JPH06106198A - Method and device for microbiological reduction of amount of surplus sludge - Google Patents

Method and device for microbiological reduction of amount of surplus sludge

Info

Publication number
JPH06106198A
JPH06106198A JP4281037A JP28103792A JPH06106198A JP H06106198 A JPH06106198 A JP H06106198A JP 4281037 A JP4281037 A JP 4281037A JP 28103792 A JP28103792 A JP 28103792A JP H06106198 A JPH06106198 A JP H06106198A
Authority
JP
Japan
Prior art keywords
sludge
surplus sludge
surplus
bacteria
solid
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.)
Granted
Application number
JP4281037A
Other languages
Japanese (ja)
Other versions
JP2572334B2 (en
Inventor
Taisuke Toya
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 Research Co Ltd
Ebara Infilco Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ebara Research Co Ltd, Ebara Infilco Co Ltd filed Critical Ebara Research Co Ltd
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

Links

Abstract

PURPOSE:To obtain a bacteriolytic action without the need of any special auxiliary equipment and a method for reducing the amt. of surplus sludge through recycling of bacteria by a method wherein the surplus sludge discharged from a process for biological treatment of dirty water is inoculated with one or more strans of the slime bacteria having a bacteriolytic action and the surplus sludge is subjected to the action of the bacteria in an aerobic condition. CONSTITUTION:The method for microbiological reduction of the amt. of surplus sludge includes introducing surplus sludge 4 from a microbiological treating tank into a surplus solid concn. tank 2 to concentrate the same to about 20,000-30,000mg/l; thereafter sending the surplus sludge 4 into a sludge amt. reducing tank 3; inoculating the surplus sludge 4 in the sludge amt. reducing tank 3 with a biomass 12 consisting of one or more strains of the slime bacteria having a bacteriolytic action on the surplus sludge 4 by using any one of supply means such as shower, sprayer, injector and simple pipe; and subjecting the surplus sludge 4 to the action of the inoculated bacteria for 3-5 days at a normal temp. of around 25 deg.C in an aerobic condition, whereby the surplus sludge 4 is bacteriolyzed, the slime bacteria is reconstructed by assimilation and the amt. of the surplus sludge 4 is reduced due to a loss entailed by the respiration of the bacteria.

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 The present invention has a bacteriolytic action that allows surplus sludge generated in the course of microbiologically treating wastewater such as human waste, sewage and / or organic wastewater to be widely distributed in nature. The present invention relates to a microbiological weight reduction method for excess sludge that is 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, excessive sludge generated from biological treatment of human waste, sewage and / or organic wastewater, particularly aerobic biological treatment, has a huge amount of generation.
The processing and disposal of them requires consumption of large amounts of energy and resources.

【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。
Currently, there are about 1, 2 human waste treatment sites in Japan.
00 places, sewage treatment plant (urban sewage) is 800-1, 00
There are 0 places, and even if the treatment of organic wastewater is excluded, the amount of surplus sludge to be treated and disposed of will be enormous. Although some of these excess sludges are effectively used, most of the excess sludges are concentrated and the dehydration auxiliary is added to the excess sludges to dehydrate them by mechanical means or method to obtain a water content of 80 to 85%. And then
A large amount of energy and resources for incineration in an incinerator are input and treated and disposed of. However, as the amount of surplus sludge increases, the facility for concentrating and dehydrating is inevitably increased in size, and the dehydration rate is also limited, and the incinerator is required to process a large amount. For this reason, each local government is not only struggling with the economic burden of treatment / disposal, but also from the perspective of technical measures against secondary pollution such as air pollution and water pollution, and global warming. Are being asked for a solution.

