JP3400953B2 - Method for regenerating microflora and enhancing physical strength in activated sludge treatment - Google Patents

Method for regenerating microflora and enhancing physical strength in activated sludge treatment

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Publication number
JP3400953B2
JP3400953B2 JP04864999A JP4864999A JP3400953B2 JP 3400953 B2 JP3400953 B2 JP 3400953B2 JP 04864999 A JP04864999 A JP 04864999A JP 4864999 A JP4864999 A JP 4864999A JP 3400953 B2 JP3400953 B2 JP 3400953B2
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Japan
Prior art keywords
bacteria
bacterium
activated sludge
regenerating
aeration tank
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 - Fee Related
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JP04864999A
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Japanese (ja)
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JP2000246281A (en
Inventor
正憲 飯田
Original Assignee
株式会社イイダ微研
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Priority to JP04864999A priority Critical patent/JP3400953B2/en
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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

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Activated Sludge Processes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

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、好気性の活性汚泥
処理に於いて、BOD及びCOD成分の除去率の低下を
起こしてきた曝気槽の微生物相の再生及び体力増強方
法、即ち、活性汚泥処理に於ける微生物相の再生及び体
力増強方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for regenerating microbial flora in an aeration tank which has caused a decrease in the removal rate of BOD and COD components in aerobic activated sludge treatment, and a method for enhancing physical strength, that is, activated sludge. The present invention relates to a method of regenerating microbial flora in treatment and enhancing physical strength.

【0002】[0002]

【従来の技術】各種製造工場から排出される廃水は、一
般に、好気性の微生物相による活性汚泥処理によって浄
化される場合が多い。しかし製造工程から排出される廃
水の水質がほぼ一定であれば、安定した処理が可能であ
るが、時として、廃水中の各種汚濁成分の濃度が急激に
変動したり、pHの急激な変動が生じたり、油脂分が多量
に混入したりすると、活性汚泥処理装置の曝気槽に生息
し汚濁物質の浄化処理を司る微生物相にダメージを与え
ることとなって、次第に処理能力の低下、即ち、BOD
及びCOD成分の除去率の低下をきたすようになる。
2. Description of the Related Art Wastewater discharged from various manufacturing plants is generally purified by treatment of activated sludge with aerobic microflora. However, if the quality of the wastewater discharged from the manufacturing process is almost constant, stable treatment is possible, but sometimes the concentration of various pollutant components in the wastewater fluctuates rapidly or the pH fluctuates rapidly. If it is generated or a large amount of oil and fat is mixed, it will damage the microflora inhabiting the aeration tank of the activated sludge treatment device and controlling the purification treatment of pollutants, and the treatment capacity will gradually decrease, that is, the BOD.
In addition, the removal rate of COD components decreases.

【0003】また、中でも油脂分が多量に混入した場合
には問題は深刻で、曝気槽の表面がネバネバとした油膜
で覆われるようになり、槽内の溶存酸素量は低下し、次
第に嫌気性状態となって微生物相は死滅することにもな
る。
[0003] Above all, when a large amount of oil and fat is mixed, the problem is serious, and the surface of the aeration tank is covered with a sticky oil film, and the amount of dissolved oxygen in the tank is lowered, and gradually anaerobic. The state will also kill the microflora.

【0004】しかし、このような曝気槽の微生物相のダ
メージも少々のことであれば、その微生物相が持ってい
る自治作用や耐性によって回復することができるが、度
重なる急激な変動によって微生物相自体の体力が弱って
しまっている場合には、回復することができず、微生物
相の状態も変化して、BOD及びCOD成分の除去率の
低下する日が続くようになってくる。
However, if the damage to the microbial flora in such an aeration tank is slight, it can be recovered by the autonomy and resistance of the microbial flora. When the physical strength of the body itself is weakened, it cannot be recovered, the state of the microflora also changes, and the days when the removal rates of BOD and COD components decrease will continue.

【0005】一般にこのような活性汚泥処理の能力の低
下した状態、即ち、BOD及びCOD成分の除去率の低
下を起こすようになった状態はバルキング状態と呼ばれ
ているが、これは微生物相の状態の変化であるため、一
朝一夕に回復させることは極めてむずかしく、その回復
には数週間から数カ月もの期間がかかる場合もある。
Generally, such a state in which the ability of activated sludge treatment is lowered, that is, a state in which the removal rate of BOD and COD components is lowered is called a bulking state. Due to changes in condition, it is extremely difficult to recover overnight, and recovery can take weeks or even months.

【0006】このような状態になった時には、通常、先
ず、曝気槽に導入する原廃水の流入量を減少させて汚濁
物質の負荷量を軽減させるべきこととなるが、直ちに、
工場の稼働を部分的にも停止させることは容易にできる
ものではなく、曝気槽の微生物相には無理やり過酷な処
理が強いられることとなって、益々状態は悪化の一途を
たどることとなることが多い。
[0006] When such a situation occurs, it is usually necessary to first reduce the inflow of raw wastewater introduced into the aeration tank to reduce the load of pollutants, but immediately
It is not easy to stop the operation of the plant even partially, and the microbial flora in the aeration tank will be forced to undergo severe treatment, and the condition will continue to worsen. There are many.

【0007】このようなバルキング状態発生の予防策及
び発生した場合の対応策には、これまでにもいろいろと
考えられている。例えば、その予防策としては、急激な
各種汚濁成分の濃度変化や急激なpHの変動には、曝気槽
に原廃水が導入される前段階の部位にセンサとアラーム
とを設置して、異常時には、センサからの検出信号に基
づいて警報を発するように構成し、これを受けた管理者
が手動により又は自動的に原廃水の流れを変え、バイパ
スによって別のピットに退避するようにすることであ
る。
Various preventive measures against the occurrence of such a bulking state and countermeasures against the occurrence of such a bulking condition have been considered so far. For example, as a preventive measure, if there is a sudden change in the concentration of various pollutants or a sudden change in pH, install a sensor and an alarm at the site before the raw wastewater is introduced into the aeration tank. By configuring to issue an alarm based on the detection signal from the sensor, the administrator who receives this can manually or automatically change the flow of raw wastewater and evacuate to another pit by bypass. is there.

【0008】また、油脂分の混入に対しては、曝気槽に
導入される前の段階で各種のオイルトラップを設けて除
去することが行われている。更に微生物相の体力強化と
しては、曝気槽に微生物の栄養剤として適量の窒素分や
リン分等を毎日添加する等の策が採られている。
Further, with respect to the mixture of oil and fat, various oil traps are provided and removed before the introduction into the aeration tank. Further, for strengthening the physical strength of the microflora, measures such as daily addition of appropriate amounts of nitrogen and phosphorus as nutrients for microorganisms to the aeration tank have been adopted.

【0009】一方、バルキング状態となってしまった場
合の対応策としては、前述のように、流入する汚濁負荷
を軽減し、空気を充分に送って溶存酸素量を確保し、栄
養剤として適量の窒素分とリン分とを加えて時間を掛け
て好気性主体の微生物相の回復を待つか、あるいは曝気
槽を空にして、新たに種汚泥を入れて、時間を掛けて微
生物相を馴養させる等の策が採られている。
On the other hand, as a countermeasure against the occurrence of the bulking state, as described above, the inflowing pollution load is reduced, air is sufficiently sent to secure the amount of dissolved oxygen, and an appropriate amount as a nutrient is provided. Add nitrogen and phosphorus and wait for the recovery of the aerobic microflora, or empty the aeration tank and add new seed sludge to allow the microbiota to acclimate over time. Etc. are adopted.

【0010】しかし一旦バルキング状態となってしまっ
た場合には、曝気槽の微生物相の再生は基より、発生し
てくる原廃水を応急的に如何に処理して排出基準値以下
にして放流するか、あるいは工場の生産を停止して廃水
を出さないようにするか、企業としては早急な対応を迫
られることとなり、非常に大きな問題となってくる。
However, once the bulking state is reached, the microbial flora in the aeration tank is regenerated, and the generated raw wastewater is expeditedly treated and discharged below the emission standard value. Or, as a company, it is necessary to take immediate action to stop the production of the factory so as not to produce wastewater, which is a very big problem.

【0011】[0011]

【発明が解決しようとする課題】本発明は、以上の従来
例の不都合を解消し、好気性活性汚泥処理に於ける曝気
槽の微生物相の状態が変化して、BOD及びCOD成分
の除去率の低下が連続して発生した場合に、曝気槽の微
生物相を速やかに健全なものに再生できるようにし得、
かつ急激な汚濁負荷が掛かってもバランスを崩すことの
ない強力な微生物相となるようにし得る、手間の掛から
ない安価な活性汚泥処理に於ける微生物相の再生及び体
力増強方法を提供することを解決の課題とする。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned disadvantages of the conventional examples and changes the state of the microbial flora of the aeration tank in the treatment of aerobic activated sludge, thereby removing the BOD and COD components. When a decrease in the number of times occurs continuously, it is possible to promptly regenerate the healthy microflora of the aeration tank,
And to provide a method for regenerating microbial flora and strengthening physical strength in an inexpensive and activated sludge treatment, which can be a strong microbial flora that does not lose its balance even when subjected to a rapid pollution load. This is a problem to be solved.

