加しなかった (a)ミクソコッカス・キサンサス(Myxococc
us xanthus ATCC25232) (b)ミクソコッカス・フルブス(Myxococcu
s fulvus ATCC23093) それぞれの粘液細菌の増量培養に使用した培地、培養条
件および培養方法は実施例2と同じである。
The concentrated excess sludge was dispensed into two 1-liter round bottom flasks (A) and (B) in 500 cc increments.
In (A), the following two types (a) and (b) were selected from the myxobacteria described above, and 2.5 cc of the increased culture solution was inoculated, respectively, and (B) was not added with the strain liquid as a control ( a) Myxococcus xanthus (Myxococc)
us xanthus ATCC25232) (b) Myxococcus fulbus
s fulbus ATCC 23093) The medium, culture conditions, and culture method used for increasing culture of each myxobacterium are the same as those in Example 2.

【0032】また、粘液細菌による濃縮活性汚泥の減量
化の実施もすべて実施例2に準拠した。その実施結果を
表6に示す。
Further, the reduction of the concentrated activated sludge by the myxobacteria was carried out in the same manner as in Example 2. Table 6 shows the results.

【0033】[0033]

【表6】 [Table 6]

【0034】表6に示したように、粘液細菌理ミクソコ
ッカス・キサンサスおよびミクソコッカス・フルブスの
2種の混合菌体液を使用しての下水系活性汚泥の減量化
試験でも汚泥の減量化は顕著であり、本発明は充分に実
用化の可能性があることが実証された。
As shown in Table 6, the sludge reduction was remarkable even in the test for reducing the amount of activated sewage sludge using the mixed bacterial body liquid of the two types of myxobacteria, Myxococcus xanthus and Myxococcus fulbus. Thus, it has been proved that the present invention has a sufficient possibility of practical use.

【0035】[0035]

【発明の効果】本発明によれば、上に詳述したように、
従来技術とは全く別の観点からの発明であり、次のよう
な作用効果を奏する。 (1) し尿処理、下水処理あるいは有機性排水の生物
学的処理、特に生物学的酸化処理の工程から排出される
極めて処理し難い大量の余剰汚泥に対して、その発生量
をほぼ半減することができる。 (2) 引いては、本発明を採用することにより、汚泥
処理施設は縮小され、処理費用も著しく低減される。
According to the present invention, as detailed above,
This is an invention from a completely different point of view from the prior art, and has the following operational effects. (1) To reduce the amount of waste sludge, sewage treatment or organic wastewater biological treatment, especially the large amount of excess sludge discharged from the biological oxidation treatment process, which is extremely difficult to treat, by almost half. Can be. (2) By adopting the present invention, the sludge treatment facility can be reduced and the treatment cost can be significantly reduced.

【0036】(3) 生物処理工程から排出される各種
の汚泥のうち、最も処理し難い余剰汚泥の発生量が半減
するために、トータルプロセスとしての汚泥処理、特に
脱水が極めて容易となる。 (4) 濃縮工程、脱水工程からの分離汚泥の一部を汚
泥減量化槽に循環返送する操作により接種すべき粘液細
菌の量を著しく低減することが可能であり、定常状態に
達すれば、粘液細菌の接種を省略できる。
(3) Of the various types of sludge discharged from the biological treatment step, since the amount of surplus sludge which is most difficult to treat is reduced by half, sludge treatment as a total process, particularly dewatering, becomes extremely easy. (4) The amount of myxobacteria to be inoculated can be significantly reduced by the operation of circulating and returning a part of the separated sludge from the concentration step and the dehydration step to the sludge reduction tank. Bacterial inoculation can be omitted.

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

【図1】本発明の方法ならびに装置の1例を示す構成図FIG. 1 is a block diagram showing an example of a method and an apparatus of the present invention.

【符号の説明】[Explanation of symbols]

1 生物処理槽 2 余剰汚泥濃縮槽 3 汚泥減量化槽 4 余剰汚泥 5 汚泥返送配管 7 濃縮装置 8 脱水機 9 余水分配管 10 分離水 11 生物処理工程 12 粘液細菌 13 空気 14 濃縮初沈汚泥 15 濃縮凝集汚泥 16 余水分配管 17 分離水 DESCRIPTION OF SYMBOLS 1 Biological treatment tank 2 Excess sludge concentration tank 3 Sludge reduction tank 4 Excess sludge 5 Sludge return piping 7 Concentrator 8 Dehydrator 9 Excess water piping 10 Separation water 11 Biological treatment process 12 Mucus bacteria 13 Air 14 Concentration primary sludge 15 Concentration Coagulated sludge 16 Residual water piping 17 Separated water