【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。
Therefore, a method for reducing the amount of excess sludge generated has been sought. For example, in sewage treatment, etc., excess sludge and first settling basin (hereinafter referred to as “first settling”) are each concentrated and then mixed at a generation rate, and methane fermentation (anaerobic digestion) is applied to reduce excess sludge. Has been. However, since surplus sludge is, as it were, surplus bacterial cells of activated sludge microorganisms, the decomposition rate of the cell walls and cell membranes of the bacterial cells is poor in ordinary methane fermentation treatment, and it takes about 20 to 30 days for digestion days, which is required for the equipment. 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, a microbiological method for destroying cell walls and cell membranes of cells without depending on digestion has been investigated. For example, Japanese Unexamined Patent Publication No. 61-129098 proposes a method of adding bacteriophage to sludge generated by biological treatment of wastewater, and reducing the amount of sludge by the bacteriolytic action. However, bacteriophages are extremely host-specific, and certain bacteriophages parasitize and lyse only certain bacteria. Therefore, when trying to reduce the amount of sludge in a mixed culture system of multiple bacterial species such as activated sludge with bacteriophage, practically the same number of types of bacteriophage as the bacterial species inhabiting activated sludge are screened from the natural world and formulated. It is necessary 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。
Furthermore, the destroyed bacterial contents are released into water, which causes new organic pollution. In the above-mentioned patent publication, the organic matter released seems to be bacteriophage, but the virus containing bacteriophage is an extremely minute particle of colloidal level, as it was called a filterable pathogen in the old days, and it can be separated by solid-liquid separation. Removal is not easy. In the patent publication, the separated water that has been subjected to solid-liquid separation is discharged, but it is clear that a large number of bacteriophages are contained in this and this becomes a new contaminant. On the other hand, it is easy to think of introducing some kind of purification device,
When it is returned to the biological treatment process, the activated sludge is inoculated with a bacteriophage solution having an extremely high lytic power, which may impair 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, a means for treating bacteriophage must be provided, but as described above, the virus has a colloidal size, and it is not possible to carry out the usual precipitation and separation, and it is also possible to use the usual filtration method. Separation is difficult,
It is necessary to separate by ultrafiltration or reverse osmosis filtration equipment. Alternatively, inactivating / sterilizing means must be provided, and in some cases, a disinfection device for the disinfectant used therefor is also required. As a result, the number of ancillary facilities is enormous and it is extremely difficult to put them to 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 It is an object of the present invention to develop a sludge reduction method and a sludge reduction device suitable for the method, which does not require special incidental equipment, by lysing and reutilizing 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 purpose of reducing sludge, the present inventors have used surplus sludge by a lytic enzyme produced outside mycelia by myxobacteria, which are in general distribution in nature. The present invention has been made paying attention to the action of lysing bacterial cells such as BOD-assimilating bacteria, which is the main constituent bacterium, and assimilating them to self-cell construction. That is, the above-mentioned object is achieved by the development of the method and apparatus for reducing the amount of surplus sludge by the present invention. 1) Microbiological weight loss of surplus sludge, which is characterized by inoculating surplus sludge discharged from the biological treatment process of wastewater with a single strain or multiple strains of myxobacteria having a bacteriolytic action and operating under aerobic conditions. Method. 2) The 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 a weight reduction process in which the strains are allowed to act under aerobic conditions, and a waste reduction process is performed. A method for microbiologically reducing excess sludge, comprising the step of solid-liquid separating the reduced sludge, and recycling a part of the solid-liquid separated separated sludge to the reducing step. 3) The excess sludge discharged from the biological treatment process of wastewater is inoculated with a single strain or multiple strains of myxobacteria having a bacteriolytic action, and the sludge is discharged from the reduction process and the reduction process in which it is allowed to act under aerobic conditions. Microorganisms of excess sludge characterized by having a step of solid-liquid separation of the reduced sludge, and circulating and returning part of the solid-liquid separated separation sludge to the reduction step, and guiding the separated liquid to a biological treatment step. Weight reduction method. And 4) a sludge reduction tank having a means for introducing an oxygen-containing gas,
A solid-liquid separator for solid-liquid separation of the reduced sludge discharged from the sludge reduction tank is provided, and means for guiding a part of the solid-liquid separated separated sludge to the sludge reduction tank, and biological treatment of the separated liquid. An apparatus for reducing the amount of excess sludge by a microbiological method, which comprises means for guiding the apparatus. 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, the embodiment of the present invention is 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 thickening tank 2, and the excess sludge concentration of 20,0
After being concentrated to about 00 to 30,000 mg / liter, it is transferred to the sludge reduction tank 3. On the other hand, it is advisable that the slime bacterium used for reducing the surplus of bacterial cells is subjected to increasing culture of one or more kinds of original strains from the natural world, and then used as seed bacteria for reducing sludge. In addition, it is also possible to select a strain having an excellent lytic action from among the strains distributed by the preservation organization 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 inoculated into the sludge reduction tank 3
May be a liquid mixed culture, 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 an ordinary means, and freeze-drying the cells. May be used. Furthermore, the combined use of both types of bacterial 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 a shower, a spray, an injector or simple piping.
Then, it is usually operated at around 25 ° C for 3 to 5 days under aerobic conditions to lyse excess sludge, rebuild assimilate into slime bacteria, and reduce sludge due to loss associated with respiration. .