【0012】[0012]

【課題を解決するための手段】本発明の1は、BOD及
びCOD成分の除去率の低下を起こしてきた活性汚泥処
理装置の曝気槽に、好気性菌を主体としこれに通性嫌気
性菌及び若干の嫌気性菌を共存させた生物共生菌を投入
して攪拌曝気し、上記曝気槽の微生物相の再生と微生物
相の体力の増強とを図る活性汚泥処理の微生物相の再生
及び体力増強方法である。
[Means for Solving the Problems] 1 of the present invention is mainly composed of aerobic bacteria in an aeration tank of an activated sludge treatment device which has caused a decrease in the removal rate of BOD and COD components. Also, a biosymbiotic bacterium coexisting with a small amount of anaerobic bacterium is added and stirred and aerated to regenerate the microbial flora in the aeration tank and enhance the stamina of the microbial flora. Is the way.

【0013】従って本発明の1の活性汚泥処理の微生物
相の再生及び体力増強方法によれば、前記のように、B
OD及びCOD成分の除去率の低下を起こした状況に於
いても、原廃水の導入量を減少させたり停止させること
なく、通常の運転を継続しながら原廃水を処理すること
ができると共に、曝気槽の微生物相を、短期間に手間を
掛けずに安価にかつ安全に健全な状態に再生し、活性汚
泥処理を正常に復帰させることができる。
Therefore, according to the method for regenerating the microbial flora and enhancing the physical strength of the activated sludge process according to the first aspect of the present invention, as described above, B
Even in a situation where the removal rate of OD and COD components is reduced, the raw wastewater can be treated while continuing the normal operation without reducing or stopping the introduction amount of the raw wastewater, and the aeration can be performed. The microbial flora in the tank can be regenerated to a healthy state inexpensively and safely without trouble in a short period of time, and the activated sludge treatment can be returned to normal.

【0014】曝気槽内が嫌気性状態、あるいは疑似嫌気
性状態となってしまい、導入された原廃水中の有機物が
膠質のようなもので包まれるような状況が発生している
ところでは、本発明者の観察によれば、好気性菌を投入
し、曝気処理を施しても膠質で包まれた有機物は殆ど上
記好気性菌による分解が行われることはなく、単に槽内
を処理廃水の移動に伴って移動するのみであり、ついに
は槽内の流れの乏しい下方の部位に沈殿堆積することに
なるものである。
In a situation where the inside of the aeration tank is in an anaerobic state or a pseudo-anaerobic state and the organic matter in the introduced raw wastewater is wrapped with something like a glue, According to the observation of the inventor, even if aerobic bacteria are introduced and subjected to aeration treatment, almost no organic matter wrapped with the collagen is decomposed by the aerobic bacteria, and the treated wastewater simply moves in the tank. It will only move with the flow of water, and will eventually settle and accumulate in the lower part of the tank where the flow is poor.

【0015】ところが、以上のような状況の槽内に、好
気性菌に通性嫌気性菌及び嫌気性菌を共生させた前記生
物共生菌を投入すると、前記の膠質に包まれた有機物の
分解が開始するに至り、良好な分解活動が継続し、BO
D及びCOD成分の除去率を所要レベルにまで回復し得
ることとなるものである。
However, when the aerobic bacterium and the biosymbiotic bacterium in which the aerobic bacterium and the anaerobic bacterium coexist are introduced into the tank in the above-mentioned situation, the organic matter encapsulated in the collagen is decomposed. Has started, good decomposition activities continued, and BO
The removal rate of the D and COD components can be restored to the required level.

【0016】これは、前記状況の槽内に前記生物共生菌
を投入すると、まず初めに、該生物共生菌中の嫌気性菌
及び通性嫌気性菌が作用して、前記有機物を包む膠質の
膜を破るとともに、内部の有機物の分解を開始させ、引
き続いて好気性菌が作用して有機物の分解を一層進め、
活性汚泥を正常に復帰させることになるからだと推定す
ることができる。
This is because, when the symbiotic bacterium is put into the tank in the above situation, first, the anaerobic bacterium and the facultative anaerobic bacterium in the symbiotic bacterium act to act as a gelatinous substance that wraps the organic matter. Along with breaking the membrane, the decomposition of organic substances inside is started, and aerobic bacteria subsequently act to further promote the decomposition of organic substances.
It can be presumed that this is because the activated sludge will be returned to normal.

【0017】本発明の2は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、好気性菌60〜80%、通性嫌気性菌20
〜10%、嫌気性菌20〜10%の組成割合の菌群を採
用したものである。
The second aspect of the present invention is the method for regenerating microbial flora and enhancing the physical strength of the activated sludge treatment of the first aspect of the present invention, wherein the aerobic bacterium is 60 to 80% and the facultative anaerobic bacterium is 20 as the biosymbiotic bacterium.
A bacterium group having a composition ratio of -10% and anaerobic bacterium 20 to 10% is adopted.

【0018】従って本発明の2の活性汚泥処理の微生物
相の再生及び体力増強方法によれば、前記のように、B
OD及びCOD成分の除去率の低下を起こしてきた活性
汚泥処理装置の曝気槽に投入する菌群中の好気性菌、通
性嫌気性菌及び嫌気性菌の菌群の割合が適切になるた
め、本発明の1に関して説明した有機物の分解のプロセ
スが良好に行われ得ることとなるものである。この割合
は、繰り返し行われた実験の結果得られたものであり、
上記割合外では、良い結果は得られない。例えば、好気
性菌が、上記最小割合より少なくても、最大割合より多
すぎても良い結果は得られない。嫌気性菌及び通性嫌気
性菌については両者をあわせた割合が、その最大割合よ
り多すぎても最小割合より少なすぎても良い結果は得ら
れない。
Therefore, according to the method 2 of the present invention for regenerating the microbial flora and enhancing the physical strength of the activated sludge treatment, as described above, B
Since the ratio of aerobic bacteria, facultative anaerobic bacteria and anaerobic bacteria groups in the bacterial groups to be put into the aeration tank of the activated sludge treatment device that has caused a reduction in the removal rate of OD and COD components becomes appropriate Therefore, the process of decomposing the organic matter described in regard to the first aspect of the present invention can be favorably performed. This percentage is the result of repeated experiments,
Outside the above range, good results cannot be obtained. For example, if the amount of aerobic bacteria is less than the above-mentioned minimum ratio or more than the maximum ratio, good results cannot be obtained. For anaerobic bacteria and facultative anaerobic bacteria, good results cannot be obtained if the combined ratio of both is larger than the maximum ratio or smaller than the minimum ratio.

【0019】本発明の3は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、導入される原廃水の温度が25〜35℃の
場合には、この温度域で活発に活動する中温菌を主とし
て採用し、導入される原廃水の温度が25℃以下の場合
には、この温度域で活発に活動する低温菌を主として採
用することとしたものである。
A third aspect of the present invention is the method for regenerating microbial flora for treatment of activated sludge and enhancing the physical strength according to the first aspect of the present invention, when the temperature of the raw waste water introduced as the biosymbiotic bacteria is 25 to 35 ° C. Decided to mainly adopt mesophilic bacteria that are active in this temperature range and, when the temperature of the raw wastewater to be introduced is 25 ° C or lower, mainly use low temperature bacteria that are active in this temperature range. It is a thing.

【0020】従って本発明の3の活性汚泥処理の微生物
相の再生及び体力増強方法によれば、前記好気性菌、通
性嫌気性菌及び嫌気性菌の各菌群に属する菌を、導入さ
れる原廃水の温度に対応させ、その温度域で活発に活動
するそれを採用することとしたので、より効率よく有機
物等の分解活動が行い得られ、スピーディに微生物相の
再生及び体力増強の結果を得ることができるものであ
る。
Therefore, according to the method 3 of the present invention for regenerating the microbial flora for the treatment of activated sludge and enhancing the physical strength thereof, the bacteria belonging to each of the aerobic bacteria, facultative anaerobic bacteria and anaerobic bacteria are introduced. The temperature of the raw wastewater that corresponds to the temperature of the raw wastewater is adjusted so that it can be activated actively in that temperature range, so that the decomposition activity of organic substances can be performed more efficiently, resulting in speedy regeneration of microbial flora and enhancement of physical strength. Is what you can get.

【0021】本発明の4は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、原廃水の基質の濃度に応じた菌濃度のそれ
を投入することとしたものである。
The fourth aspect of the present invention is, in the method for regenerating a microbial flora for treatment of activated sludge and for enhancing the physical strength of the first aspect of the present invention, as the symbiotic bacterium, a microbial concentration corresponding to the concentration of the substrate of the raw wastewater is added. I decided to do it.

【0022】従って本発明の4の活性汚泥処理の微生物
相の再生及び体力増強方法によれば、原廃水の基質濃度
に応じて菌濃度を調節し、例えば、基質濃度が高い場合
にも、キャリアの量を増加させないで、必要な量の生物
共生菌を投入することとしたので、処理対象の廃水中に
要分解物質を増加させないで済むものである。
Therefore, according to the method 4 for regenerating the microbial flora of the activated sludge treatment and enhancing the physical strength of the present invention, the bacterial concentration is adjusted according to the substrate concentration of the raw wastewater. Since it was decided to add the necessary amount of the symbiotic bacterium without increasing the amount of the above, it is not necessary to increase the substance requiring decomposition in the wastewater to be treated.