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 汚水の生物処理工程より排出される余剰
汚泥に溶菌作用を有する粘液細菌の単一菌株または複数
菌株を接種し、好気条件下で作用させることを特徴とす
る余剰汚泥の微生物学的減量化方法。
1. A microorganism for surplus sludge characterized by inoculating surplus sludge discharged from a biological treatment step of sewage with a single strain or a plurality of strains of lytic bacteria having a bacteriolytic action, and allowing them to act under aerobic conditions. Biological weight loss method.
【請求項2】 汚水の生物処理工程より排出される余剰
汚泥に溶菌作用を有する粘液細菌の単一菌株または複数
菌株を接種し、好気条件下で作用させる減量化工程と、
減量化工程より排出される減量化汚泥を固液分離する工
程を有すると共に、固液分離された分離汚泥の一部を前
記減量化工程に循環返送することを特徴とする余剰汚泥
の微生物学的減量化方法。
2. A reduction step of inoculating surplus sludge discharged from a biological treatment step of sewage with a single strain or a plurality of strains of myxobacteria having a bacteriolytic action, and acting under aerobic conditions.
A microbiological method of surplus sludge characterized by having a step of solid-liquid separation of the reduced sludge discharged from the reduction step, and circulating and returning a part of the separated sludge subjected to the solid-liquid separation to the reduction step. Weight loss method.
【請求項3】 汚水の生物処理工程より排出される余剰
汚泥に溶菌作用を有する粘液細菌の単一菌株または複数
菌株を接種し、好気条件下で作用させる減量化工程と、
減量化工程より排出される減量化汚泥を固液分離する工
程を有すると共に、固液分離された分離汚泥の一部を前
記減量化工程に循環返送し、分離液を生物処理工程に導
くことを特徴とする余剰汚泥の微生物学的減量化方法。
3. A weight-reducing step in which a surplus sludge discharged from a biological treatment step of sewage is inoculated with a single strain or a plurality of strains of myxobacteria having a bacteriolytic action and allowed to act under aerobic conditions;
It has a step of solid-liquid separation of the reduced sludge discharged from the weight reduction step, and circulates and returns a part of the separated sludge subjected to the solid-liquid separation to the weight reduction step, thereby leading the separated liquid to the biological treatment step. Characteristic method for microbiological reduction of excess sludge.
【請求項4】 酸素含有気体の導入手段を有する汚泥減
量化槽と、汚泥減量化槽より排出される減量化汚泥を固
液分離する固液分離装置を備えると共に、固液分離され
た分離汚泥の一部を前記汚泥減量化槽に導く手段と、分
離液を生物処理装置に導く手段を有することを特徴とす
る余剰汚泥の微生物学的減量化装置。
4. A sludge reduction tank having means for introducing an oxygen-containing gas, a solid-liquid separation device for solid-liquid separation of reduced sludge discharged from the sludge reduction tank, and a solid-liquid separated sludge. A means for guiding a part of the sludge to the sludge reduction tank, and a means for guiding the separated liquid to the biological treatment apparatus.
JP4281037A 1992-09-28 1992-09-28 Method and apparatus for microbiological reduction of excess sludge Expired - Lifetime JP2572334B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4281037A JP2572334B2 (en) 1992-09-28 1992-09-28 Method and apparatus for microbiological reduction of excess sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4281037A JP2572334B2 (en) 1992-09-28 1992-09-28 Method and apparatus for microbiological reduction of excess sludge

Publications (2)

Publication Number Publication Date
JPH06106198A JPH06106198A (en) 1994-04-19
JP2572334B2 true JP2572334B2 (en) 1997-01-16

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ID=17633418

Family Applications (1)

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103249682A (en) * 2010-12-17 2013-08-14 通用电气公司 Biochemical process for selenium recovery from bioremediation effluent or sludge

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2836910B1 (en) * 2002-03-08 2005-02-11 Amenagement Urbain & Rural METHOD OF DEGRADING ORGANIC MATTER THROUGH MYCELIA
JP6666000B2 (en) * 2015-07-31 2020-03-13 国立研究開発法人産業技術総合研究所 Sludge volume reduction method and membrane-separated activated sludge treatment apparatus using the same
CN114573095B (en) * 2022-03-10 2023-09-26 西安建筑科技大学 Biological denitrification, sludge reduction and increased heat production water treatment operation method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5534176A (en) * 1978-09-04 1980-03-10 Hitachi Ltd Aerobic digestion method of sludge
JPS61129098A (en) * 1984-11-27 1986-06-17 Nishihara Environ Sanit Res Corp Method for reducing quantity of sludge
JPH0732920B2 (en) * 1988-07-08 1995-04-12 日本碍子株式会社 Enzymatic modification and concentration method of organic sludge

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103249682A (en) * 2010-12-17 2013-08-14 通用电气公司 Biochemical process for selenium recovery from bioremediation effluent or sludge

Also Published As

Publication number Publication date
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