【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。
The remaining sludge is the decomposition residue of activated sludge and the re-propagation of slime bacteria. These are led to a concentrating device 7, concentrated to an appropriate concentration, and if necessary, an organic and / or inorganic coagulant is injected, and then the remaining sludge is dehydrated by a dehydrator 8 which is usually used to form a dehydrated cake. obtain. As the concentrating device 7 and the dehydrator 8, any conventional device for biological treatment sludge can be used. Further, it is effective to mix the concentrated sludge 14 and / or the coagulated sludge 15 before dehydrating the residual sludge and then dehydrate it. Of course, the solid-liquid separation means may be other 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 of the mycelial bacteria and the bacterial cell contents in the excess sludge lysed by the mycobacterium are dissolved without being assimilated. Since the bacterial cell contents are mainly easily decomposable organic substances and, in turn, become BOD components, they are taken out of the system by the excess water pipe 9 and merged with the biological treatment apparatus 1 for human waste, sewage or organic waste water for treatment. Efficient and preferred. Alternatively, the BOD is introduced into the biological treatment step 11 which is separately and independently provided.
The components may be decomposed and then discharged to the outside. For these biological treatment steps 1 and 11, conventional biological treatment methods such as ordinary activated sludge treatment and carrier-introduced fluidized bed biofilm treatment can be appropriately applied. Further, the treatment of the separated liquid 10 by a method that does not depend on biological treatment is not hindered.

【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。
The myxobacteria slightly contained in the residual water are
It does not hinder the operation of activated sludge due to its slow growth rate compared to BOD assimilating bacteria in activated sludge, etc. It can be removed with. If applied to the membrane separation type activated sludge method, which has made remarkable progress in recent years, a particularly preferable system can be constructed.

【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 concentrated myxobacteria are present in the separated sludge, it can be used repeatedly if it is returned to the weight-reducing tank through the return pipe, and if it becomes stable as an inoculum, new inoculation of myxobacteria is not possible. It becomes unnecessary. However, in order to prepare for the initial enrichment culture and the reduction of myxobacteria due to some accident, it is preferable consideration to provide a culture facility for myxobacteria near the facility of the present invention or to prepare a transfer means from the outside. 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。
(Function) The method for reducing excess sludge by the microorganism of the present invention is a microorganism, for example, Myxococcus (Myxo).
genus Coccus and Stigmatera
Lla), Cystobacter
r) genus, Melittangium
Myxobacteria including genus secrete lytic enzymes outside the microbial cells under aerobic conditions, lyse other viable microbial cells that exist around the mycelial bacterium, and use them as their own nutrient sources for growth. This is a completely new method of reducing excess sludge, focusing on the fact that The characteristic of the myxobacteria used in the present invention is that the specificity for predation is low,
The lytic enzyme produced outside the bacteria acts on and dissolves a wide range of microorganisms present in the sludge, so that the reduction of the sludge can be reliably achieved.