【0023】前記生物共生菌は、キャリアに吸着固定さ
せて用いるものであるが、基質の濃度が高い場合、例え
ば、蛋白質、炭水化物、脂肪、窒素分、燐分等の濃度が
高い場合には、投入する生物共生菌の割合も増加させる
必要が生じる。しかし、単に、その投入量を増加したの
では、キャリアの投入量も同時に増加する問題が生じ
る。即ち、キャリアもまた要分解対象となるものであ
り、これが必要以上に増加するのは、云うまでもなく、
好ましくない。従って生物共生菌の力価、即ち、その濃
度を、基質の濃度に対応するものとしてキャリアに吸着
固定させて用いるようにしたものであり、こうすること
により、無用な要分解物を増加させずに効率よく活性汚
泥処理ができるものとなる。
The above-mentioned symbiotic bacterium is used by being adsorbed and immobilized on a carrier, but when the concentration of the substrate is high, for example, when the concentration of protein, carbohydrate, fat, nitrogen content, phosphorus content, etc. is high, It will also be necessary to increase the proportion of symbiotic bacteria to be input. However, simply increasing the input amount causes a problem that the input amount of carriers also increases at the same time. That is, the carrier also needs to be disassembled, and needless to say, this will increase more than necessary.
Not preferable. Therefore, the titer of the symbiotic bacterium, that is, the concentration of the symbiotic bacterium, is used by adsorbing and fixing it on the carrier as a substance corresponding to the concentration of the substrate, and by doing so, unnecessary unnecessary decomposition products are not increased. The activated sludge can be treated very efficiently.

【0024】本発明の5は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、好気性菌を主体とする酵母菌、子嚢菌及び
セルロース分解菌と、通性嫌気性菌を主体とする蛋白質
分解菌、乳酸菌及び枯草菌と、嫌気性菌を主体とする光
合成菌、窒素固定菌、酢酸菌及び酪酸菌とを含む菌群
を、キャリアに吸着固定させて共生させ、適用対象の原
廃水の基質濃度に対応する菌濃度に培養した複合微生物
菌を採用したものである。
The fifth aspect of the present invention is the method for regenerating the microbial flora of the activated sludge treatment and enhancing the physical strength of the first aspect of the present invention, wherein, as the above-mentioned symbiotic bacteria, yeasts mainly composed of aerobic bacteria, ascomycetes and cellulose decomposition. Bacteria, proteolytic bacteria mainly composed of facultative anaerobic bacteria, lactic acid bacteria and Bacillus subtilis, and photosynthetic bacteria mainly composed of anaerobic bacteria, nitrogen-fixing bacteria, acetic acid bacteria and butyric acid bacteria as carriers, This is a method that employs a complex microbial bacterium that is adsorbed and fixed to coexist, and cultivated at a bacterium concentration corresponding to the substrate concentration of the raw wastewater to which it is applied.

【0025】本発明の5の活性汚泥処理の微生物相の再
生及び体力増強方法によれば、生物共生菌を構成するの
に必要な好気性菌、通性嫌気性菌及び嫌気性菌の菌群に
ついて以上の各種の菌群を選択したため、前記のよう
に、BOD及びCOD成分の除去率の低下を起こした状
況の曝気槽中に、これらを投入することにより、前記し
た嫌気性菌及び通性嫌気性菌の作用及び好気性菌の作
用、即ち、前者の膠質に包まれた有機物の分解及びその
後の有機物の酸化分解の作用を効率良く行うことがで
き、その結果、BOD及びCOD成分の除去率を所要レ
ベルにまでスピーディに回復し得ることとなるものであ
る。
According to the method 5 for regenerating the microbial flora of the activated sludge treatment and enhancing the physical strength of the present invention, a group of aerobic bacteria, facultative anaerobic bacteria and anaerobic bacteria necessary for constituting a symbiotic bacterium. Since the above-mentioned various bacterial groups were selected, as described above, by introducing them into the aeration tank in the situation where the removal rate of BOD and COD components was lowered, the anaerobic bacteria and facultative bacteria The effects of anaerobic bacteria and aerobic bacteria, that is, the decomposition of organic substances encapsulated in the collagen and the subsequent oxidative decomposition of organic substances can be efficiently performed, and as a result, the removal of BOD and COD components The rate can be quickly recovered to the required level.

【0026】また以上の菌群によって構成される生物共
生菌を採用した場合は、有機物の分解に於いて、悪臭ガ
スの発生がなく、二酸化炭素と水とに効率的に分解され
るので、汚泥の発生が極めて少ないものとなって、汚泥
処理の負荷を軽減させるものとなる。
When a symbiotic bacterium composed of the above-mentioned bacterial group is adopted, no odorous gas is generated in the decomposition of organic matter and the organic matter is efficiently decomposed into carbon dioxide and water. The generation of sewage is extremely small, and the load of sludge treatment is reduced.

【0027】更にまた以上の菌群によって構成される生
物共生菌は、安全性が確保できるものであり、曝気槽に
投入され、活動を開始すると、該曝気槽の中で新たな生
物共生菌を生体合成するので、該曝気槽の微生物相は原
廃水の変動に対して耐性のある良好な状態となる。
Furthermore, the biosymbiotic bacteria composed of the above-mentioned bacterial groups can ensure safety, and when they are put into the aeration tank and the activity is started, new biosymbiotic bacteria are formed in the aeration tank. Since biosynthesis is carried out, the microflora of the aeration tank is in a good state of being resistant to fluctuations in the raw wastewater.

【0028】[0028]

【発明の実施の形態】以下、発明の実施の形態を詳細に
説明する。本発明の活性汚泥処理の微生物相の再生及び
体力増強方法は、既存の好気性の活性汚泥処理に於いて
その曝気槽に適用することができるものである。
BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described in detail below. INDUSTRIAL APPLICABILITY The method for regenerating microbial flora and enhancing the physical strength of the activated sludge process of the present invention can be applied to the aeration tank in the existing aerobic activated sludge process.

【0029】ここで対象とする活性汚泥処理は、一般に
知られているものであって、特に説明を要するものとは
思われないが、都合上、要点のみを説明すると、通常、
処理装置としては、原廃水を導入する原水槽、原廃水を
曝気する曝気槽、曝気によって発生した汚泥を沈降分離
する沈殿槽、沈殿槽の上澄みを貯留する放流槽及び沈殿
槽で沈降させた汚泥を貯留する汚泥槽、更に汚泥を処理
する付帯装置として汚泥の水分を脱水する汚泥脱水機及
び脱水汚泥を焼却する焼却炉等からなる一連の設備であ
る。
The target activated sludge treatment here is generally known and does not seem to require any particular explanation. However, for the sake of convenience, only the essential points will be described below.
The treatment equipment includes a raw water tank for introducing raw wastewater, an aeration tank for aerating the raw wastewater, a settling tank for settling and separating sludge generated by aeration, a discharge tank for storing the supernatant of the settling tank, and sludge settling in the settling tank. It is a series of equipment including a sludge tank that stores sludge, a sludge dehydrator that dehydrates the water content of the sludge as an auxiliary device that processes the sludge, and an incinerator that incinerates the dehydrated sludge.

【0030】前記曝気槽は、そのピットの容量としては
原廃水の発生量と曝気槽に於ける必要曝気処理時間とに
よって決められるもので、通常は原廃水が槽内で4〜6
時間程度滞留して処理されるように設計されている。
The capacity of the pit of the aeration tank is determined by the amount of raw wastewater generated and the required aeration processing time in the aeration tank. Normally, the raw wastewater is 4 to 6 in the tank.
It is designed to be processed for a long period of time.

【0031】また前記曝気槽内には、原廃水を攪拌する
攪拌装置及び槽内の原廃水に溶存酸素を供給する散気管
等の空気を送り込む装置、更に運転管理に必要な水量
計、溶存酸素計、pH計及び温度計等が付設されている。
Further, in the aeration tank, a stirring device for stirring the raw wastewater, a device for feeding air such as a diffuser pipe for supplying dissolved oxygen to the raw wastewater in the tank, a water meter necessary for operation management, and dissolved oxygen. A meter, pH meter and thermometer are attached.

【0032】活性汚泥処理による廃水中の汚濁物質の浄
化は、主として廃水中の有機物質、即ち、BOD成分を
微生物によって食させて処理するものであって、対象が
微生物であるために、その生息環境を調えることが大切
で、特に温度、pH、溶存酸素量、栄養源の窒素分や燐分
及び各種汚濁負荷量を一定範囲の下で運転することが必
要となっている。
Purification of pollutants in wastewater by treatment with activated sludge is mainly to treat organic substances in wastewater, that is, BOD components, by treating them with microorganisms. It is important to adjust the environment, and it is especially necessary to operate within a certain range of temperature, pH, dissolved oxygen content, nitrogen and phosphorus content of nutrient sources, and various pollution loads.

【0033】しかし工場等の廃水発生源から排出されて
くる原廃水は、常に一定の水質で排出されてくることは
稀で、時として、例えば、製造工程でのトラブルの発生
時や定期的な補修の時等には、各種汚濁物質の増加とな
って、急激なpHの変動や、急激なBOD及びCOD成分
の増加や、急激な油脂分の増加等となって、一定範囲の
管理下での運転から大幅に外れてしまうことがある。
However, raw wastewater discharged from a wastewater generation source such as a factory is rarely always discharged with a constant water quality, and occasionally, for example, when trouble occurs in the manufacturing process or at regular intervals. At the time of repair, etc., the amount of various pollutants will increase, the pH will change rapidly, the BOD and COD components will increase rapidly, and the oil content will increase rapidly. It may deviate significantly from driving.

【0034】このような状態の時には、センサにより異
常を検出して、前記原廃水を一時バイパスして別のピッ
トへ導入させる等の対策が必要となるが、廃水量の多い
工場や、バイパスさせて一時貯留するピットを持たない
ところでは、仕方なく処理を継続させてしまうために、
曝気槽の微生物相に大きなダメージを与えてしまうこと
になって、その結果としてBOD及びCOD成分の除去
率の低下が続くようになる。
In such a state, it is necessary to take a measure such as detecting an abnormality with a sensor and temporarily bypassing the raw wastewater and introducing it into another pit. In a place where there is no pit for temporary storage, in order to continue processing without help,
The microflora in the aeration tank will be greatly damaged, and as a result, the removal rate of BOD and COD components will continue to decrease.

【0035】またこのような状態になった時には、前述
のように、早めに曝気槽に導入する原廃水の流入量を減
少させて汚濁物質の負荷量を軽減させ、充分な溶存酸素
量の下で、窒素分や燐分等の栄養剤を与えて養生させて
やること等の処置が必要となる。
When such a state occurs, as described above, the inflow amount of the raw waste water introduced into the aeration tank is reduced early to reduce the load amount of the pollutants, and the amount of dissolved oxygen is reduced. Therefore, it is necessary to provide a nutrient such as nitrogen or phosphorus to cure the nutrient.

【0036】しかし、このような状況の下で使用するた
めのバイパス設備をもたない工場では、工場の稼働を部
分的に停止することもままならず、曝気槽の微生物相に
は、益々過酷な処理が強いられることとなって曝気槽の
状態の悪化が続き、曝気槽には糸状菌が多く見られるよ
うになり、次第に嫌気性となって曝気槽の色相も変化し
て前述のようにバルキング状態になってしまうのであ
る。
However, in a factory that does not have a bypass facility for use under such a situation, the operation of the factory cannot be partially stopped, and the microflora in the aeration tank is treated more and more severely. As a result, the condition of the aeration tank continues to deteriorate, and many filamentous fungi are found in the aeration tank, gradually becoming anaerobic and the hue of the aeration tank also changes, resulting in the bulking state. It becomes.

【0037】本発明では、前記曝気槽にこのような悪化
傾向の現象が現れ始めた場合に、曝気槽に対して、好気
性菌を主体としこれに通性嫌気性菌及び若干の嫌気性菌
を共存させた生物共生菌を投入して攪拌曝気し、こうし
て曝気槽中の微生物相の再生又は回復と微生物相の体力
増強とを付与させるものである。
In the present invention, when such a phenomenon of a deterioration tendency begins to appear in the aeration tank, aerobic bacteria are mainly contained in the aeration tank, and facultative anaerobic bacteria and some anaerobic bacteria are added. The coexisting symbiotic bacteria are added and aerated with stirring, thereby imparting regeneration or recovery of the microflora in the aeration tank and enhancement of the physical strength of the microflora.

【0038】ここで前記生物共生菌について説明する。
前記生物共生菌は、自然界に存在する無数の微生物群の
中から、浄化に有効な好気性、通性嫌気性及び嫌気性の
菌群を厳選したものであって、対象となる原廃水の温度
に応じて、例えば、原廃水の温度が25〜35℃の範囲
であれば中温菌の中から、温度が25℃以下であれば低
温菌の中から選択して用いるものである。
Here, the symbiotic bacterium will be described.
The symbiotic bacterium is an aerobic, effective facultative anaerobic and anaerobic bacterial group that is carefully selected from a myriad of microbial groups existing in nature, and is the temperature of the target wastewater. According to the above, for example, if the temperature of the raw waste water is in the range of 25 to 35 ° C., it is selected from mesophilic bacteria, and if the temperature is 25 ° C. or less, it is selected from low temperature bacteria and used.

【0039】またこれらの菌群は、主として好気性菌群
を含む酵母菌、子嚢菌及びセルロース分解菌と、主とし
て通性嫌気性菌群を含む蛋白質分解菌、乳酸菌及び枯草
菌等と、主として嫌気性菌群を含む光合成菌、窒素固定
菌、酢酸菌及び酪酸菌とを共生させた複合微生物菌群で
ある。
These bacterial groups are mainly anaerobic, mainly yeasts containing aerobic bacteria, ascomycetes and cellulolytic bacteria, proteolytic bacteria mainly containing facultative anaerobic bacteria, lactic acid bacteria and Bacillus subtilis. It is a group of complex microorganisms that coexist with photosynthetic bacteria including nitrogenous bacteria, nitrogen-fixing bacteria, acetic acid bacteria and butyric acid bacteria.

【0040】更にまたこれらの菌群は、好気性菌群が6
0〜80%程度、通性嫌気性菌群が20〜10%程度、
嫌気性菌群が20〜10%程度に含まれるものが有効で
ある。
Further, among these bacterial groups, aerobic bacterial groups are 6
0-80%, facultative anaerobic bacteria group 20-10%,
Those in which the anaerobic bacteria group is contained in about 20 to 10% are effective.

【0041】これらの複合微生物菌群は、共生培養し、
その際のキャリアとして、例えば、玄米の粉、米糠、ふ
すま、繊維素類及びゼオライトの単独又は複数種を組み
合わせたものと、プロティン、コーン粉末、窒素無機
物、ビタミン類及びミネラル類の単独又は複数種を組み
合わせたものとを混合してなるものに吸着固定させるも
のであり、またこれらの菌群は、これらのキャリアに植
え付けて共生培養しつつ、徐々に水分割合を低下させ、
休眠状態で坦持する。これらの休眠中の菌は、曝気槽の
原廃水中に投入されると、すぐに活動を再開することと
なる。
These complex microbial groups are co-cultivated,
As a carrier in that case, for example, brown rice powder, rice bran, bran, a combination of single or plural kinds of zeolite and fiber, protein, corn powder, nitrogen inorganic matter, single or plural kinds of vitamins and minerals It is intended to be adsorbed and fixed to a mixture of a mixture of these, and these bacterial groups are gradually planted in these carriers and co-cultivated while gradually reducing the water content,
Carry in a dormant state. When these dormant bacteria are put into the raw wastewater of the aeration tank, they will immediately resume their activities.

【0042】上記キャリアに吸着させる菌群の濃度(力
価)は、適用対象となる原廃水の基質濃度に応じて決定
することとし、これは主としてキャリアに菌を植え付け
る際の菌原液(種菌から醸造して得たもの)の濃度を調
節することによって行う。例えば、本発明者の醸造した
菌原液を用いた場合で、通常の場合は、キャリア10Kg
に対して菌原液700ccの割合で菌を植え付けている。
これに対して菌群の濃度(力価)を高める必要のある場
合は、その必要に応じて菌原液の割合を高めることとす
る。植え付ける際の菌原液の濃度を高くすれば、培養が
完了し、水分割合を低下させて休眠状態にした時の菌濃
度は必ずしも比例して高くなるとまでは云えないが、概
ねそれに応じて高くなる。
The concentration (titer) of the bacterial group to be adsorbed on the carrier is determined according to the substrate concentration of the raw wastewater to be applied, which is mainly the bacterial stock solution (from inoculum) when planting the bacteria on the carrier. (Obtained by brewing). For example, in the case of using the bacterium stock solution brewed by the present inventor, in the usual case, 10 kg of carrier
On the other hand, the bacteria are planted at a ratio of 700 cc of the stock solution.
On the other hand, when it is necessary to increase the concentration (titer) of the bacterial group, the proportion of the stock solution is increased as necessary. It cannot be said that the bacterial concentration at the time of planting is high when the concentration of the undiluted solution is high when the culture is completed and the water content is lowered to the dormant state, but it generally increases accordingly. .

【0043】なお原廃水に投入する菌群の濃度の基準は
実験的に定めることができる。例えば、一定の条件で醸
造した菌原液を一定のキャリアに植え付けて一定の条件
で培養固定した菌群を一定の基質条件(濃度)の原廃水
に一定量投入して実験を繰り返すことにより、そのよう
な菌群の有効性の程度が明らかとなり、これを菌濃度の
基準値とすることができる。こうして一定の基質濃度の
原廃水に有効に作用する菌の濃度の基準が定まれば、原
廃水の基質濃度を、基準とした上記一定の基質濃度と比
較し、それを上回る場合には、それに応じて菌濃度を高
めれば良いこととなる。菌濃度は、既述のように、キャ
リアに植え付ける菌原液の割合を高めることによって、
高めることができる。
The standard of the concentration of the bacterial group to be added to the raw wastewater can be determined experimentally. For example, by inoculating a bacterium stock solution brewed under a certain condition in a certain carrier, culturing and fixing the bacterium group under a certain condition into a certain amount of raw wastewater having a certain substrate condition (concentration), and repeating the experiment, The degree of effectiveness of such a bacterial group becomes clear, and this can be used as a reference value for bacterial concentration. In this way, if the standard of the concentration of bacteria that effectively acts on the raw wastewater with a constant substrate concentration is determined, the substrate concentration of the raw wastewater is compared with the above-mentioned constant substrate concentration as the standard, and if it exceeds it, Therefore, the bacterial concentration should be increased accordingly. As described above, the bacterium concentration can be increased by increasing the ratio of the bacterium stock solution to be planted on the carrier.
Can be increased.

【0044】また、この複合微生物菌群は、自然界に存
在する浄化に有効に働く菌であって、いずれにしても安
全な菌群を選択するものである。
Further, this complex microbial group is a bacterium that exists in nature and works effectively for purification, and in any case, a safe microbial group is selected.