【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 the other excess sludge cannot grow because the organic substances available to the outside are depleted. However, the myxobacteria used in the present invention have the above-mentioned effects, and thus the bacteria of other species can be grown under such conditions. Propagate as a source of organic matter. Further, since myxobacteria have a complicated life cycle, their energy efficiency is low, and the conversion rate of the food source used is low. Therefore, the yield is low when the organic matter is reconstructed as myxobacterial cells, and the effect of weight reduction is great. According to the present invention, the final excess sludge amount can be reduced to ½ amount 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 specifically described below with reference to examples, but the present invention is not limited thereto.

【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 action and function of each of the 6 types of strains of the tested 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 human waste was placed in a 0.5-liter round bottom flask, and expanded culture was performed with the two-membered culture medium of Table 1 The liquid culture of each myxobacteria shown in (3) was added and allowed to act at 3 cc / liter.
When shaking culture was carried out at a culture temperature of 25 ° C. and a culture time of 5 days,
Although a slight difference was observed depending on each strain, it was confirmed that the cell walls of the surplus activated sludge cells were almost completely dissolved and that the cell content liquid discharged to the liquid side was assimilated by myxobacteria. It 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 viable bacterium added to the above-mentioned medium, or a prey may be obtained from the 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 solution circulation type nitrification and denitrification process was used as a target for weight reduction by slime bacteria. The general composition of this excess sludge is shown in Table 3.

【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, as myxobacteria for lysing and reducing the excess sludge, there are Myxococcus xanthus Myxococ.
cus xanthus ATCC 25232 was selected. Using commercially available baker's yeast as a dietary bacterium of bacteria obtained from the microbial strain preservation organization (ATCC), the medium for two-membered culture shown in Table 1 was placed in a 1-liter round bottom flask.
Inoculate 0 cc, inoculate the fungus into 2 platinum loop culture solution,
The cells were cultivated at 5 ° C. for 5 days with shaking (aerobic growth culture).

【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, the sample (1) shown in Table 3 was selected as the test surplus activated sludge, and two 1 liter round bottom flasks (A,
500 cc each in B), 5 cc of the above-mentioned Myxococcus xanthus culture solution in A, and B as a control for 5 days at 25 ° C. (room temperature) with shaking culture, and after 5 days with shaking culture solution (A), ( Regarding B), the concentration of organic matter in the excess sludge and its reduction rate were obtained. The results are shown in Table 4.

【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 amount of excess activated sludge of night soil caused by the myxobacteria 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) A surplus activated sludge obtained by treating the group groundwater substantially free from factory wastewater by the standard activated sludge method was selected, and two kinds of slime bacteria were inoculated to reduce the weight. First, add the activated sludge mixture from the aeration tank of the standard activated sludge facility.
0 liter was sampled and allowed to stand for 1.5 hours by the usual gravity precipitation method, and the activated sludge that had been precipitated and concentrated at the bottom was used as a test sample.
The analytical values of this sample are shown in Table 5.

【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。
This concentrated excess sludge was dispensed into two 1-liter round bottom flasks (A) and (B) in 500 cc aliquots,
(A) was inoculated with 2.5 cc each of the following two types (a) and (b) selected from the above-mentioned myxobacteria and 2.5 cc each of them was inoculated, and (B) was not added with the strain solution. a) Myxococcus xanthus
us xanthus ATCC25232) (b) Myxococcus fulbus
s fulvus ATCC23093) The medium, the culture conditions and the culture method used for the expansion culture of each myxobacteria are the same as 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 concentration of the concentrated activated sludge by the myxobacteria was all carried out in accordance with Example 2. The execution results are shown in Table 6.

【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 reduction of sludge was remarkable even in the reduction test of sewage system activated sludge using a mixed bacterial cell liquid of two kinds of myxobacteria Myxococcus xanthus and Myxococcus fulbus. Therefore, it was demonstrated that the present invention has a sufficient possibility of practical application.

【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,
It is an invention from a completely different viewpoint from the prior art, and has the following operational effects. (1) To almost halve the amount of excess sludge that is extremely difficult to treat discharged from human waste treatment, sewage treatment or biological treatment of organic wastewater, especially biological oxidation treatment. You can (2) In addition, by adopting the present invention, the sludge treatment facility can be reduced in size and the treatment cost can be remarkably 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 sludges discharged from the biological treatment process, the generation amount of surplus sludge, which is the most difficult to treat, is halved, so sludge treatment as a total process, particularly dehydration, becomes extremely easy. (4) It is possible to significantly reduce the amount of myxobacteria to be inoculated by circulating and returning a part of the separated sludge from the concentration step and dehydration step to the sludge reduction tank. Inoculation of bacteria can be omitted.

【図面の簡単な説明】[Brief description of 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 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 1 Biological Treatment Tank 2 Excess Sludge Concentration Tank 3 Sludge Reduction Tank 4 Excess Sludge 5 Sludge Return Pipe 7 Concentrator 8 Dehydrator 9 Excess Moisture Pipe 10 Separation Water 11 Biotreatment Process 12 Mucus Bacteria 13 Air 14 Concentration Initial Sludge 15 Concentration Coagulated sludge 16 Surplus water pipe 17 Separation water

Claims (4)

【特許請求の範囲】[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 surplus sludge microorganism characterized in that surplus sludge discharged from a biological treatment process of wastewater is inoculated with a single strain or multiple strains of myxobacteria having a bacteriolytic action and allowed to act under aerobic conditions. Weight reduction 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 weight-reducing step in which surplus sludge discharged from the biological treatment step of wastewater is inoculated with a single strain or a plurality of strains of myxobacteria having a bacteriolytic action and allowed to act under aerobic conditions.
Microbiology of excess sludge characterized by having a step of solid-liquid separation of the reduced sludge discharged from the weight reduction step, and recycling a part of the solid-liquid separated separation sludge to the weight reduction step Weight reduction 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 surplus sludge discharged from the biological treatment step of wastewater is inoculated with a single strain or multiple strains of myxobacteria having a bacteriolytic action and allowed to act under aerobic conditions.
In addition to having a step of solid-liquid separation of the reduced sludge discharged from the weight reduction step, a part of the solid-liquid separated separation sludge is circulated back to the weight reduction step to guide the separated liquid to the biological treatment step. A method for reducing the amount of excess sludge by a microbe.
【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 separation sludge that is solid-liquid separated, including a sludge reduction tank having a means for introducing an oxygen-containing gas, and a solid-liquid separation device for solid-liquid separation of the reduction sludge discharged from the sludge reduction tank. And 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)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005526595A (en) * 2002-03-08 2005-09-08 ソシエート ダメナゲメント アーバイン エト ルーラル Treatment method of sludge in purification facilities by mycelium means
JP2017029925A (en) * 2015-07-31 2017-02-09 国立研究開発法人産業技術総合研究所 Sludge volume reduction method, and activated sludge treatment apparatus of membrane separation type using the same
CN114573095A (en) * 2022-03-10 2022-06-03 西安建筑科技大学 Biological denitrification, sludge reduction and hot water production increase treatment operation method and sludge thereof

Families Citing this family (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

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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
JPH0222000A (en) * 1988-07-08 1990-01-24 Ngk Insulators Ltd Method for modifying and concentrating organic sludge with enzyme

Patent Citations (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
JPH0222000A (en) * 1988-07-08 1990-01-24 Ngk Insulators Ltd Method for modifying and concentrating organic sludge with enzyme

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005526595A (en) * 2002-03-08 2005-09-08 ソシエート ダメナゲメント アーバイン エト ルーラル Treatment method of sludge in purification facilities by mycelium means
JP2017029925A (en) * 2015-07-31 2017-02-09 国立研究開発法人産業技術総合研究所 Sludge volume reduction method, and activated sludge treatment apparatus of membrane separation type using the same
CN114573095A (en) * 2022-03-10 2022-06-03 西安建筑科技大学 Biological denitrification, sludge reduction and hot water production increase treatment operation method and sludge thereof
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

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