【0045】以上の生物共生菌による浄化のメカニズム
は、自然界で行われている微生物群の働きによる有効な
浄化作用を見いだし、これを人工的に効果的に行わしめ
るものである。本発明者の知見によれば、各種有機物
は、好気性菌による酸化活動と嫌気性菌による還元活動
の繰り返しによって分解されるものであり、本発明に於
いては、前記生物共生菌中に含まれる好気性、通性嫌気
性及び嫌気性の菌群によって、それぞれ役割分担されて
酸化・還元の作用が行われ、対象の原廃水中の各種有機
物の分解が行われるものである。更に前記生物共生菌
は、このような活動に伴って新たな生体合成が行われ、
増殖が繰り返され、安定した浄化作用が継続することと
なるものである。
The above-mentioned mechanism of purification by the symbiotic bacterium is to find an effective purification action by the action of the microorganism group which is carried out in the natural world, and to carry out this effectively artificially. According to the knowledge of the present inventor, various organic substances are decomposed by repeated oxidation activity by aerobic bacteria and reduction activity by anaerobic bacteria, and in the present invention, they are included in the above-mentioned symbiotic bacteria. The aerobic, facultative and anaerobic, and anaerobic bacterial groups are responsible for their respective functions of oxidation and reduction, and decompose various organic substances in the target raw wastewater. Furthermore, the biosymbiotic bacterium undergoes new biosynthesis along with such activity,
Proliferation is repeated and a stable purifying action continues.

【0046】なおこのような生物共生菌による効果的な
活動が行われるためには、環境設定因子として、温度、
pH、溶存酸素量、栄養塩バランス、微量元素及び酵素等
が適したものであることが必要である。
In order to carry out such an effective activity by the symbiotic bacterium, temperature,
It is necessary that pH, dissolved oxygen content, nutrient balance, trace elements, enzymes, etc. be suitable.

【0047】しかして本発明に於いては、既述のよう
に、対象となる原廃水の温度によって用いる菌を選択す
る。原廃水が10℃を下回る低温の場合には、低温菌の
中でも低温を好む好冷菌を採用することができる。
Therefore, in the present invention, as described above, the bacterium to be used is selected depending on the temperature of the target raw wastewater. When the raw wastewater has a low temperature of less than 10 ° C., a psychrophilic bacterium that prefers a low temperature can be adopted among the psychrophilic bacteria.

【0048】原廃水のpHは5.5〜8.5程度が、溶存
酸素量は1〜1.5ppm 程度がそれぞれ好適な条件であ
り、適合していない場合は調節する。
It is preferable that the pH of the raw wastewater is about 5.5 to 8.5 and the dissolved oxygen amount is about 1 to 1.5 ppm.

【0049】一方、栄養塩バランスとしては適量の窒素
及び燐の塩類が好気性の下における酸化分解に必要であ
る。また、微量元素としてはカリウム、ナトリウム、カ
ルシウム及びマグネシウム等の元素が、微生物の生育と
代謝において外部の環境変化に対し生体内浸透圧を一定
に保つ浸透圧調整作用や酵素を活性化する触媒作用に必
要である。
On the other hand, as a nutrient salt balance, appropriate amounts of nitrogen and phosphorus salts are required for oxidative decomposition under aerobic conditions. Also, as trace elements, elements such as potassium, sodium, calcium and magnesium are osmotic pressure adjusting action that keeps the in vivo osmotic pressure constant against external environmental changes in the growth and metabolism of microorganisms and catalytic action that activates enzymes. Needed for.

【0050】更に、重炭酸塩や燐酸塩等も生体内のpHを
一定に保つ緩衝作用を付与することから必要となる。更
にまた酵素も各種菌の好気性の下における酸化分解に重
要な役割を担っている。
Further, bicarbonates, phosphates and the like are also necessary because they impart a buffering effect for keeping the pH in the body constant. Furthermore, enzymes also play an important role in oxidative degradation of various bacteria under aerobic conditions.

【0051】このような生物共生菌による有機物の分解
作用は、その過程において悪臭ガスの発生がなく、有機
物は水と二酸化炭素に効果的に分解されるので、汚泥の
発生が極めて少ないことが特徴となっている。
The function of decomposing organic matter by such a symbiotic bacterium does not generate a foul-smelling gas in the process and the organic matter is effectively decomposed into water and carbon dioxide, so that the generation of sludge is extremely small. Has become.

【0052】このような生物共生菌の曝気槽への添加量
は、前記のようにして本発明者が培養したそれの場合
で、BOD汚濁負荷量(kg/日)に対してキャリア共々
3〜4%程度に毎日添加するのが適当である。またBO
D汚濁負荷が高い(基質濃度が高い)場合には、既述の
ように、菌の力価(濃度)を高めて添加することが、キ
ャリアの量の影響を受けることが軽減されるので好まし
い。更に曝気槽の状態の回復が確認されても、しばら
く、例えば、1週間程度は継続して添加することが微生
物相に体力を付けてやる上からも必要である。
The amount of such a symbiotic bacterium to be added to the aeration tank is 3 to 3 for both carriers with respect to the BOD pollution load amount (kg / day) in the case of culturing by the present inventor as described above. It is suitable to add about 4% daily. Also BO
D When the pollution load is high (the substrate concentration is high), it is preferable to increase the titer (concentration) of the bacterium to be added, as described above, because the influence of the carrier amount is reduced. . Further, even if the recovery of the state of the aeration tank is confirmed, it is necessary to continuously add it for a while, for example, for about a week, in order to strengthen the microbiota.

【0053】次に、BOD及びCOD成分の除去率の低
下が連続して発生し、曝気槽の微生物相に異常が見られ
るようになった時の生物共生菌による処理方法について
説明する。
Next, a method of treatment with a symbiotic bacterium when a decrease in the removal rate of BOD and COD components occurs continuously and an abnormality is observed in the microflora of the aeration tank will be described.

【0054】通常、活性汚泥処理に於いては、日常のパ
トロールによって、曝気槽の色や臭いや泡等を観察した
り、曝気槽で処理中の曝気溶液を1リットルのメスシリ
ンダに採取し、30分間静置して活性汚泥の沈降性(S
V)を計る等を行って、曝気槽の状態の良好な時の様子
を把握しておくことが重要である。
Usually, in the activated sludge treatment, the color, smell and bubbles of the aeration tank are observed by daily patrol, and the aeration solution being treated in the aeration tank is collected in a 1-liter graduated cylinder. Let stand for 30 minutes and settle the activated sludge (S
It is important to measure V) to understand the condition of the aeration tank when it is in good condition.

【0055】こうして現状との対比により状態の変化を
視覚や嗅覚で感じ取ることと、活性汚泥処理前後の廃水
のpH、BOD、COD、SSの値及びBOD、COD、
SSの除去率の値とから変化をいち早く読み取ることで
ある。
In this way, the change in the state is visually or olfactually compared with the current situation, and the pH, BOD, COD, SS values and BOD, COD of the wastewater before and after the activated sludge treatment,
It is to read the change quickly from the value of the removal rate of SS.

【0056】一般にBOD、COD及びSSの測定は、
1週間に2回程度の測定としているところが多いが、曝
気槽の状態変化をいち早く見つけるには、毎日測定して
おくことが好ましい。通常、良好な時の状態との変化が
3日間続いた場合には、要注意状態で、4〜5日以上続
くようになったら早急に手当てが必要と見るべきであ
る。この状態で更に放置しておくと曝気槽の微生物相の
回復には長期間を要することとなり、酷い時には、種汚
泥から微生物相の作り直しとなってしまうこともある。
Generally, BOD, COD and SS are measured by
In many cases, the measurement is made about twice a week, but it is preferable to make the measurement every day in order to quickly find the change in the condition of the aeration tank. Usually, when the change from a good condition lasts for 3 days, it should be considered as urgently necessary to be treated if it continues to be for 4 to 5 days or more with caution. If left in this state, it will take a long time to recover the microbial flora in the aeration tank, and in severe cases, the microbial flora may be regenerated from the seed sludge.

【0057】このような状態になった場合には、早急に
曝気槽のpHを6.0〜8.0に、溶存酸素量を1〜1.
5ppm に、それぞれコントロールして、原廃水を導入し
ながら攪拌を続け、前記生物共生菌を、曝気槽に、原廃
水のBOD汚濁負荷量(kg/日)に対して一定割合、例
えば、既述のように、本発明者の培養したそれの場合
で、キャリア共々3〜4%程度になるように添加する。
前記生物共生菌の添加は毎日行い、状態が回復しても1
週間〜10日間程度は継続して添加することが、曝気槽
の微生物相に体力を付けることからも好ましい。
In such a case, the pH of the aeration tank is promptly adjusted to 6.0 to 8.0, and the dissolved oxygen content is adjusted to 1 to 1.
5ppm each, while continuing to stir while introducing the raw wastewater, the biosymbiotic bacteria in the aeration tank, a certain ratio to the BOD pollution load of the raw wastewater (kg / day), for example, as described above. As described above, in the case of culturing by the present inventor, the carrier is added so as to be about 3 to 4%.
The above-mentioned symbiotic bacteria are added every day, and even if the condition is restored, 1
It is preferable to continuously add it for about a week to 10 days in order to strengthen the microflora in the aeration tank.

【0058】曝気槽の微生物相は、前記生物共生菌が加
わって少しずつ状態が回復する方向に向かい、処理水の
BOD、COD、SSの値及び廃水のBOD、COD、
SSの除去率が向上してくる。また前記生物共生菌を添
加することによって曝気槽の微生物相には新たな生物共
生菌が生体合成によって生じてくるので、微生物相は次
第に耐性のある良好な状態となって行くものである。
The microbial flora in the aeration tank is gradually recovered by the addition of the above-mentioned symbiotic bacteria, and the BOD, COD, SS values of the treated water and the BOD, COD of the waste water,
The removal rate of SS improves. Further, by adding the above-mentioned symbiotic bacterium, a new symbiotic bacterium is generated in the microbial flora of the aeration tank by biosynthesis, so that the microbial flora gradually becomes resistant and is in a good state.

【0059】[0059]

【実施例】次に実施例1及び実施例2によって本発明を
具体的に説明するが、これは本発明の効果を説明するた
めのものであって、これによって本発明が限定されるも
のではない。
EXAMPLES Next, the present invention will be described in detail with reference to Examples 1 and 2, but this is for explaining the effects of the present invention, and the present invention is not limited thereby. Absent.

【0060】<実施例1>食品加工工場の凝集沈殿処理
後の原廃水(排水量140m3/日)の水質が、廃水温度
28℃、pH5.5、BOD850ppm 、COD380pp
m 、SS360ppm 、N−ヘキサン抽出物75ppm に対
して、通常の好気性の活性汚泥処理法によって処理を行
っていた。
<Example 1> The water quality of the raw wastewater (effluent volume 140 m 3 / day) after coagulation and sedimentation treatment in a food processing plant was such that the wastewater temperature was 28 ° C., pH 5.5, BOD 850 ppm, and COD 380 pp.
m, SS 360 ppm, and N-hexane extract 75 ppm were treated by the usual aerobic activated sludge treatment method.

【0061】しかし活性汚泥処理後の水質がBOD90
〜120ppm 、COD70〜140ppm 、SS70〜1
40ppm と処理状態が劣ってきた状態が5日間続いたの
で、異常と察知して、曝気槽に下記組成の生物共生菌
(菌濃度はほぼ基準濃度)をキャリア共々4.2kg投入
(BOD汚濁負荷量に対して3.5%添加)し、pHを
6.0〜8.0、溶存酸素量を1〜1.5ppm にそれぞ
れ管理し、原廃水を導入して攪拌曝気しながら活性汚泥
処理を継続した。前記生物共生菌の投入は、毎日キャリ
ア共々4.2kgを10日間続けて投入し、曝気槽の状態
の観察と処理後の水質試験を行った。
However, the water quality after the activated sludge treatment is BOD 90.
~ 120ppm, COD70 ~ 140ppm, SS70 ~ 1
Since the treatment condition was 40 ppm, which was inferior for 5 days, it was detected as abnormal, and 4.2 kg of bio-symbiotic bacteria of the following composition (bacterial concentration was almost the standard concentration) was added to the aeration tank together with the carrier (BOD pollution load). (3.5% of the amount added), pH was controlled at 6.0-8.0, dissolved oxygen amount was controlled at 1-1.5 ppm, and raw sludge was introduced and activated sludge treatment was performed while stirring and aeration. Continued. Regarding the introduction of the symbiotic bacterium, 4.2 kg of each carrier was continuously introduced every day for 10 days, and the state of the aeration tank was observed and the water quality test after the treatment was conducted.

【0062】[実施例1の生物共生菌の組成]好気性菌
として酵母菌、子嚢菌及びセルロース分解菌の中から、
通性嫌気性菌として蛋白質分解菌、乳酸菌及び枯草菌の
中から、嫌気性菌として光合成菌、窒素固定菌及び酢酸
菌の中から、それぞれ菌群を選定し、好気性菌群を65
%、通性嫌気性菌群を20%、嫌気性菌群を15%の割
合で配合した。いずれも中温菌に属する菌群を選んだ。
これらの菌群を共生させて培養し、キャリアとして玄米
の粉及びふすま並びにプロティン、コーン粉末、ビタミ
ン類及びミネラル類を混合したものに吸着固定させた。
上記生物共生菌については、実施例1の処理に先立っ
て、魚類のヒメダカによる急性毒性試験及びマウスによ
る経口急性毒性試験によって安全であることを確認し
た。
[Composition of the symbiotic bacterium of Example 1] As aerobic bacteria, yeast, ascomycetes, and cellulolytic bacteria
As a facultative anaerobic bacterium, a proteolytic bacterium, a lactic acid bacterium, and a Bacillus subtilis are selected, and as an anaerobic bacterium, a photosynthetic bacterium, a nitrogen-fixing bacterium, and an acetic acid bacterium are selected.
%, The facultative anaerobic group was 20%, and the anaerobic group was 15%. In each case, a group of bacteria belonging to the mesophilic bacterium was selected.
These bacterial groups were symbioticly cultivated and adsorbed and fixed on a mixture of brown rice flour and bran, protein, corn powder, vitamins and minerals as a carrier.
Prior to the treatment of Example 1, it was confirmed that the above-mentioned symbiotic bacterium was safe by an acute toxicity test using a fish killifish and an oral acute toxicity test using a mouse.

【0063】<実施例2>羊毛処理工場の原廃水(排水
量1270m3/日)の水質が、廃水温度26℃、pH8.
4、BOD900ppm 、COD300ppm 、SS180
ppm 、N−ヘキサン抽出物90ppm に対して、通常の好
気性の活性汚泥処理法によって処理を行っていた。
<Example 2> The quality of the raw wastewater (wastewater amount 1270 m 3 / day) of the wool treatment plant was such that the wastewater temperature was 26 ° C and the pH was 8.
4, BOD900ppm, COD300ppm, SS180
The ppm and the N-hexane extract of 90 ppm were treated by the usual aerobic activated sludge treatment method.

【0064】しかし活性汚泥処理後の水質がBOD10
0〜140ppm 、COD70〜85ppm 、SS40〜6
0ppm と処理状態が劣ってきた状態が5日間続いたの
で、異常と察知して、曝気槽に下記組成の菌の力価(菌
濃度)を通常のほぼ3倍に高めた生物共生菌をキャリア
共々12kg投入(BOD汚濁負荷量に対して通常の力価
換算で3.2%添加)し、pHを6.0〜8.0、溶存酸
素量を1〜1.5ppm にそれぞれ管理し、原廃水を導入
して攪拌曝気しながら活性汚泥処理を継続した。また、
前記生物共生菌の投入は、毎日キャリア共々12kgを1
0日間続けて投入し、曝気槽の状態の観察と処理後の水
質試験を行った。
However, the water quality after the activated sludge treatment is BOD10.
0-140ppm, COD70-85ppm, SS40-6
Since the treatment condition was 0 ppm and continued to be inferior for 5 days, it was detected as an abnormality and the aeration tank was treated with a symbiotic bacterium with the titer (bacterial concentration) of the bacteria of the following composition increased to about 3 times the normal level. Add 12 kg each (add 3.2% in normal titer to BOD pollution load), control pH to 6.0-8.0 and dissolved oxygen content to 1-1.5 ppm respectively. The activated sludge treatment was continued while introducing waste water and stirring and aerating. Also,
The above-mentioned symbiotic fungus input is 12 kg for each carrier every day.
It was continuously charged for 0 days, and the state of the aeration tank was observed and the water quality test after the treatment was performed.

【0065】[実施例2の生物共生菌の組成]好気性菌
として酵母菌、子嚢菌及びセルロース分解菌の中から、
通性嫌気性菌として蛋白質分解菌、乳酸菌及び枯草菌の
中から、嫌気性菌として光合成菌、窒素固定菌及び酪酸
菌の中から、それぞれ菌群を選定し、好気性菌群を70
%、通性嫌気性菌群を15%、嫌気性菌群を15%の割
合で配合した。いずれも中温菌を選定した。これらの菌
群を共生させて、菌を植え付ける際の原液量(本発明者
が醸造したもの)で前記した基準値の3倍を添加して培
養し、キャリアとして玄米の粉及びふすま並びにプロテ
ィン、コーン粉末、ビタミン類及びミネラル類を混合し
たものに吸着固定させた。また、上記生物共生菌につい
ても、実施例2の処理に先立って、魚類のヒメダカによ
る急性毒性試験及びマウスによる経口急性毒性試験によ
って安全であることを確認した。
[Composition of the symbiotic bacterium of Example 2] Among aerobic bacteria, yeast, ascomycetes and cellulolytic bacteria,
As a facultative anaerobic bacterium, proteolytic bacteria, lactic acid bacteria and Bacillus subtilis are selected, and as anaerobic bacteria, photosynthetic bacteria, nitrogen-fixing bacteria and butyric acid bacteria are selected.
%, The facultative anaerobic group was 15%, and the anaerobic group was 15%. In all cases, mesophilic bacteria were selected. Coexisting with these bacterial groups, the amount of the stock solution when planting the bacteria (the one brewed by the present inventor) was added and cultivated at 3 times the reference value described above, and the mixture was cultured as brown rice flour and bran and protein, It was adsorbed and fixed to a mixture of corn powder, vitamins and minerals. In addition, it was confirmed that the above-mentioned symbiotic bacterium was also safe prior to the treatment in Example 2 by an acute toxicity test using a fish killifish and an oral acute toxicity test using a mouse.

【0066】実施例1及び実施例2に於いて、それぞれ
の原廃水の水質データと、それぞれの曝気槽に前記組成
の生物共生菌を投入する前の水質データと、前記組成の
生物共生菌を投入7日後の水質データとを、次に示す測
定項目及び測定方法によって測定して、それぞれ表1及
び表2にまとめた。
In Examples 1 and 2, the water quality data of each raw wastewater, the water quality data before introducing the symbiotic bacterium of the above composition into each aeration tank, and the symbiotic bacterium of the above composition were used. The water quality data 7 days after the injection was measured by the following measurement items and measurement methods, and summarized in Table 1 and Table 2, respectively.

【0067】<測定項目及び測定方法> 1.排水量の測定 市販の流量計により測定する。 2.pHの測定 JIS K0102 12.1に基づき測定する。 3.BODの測定 JIS K0102 21に基づき測定する。 4.CODの測定 JIS K0102 17に基づき測定する。 5.SSの測定 S46環告59付表8に基づき測定する。 6.N−ヘキサン抽出物質の測定 S49環告64付表5に基づき測定する。 7.曝気槽に於ける臭いの判定 曝気槽に於ける運転中の臭いを嗅覚によって嗅ぎ分け表
現する。
<Measurement Item and Measurement Method> 1. Measurement of Discharged Water A commercially available flow meter is used for measurement. 2. Measurement of pH Measured according to JIS K0102 12.1. 3. BOD measurement It is measured according to JIS K01021. 4. COD measurement It is measured according to JIS K01021. 5. SS measurement S46 Announcement 59 Measure according to Appendix Table 8. 6. Measurement of N-hexane extract substance Measure according to S49 Announcement 64 Appendix 5. 7. Judgment of odor in the aeration tank The odor during operation in the aeration tank is scented and expressed.

【0068】[0068]

【表1】 [Table 1]

【0069】表1に示した実施例1の生物共生菌の投入
前後の水質試験の結果から分かるように、生物共生菌の
投入前の弱い腐敗臭が、投入後は活性汚泥処理特有のや
や甘酸っぱい臭いに変わってきており、はっきりと状態
が好転したことが感覚的に分かる。また生物共生菌の投
入前後のBOD、COD及びSSのそれぞれの値を見て
も数値が下がってきており、はっきりした効果が出てい
ることが分かる。
As can be seen from the results of the water quality test before and after the addition of the symbiotic bacterium of Example 1 shown in Table 1, the weak rotten odor before the addition of the symbiotic bacterium was slightly sweet and sour peculiar to the activated sludge treatment after the addition. The smell has changed, and you can clearly feel that the condition has improved. Also, looking at the respective values of BOD, COD, and SS before and after the addition of the symbiotic bacterium, the numerical values are decreasing, and it can be seen that there is a clear effect.

【0070】[0070]

【表2】 [Table 2]

【0071】表2に示すように、生物共生菌の投入前の
弱い腐敗臭が、投入後は活性汚泥処理特有のやや甘酸っ
ぱい臭いに変わってきており、実施例2に於いてもはっ
きりと状態が好転したことが感覚的に分かる。また、水
質試験結果に於いても生物共生菌の投入前後のBOD、
COD及びSSのそれぞれの値を見ても数値が下がって
きており、ここでもはっきりした効果が出ていることが
分かる。
As shown in Table 2, the weak rotten odor before the addition of the symbiotic bacterium has changed to a slightly sweet and sour odor peculiar to the activated sludge treatment after the addition, and the state is clearly shown in Example 2. You can feel the improvement. Also, in the water quality test results, BOD before and after the introduction of the symbiotic bacteria,
Looking at the respective values of COD and SS, the numerical values are decreasing, and it can be seen that a clear effect is obtained here as well.

【0072】[0072]

【発明の効果】以上述べたように、本発明の1の活性汚
泥処理の微生物相の再生及び体力増強方法によれば、原
廃水の導入量を減少させたり停止させることなく、通常
の運転を継続しながら原廃水を処理することができると
共に、曝気槽の微生物相を、短期間に手間をかけずに安
価にかつ安全に健全な状態に再生し、活性汚泥処理を正
常に復帰させることができる。
As described above, according to the method for regenerating microbial flora and enhancing the physical strength of the activated sludge process of the present invention 1, normal operation can be performed without reducing or stopping the introduction amount of raw wastewater. The raw wastewater can be treated while continuing, and the microbial flora in the aeration tank can be regenerated to a healthy state inexpensively and safely in a short period of time without any trouble, and the activated sludge treatment can be restored to normal. it can.

【0073】曝気槽内が、前記のような嫌気性状態、あ
るいは疑似嫌気性状態となってしまい、導入された原廃
水中の有機物が膠質のようなもので包まれるような状況
が発生してしまった場合、そのような状況の槽内であっ
ても、好気性菌に通性嫌気性菌及び嫌気性菌を共生させ
た前記生物共生菌を投入すると、前記膠質に包まれた有
機物の分解が開始するに至り、良好な分解活動が継続
し、BOD及びCOD成分の除去率を所要レベルにまで
回復し得ることとなるものである。
The inside of the aeration tank is in the anaerobic state or the pseudo-anaerobic state as described above, and a situation occurs in which the organic matter in the raw waste water introduced is wrapped in something like a colloid. If it does, even if it is inside the tank in such a situation, if the aerobic bacterium and the biosymbiotic bacterium in which the anaerobic bacterium is symbiotic are added, the decomposition of the organic matter encapsulated in the collagen is caused. As a result, good decomposition activity will continue, and the removal rates of BOD and COD components can be restored to the required levels.

【0074】これは、前記状況の槽内に前記生物共生菌
を投入すると、まず初めに、該菌中の嫌気性菌及び通性
嫌気性菌が作用して、前記有機物を包む膠質の膜を破る
とともに内部の有機物の分解を開始させ、引き続いて好
気性菌が作用して有機物の分解を一層進め、活性汚泥を
正常に復帰させることになるからであると推定すること
ができる。
This is because when the symbiotic bacterium is put into the tank in the above situation, first, the anaerobic bacterium and the facultative anaerobic bacterium in the bacterium act to act on the colloidal membrane wrapping the organic matter. It can be presumed that this is because when the organic sludge is broken, the decomposition of the organic matter in the inside is started, and subsequently the aerobic bacteria act to further promote the decomposition of the organic matter to restore the activated sludge to the normal state.

【0075】本発明の2は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、好気性菌60〜80%、通性嫌気性菌20
〜10%、嫌気性菌20〜10%の組成割合の菌群を採
用したものであり、それ故、本発明の2によれば、BO
D及びCOD成分の除去率の低下を起こしてきた活性汚
泥処理装置の曝気槽に投入する菌群中の好気性菌、通性
嫌気性菌及び嫌気性菌の菌群の割合が適切になるため、
本発明の1に関して説明した有機物の分解のプロセスが
良好に行われ得ることとなるものである。
The second aspect of the present invention is the method for regenerating microbial flora and enhancing the physical strength of the activated sludge process according to the first aspect of the present invention, wherein the aerobic bacterium is 60 to 80%, and the facultative anaerobic bacterium is 20% as the symbiotic bacterium.
A bacterium group having a composition ratio of 10% to 10% and an anaerobic bacterium of 20% to 10% is adopted. Therefore, according to 2 of the present invention, BO
Since the proportion of aerobic bacteria, facultative anaerobic bacteria and anaerobic bacteria groups in the bacterial groups to be put into the aeration tank of the activated sludge treatment device that has caused a decrease in the removal rate of D and COD components becomes appropriate. ,
The process of decomposing organic matter described in relation to 1 of the present invention can be well performed.

【0076】本発明の3は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、導入される原廃水の温度が25〜35℃の
場合には、この温度域で活発に活動する中温菌を主とし
て採用し、導入される原廃水の温度が25℃以下の場合
には、この温度域で活発に活動する低温菌を主として採
用することとしたものであり、それ故、本発明の3によ
れば、前記好気性菌、通性嫌気性菌及び嫌気性菌の各菌
群に属する菌を、導入される原廃水の温度に対応させ、
その温度で活発に活動するそれを採用することとしたの
で、より効率よく有機物等の分解活動が行い得られ、ス
ピーディに微生物相の再生及び体力増強の結果を得るこ
とができるものである。
The third aspect of the present invention is the method for regenerating the microbial flora of the activated sludge treatment of the first aspect of the present invention, wherein the raw wastewater introduced as the symbiotic bacterium has a temperature of 25 to 35 ° C. Decided to mainly adopt mesophilic bacteria that are active in this temperature range and, when the temperature of the raw wastewater to be introduced is 25 ° C or lower, mainly use low temperature bacteria that are active in this temperature range. Therefore, according to 3 of the present invention, the bacteria belonging to each of the aerobic bacteria, facultative anaerobic bacteria and anaerobic bacteria groups are made to correspond to the temperature of the raw wastewater to be introduced,
Since it is decided to use the one that is active at that temperature, it is possible to more efficiently decompose organic substances and the like, and it is possible to speedily obtain the results of microbial flora regeneration and physical strength enhancement.

【0077】本発明の4は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、原廃水の基質の濃度に応じた菌濃度のそれ
を投入することとしたものであり、それ故、本発明の4
によれば、原廃水の基質濃度に応じて菌濃度を調節し、
例えば、基質濃度が高い場合にも、キャリアの量を増加
させないで、必要な量の生物共生菌を投入することとし
たので、処理対象の廃水中に要分解物質を増加させない
で済むものである。
The fourth aspect of the present invention is the method for regenerating the microbial flora and enhancing the physical strength of the activated sludge process according to the first aspect, wherein the symbiotic bacterium is added at a microbial concentration corresponding to the concentration of the raw wastewater substrate. Therefore, according to the present invention,
According to, according to the substrate concentration of the raw wastewater, the bacterial concentration is adjusted,
For example, even when the substrate concentration is high, the required amount of the biosymbiotic bacterium is introduced without increasing the amount of the carrier, so that it is not necessary to increase the substance to be decomposed in the wastewater to be treated.

【0078】本発明の5は、本発明1の活性汚泥処理の
微生物相の再生及び体力増強方法に於いて、前記生物共
生菌として、好気性菌を主体とする酵母菌、子嚢菌及び
セルロース分解菌と、通性嫌気性菌を主体とする蛋白質
分解菌、乳酸菌及び枯草菌と、嫌気性菌を主体とする光
合成菌、窒素固定菌、酢酸菌及び酪酸菌とを含む菌群
を、キャリアに吸着固定させて共生させ、適用対象の原
廃水の基質濃度に対応する菌濃度に培養した複合微生物
菌を採用したものであり、それ故、本発明の5によれ
ば、生物共生菌を構成するのに必要な好気性菌、通性嫌
気性菌及び嫌気性菌の菌群について以上の各種の菌群を
選択したため、前記のように、BOD及びCOD成分の
除去率の低下を起こした状況の曝気槽中に、これらを投
入することにより、前記した嫌気性菌及び通性嫌気性菌
の作用及び好気性菌の作用、即ち、前者による膠質に包
まれた有機物の分解及び後者によるその後の有機物の酸
化分解の作用を効率良く行うことができ、その結果、B
OD及びCOD成分の除去率を所要レベルにまでスピー
ディに回復し得ることとなるものである。
The fifth aspect of the present invention is the method for regenerating the microbial flora of the activated sludge treatment and enhancing the physical strength of the first aspect of the present invention, wherein yeasts, ascomycetes and cellulosics mainly composed of aerobic bacteria are used as the symbiotic bacteria. Bacteria, proteolytic bacteria mainly composed of facultative anaerobic bacteria, lactic acid bacteria and Bacillus subtilis, and photosynthetic bacteria mainly composed of anaerobic bacteria, nitrogen-fixing bacteria, acetic acid bacteria and butyric acid bacteria as carriers, The present invention employs a complex microbial bacterium that is adsorbed, fixed and symbiotic, and cultivated at a bacterium concentration corresponding to the substrate concentration of the target wastewater to be applied. Therefore, according to 5 of the present invention, a symbiotic bacterium is constituted. Since the above-mentioned various bacterial groups were selected among the aerobic bacteria, facultative anaerobic bacteria and anaerobic bacteria necessary for the above, as described above, in the situation in which the removal rate of BOD and COD components was decreased By putting these into the aeration tank, The action of the anaerobic bacterium and the facultative anaerobic bacterium and the action of the aerobic bacterium, that is, the action of the decomposition of the organic substance encapsulated in the collagen by the former and the subsequent oxidative decomposition of the organic substance by the latter can be efficiently performed, As a result, B
The removal rate of the OD and COD components can be quickly recovered to the required level.

【0079】また以上の菌群によって構成される生物共
生菌を採用した場合は、有機物の分解に於いて、悪臭ガ
スの発生がなく、二酸化炭素と水とに効率的に分解され
るので、汚泥の発生が極めて少ないものとなって、汚泥
処理の負荷を軽減させるものとなる。
When a symbiotic bacterium composed of the above-mentioned group of bacteria is adopted, no odorous gas is generated in the decomposition of organic matter, and the organic matter is efficiently decomposed into carbon dioxide and water. The generation of sewage is extremely small, and the load of sludge treatment is reduced.

【0080】更にまた以上の菌群によって構成される生
物共生菌は、安全性が確保できるものであり、曝気槽に
投入され、活動を開始すると、該曝気槽の中で新たな生
物共生菌を生体合成するので、該曝気槽の微生物相は原
廃水の変動に対して耐性のある良好な状態となる。
Further, the symbiotic bacterium composed of the above-mentioned bacterium group can ensure the safety, and when it is put into the aeration tank and the activity is started, a new symbiotic bacterium is generated in the aeration tank. Since biosynthesis is carried out, the microflora of the aeration tank is in a good state of being resistant to fluctuations in the raw wastewater.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C12N 1/00 C12N 1/00 S //(C12N 1/00 C12R 1:01) C12R 1:01 (C12N 1/00 1:125 C12R 1:125) C12R 1:645 (C12N 1/00 C12R 1:645) (58)調査した分野(Int.Cl.7,DB名) C02F 3/12 C02F 3/34 ─────────────────────────────────────────────────── ─── Continued Front Page (51) Int.Cl. 7 Identification Code FI C12N 1/00 C12N 1/00 S // (C12N 1/00 C12R 1:01) C12R 1:01 (C12N 1/00 1: 125 C12R 1: 125) C12R 1: 645 (C12N 1/00 C12R 1: 645) (58) Fields investigated (Int.Cl. 7 , DB name) C02F 3/12 C02F 3/34

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 BOD及びCOD成分の除去率の低下を
起こしてきた活性汚泥処理装置の曝気槽に、好気性菌を
主体としこれに通性嫌気性菌及び若干の嫌気性菌を共存
させた生物共生菌を投入して攪拌曝気し、上記曝気槽の
微生物相の再生と微生物相の体力の増強とを図る活性汚
泥処理の微生物相の再生及び体力増強方法。
1. An aeration tank of an activated sludge treatment device, which has caused a reduction in the removal rate of BOD and COD components, is mainly composed of aerobic bacteria, and facultative anaerobic bacteria and some anaerobic bacteria are allowed to coexist therewith. A method for regenerating a microbial flora in an activated sludge process and a method for enhancing a stamina, which comprises introducing a symbiotic bacterium and stirring and aerating to revitalize the microbial fauna in the aeration tank and enhance the stamina of the microflora.
【請求項2】 前記生物共生菌として、好気性菌60〜
80%、通性嫌気性菌20〜10%、嫌気性菌20〜1
0%の組成割合の菌群を採用した請求項1の活性汚泥処
理の微生物相の再生及び体力増強方法。
2. An aerobic bacterium 60-as the symbiotic bacterium.
80%, facultative anaerobic bacteria 20 to 10%, anaerobic bacteria 20 to 1
The method for regenerating the microbial flora and enhancing the physical strength of the activated sludge process according to claim 1, wherein a bacterial group having a composition ratio of 0% is adopted.
【請求項3】 前記生物共生菌として、導入される原廃
水の温度が25〜35℃の場合には、この温度域で活発
に活動する中温菌を主として採用し、導入される原廃水
の温度が25℃以下の場合には、この温度域で活発に活
動する低温菌を主として採用することとした請求項1又
は2の活性汚泥処理の微生物相の再生及び体力増強方
法。
3. When the temperature of the raw wastewater to be introduced is 25 to 35 ° C., the mesophilic bacterium actively active in this temperature range is mainly used as the biosymbiotic bacterium, and the temperature of the raw wastewater to be introduced is selected. When the temperature is 25 ° C or lower, the method for regenerating microbial flora and enhancing the physical strength of the activated sludge treatment according to claim 1 or 2, wherein psychrophilic bacteria actively active in this temperature range are mainly adopted.
【請求項4】 前記生物共生菌として、原廃水の基質の
濃度に応じた菌濃度のそれを投入することとした請求項
1、2又は3の活性汚泥処理の微生物相の再生及び体力
増強方法。
4. The method for regenerating microbial flora and enhancing physical strength of activated sludge treatment according to claim 1, 2 or 3, wherein the symbiotic bacterium is added at a bacterium concentration corresponding to the concentration of a substrate of raw wastewater. .
【請求項5】 前記生物共生菌として、好気性菌を主体
とする酵母菌、子嚢菌及びセルロース分解菌と、通性嫌
気性菌を主体とする蛋白質分解菌、乳酸菌及び枯草菌
と、嫌気性菌を主体とする光合成菌、窒素固定菌、酢酸
菌及び酪酸菌とを含む菌群を、キャリアに吸着固定させ
て共生させ、適用対象の原廃水の基質濃度に対応する菌
濃度に培養した複合微生物菌を採用した請求項1、2又
は3の活性汚泥処理の微生物相の再生及び体力増強方
法。
5. As the symbiotic bacteria, yeasts, ascomycetes, and cellulolytic bacteria mainly composed of aerobic bacteria, proteolytic bacteria, lactic acid bacteria and Bacillus subtilis mainly composed of facultative anaerobic bacteria, and anaerobic A complex consisting of photosynthetic bacteria mainly consisting of bacteria, nitrogen-fixing bacteria, acetic acid bacteria and butyric acid bacteria, which are adsorbed and fixed on a carrier to coexist, and cultured at a bacterial concentration corresponding to the substrate concentration of the raw wastewater to be applied. The method for regenerating the microbial flora and enhancing the physical strength of the activated sludge treatment according to claim 1, 2 or 3 employing a microbial bacterium.
JP04864999A 1999-02-25 1999-02-25 Method for regenerating microflora and enhancing physical strength in activated sludge treatment Expired - Fee Related JP3400953B2 (en)

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