JPH06277686A - Treatment capacity recovery method for active sludge tank - Google Patents

Treatment capacity recovery method for active sludge tank

Info

Publication number
JPH06277686A
JPH06277686A JP5093779A JP9377993A JPH06277686A JP H06277686 A JPH06277686 A JP H06277686A JP 5093779 A JP5093779 A JP 5093779A JP 9377993 A JP9377993 A JP 9377993A JP H06277686 A JPH06277686 A JP H06277686A
Authority
JP
Japan
Prior art keywords
activated sludge
bacteria
sludge tank
treatment capacity
wastewater
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
JP5093779A
Other languages
Japanese (ja)
Other versions
JP3348904B2 (en
Inventor
Masaaki Okada
正明 岡田
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.)
Fujita Corp
Original Assignee
Fujita Corp
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 Fujita Corp filed Critical Fujita Corp
Priority to JP09377993A priority Critical patent/JP3348904B2/en
Publication of JPH06277686A publication Critical patent/JPH06277686A/en
Application granted granted Critical
Publication of JP3348904B2 publication Critical patent/JP3348904B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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

Landscapes

  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To recover the capacity in a period shorter than heretofore required when the drainage treatment capacity of an active sludge tank is lowered because of the variation in water quality. CONSTITUTION:A number of bacteria relating to the organic substance decomposition are separated from an active sludge tank representing good drainage treatment capacity, and the characteristics of the bacteria are confirmed and preserved. When the properties of active sludge is changed because the variation of water quality and the drainage treatment capacity is lowered, bacteria with which no resistance to the variation of water quality are selected out of the separated and preserved bacteria, and cultured in a perfect neutrified medium, anti proliferated bacteria are put into an active sludge tank.

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、有機性排水の浄化処理
に使われている活性汚泥槽の処理能力が低下したとき、
短時間で正常処理能力を回復させる方法に関するもので
ある。
BACKGROUND OF THE INVENTION The present invention relates to an activated sludge tank used for the purification treatment of organic waste water, when the treatment capacity of the activated sludge tank decreases.
The present invention relates to a method for recovering normal processing capacity in a short time.

【0002】[0002]

【従来の技術】食品工場廃水、薬品工場廃水、生活排
水、都市下水等の有機性排水の浄化処理には、好気性微
生物の有機物分解作用を利用する活性汚泥法がきわめて
有効であり、広く実施されている。周知のように、活性
汚泥法においては適量の活性汚泥を存在させた活性汚泥
槽に被処理排水を連続的に流入させ、ばっ気を行なって
酸素を供給しながら、活性汚泥中の微生物に有機物を分
解させる。
2. Description of the Related Art The activated sludge method, which utilizes the decomposition of organic substances by aerobic microorganisms, is extremely effective for the purification of organic wastewater such as food factory wastewater, chemical factory wastewater, domestic wastewater, and municipal wastewater. Has been done. As is well known, in the activated sludge method, the wastewater to be treated is continuously flown into an activated sludge tank in which an appropriate amount of activated sludge is present, aeration is performed to supply oxygen, and organic matter is added to microorganisms in the activated sludge. Disassemble.

【0003】活性汚泥は、ケイ素等の無機物も含むが、
大部分は、多種類の微生物、および微生物が細胞外に産
生した高分子化合物からなる。微生物は、主に細菌、酵
母、カビ、原生動物であって、このうち有機物の分解に
関与しているのは、事実上、細菌である。他の微生物
は、余剰有機物を分解するか、食物連鎖の関係上共生し
ている生物群であると考えられている。処理される有機
性排水中の有機物は、細菌群により一部はCO2、N2
2O等の無機物まで完全に分解され、一部は細菌の増
殖に利用される。増殖した細菌とそれが産生する高分子
化合物により、活性汚泥槽中の活性汚泥量は次第に増加
するので、過剰の活性汚泥は適宜槽外に取り出される。
Although activated sludge also contains inorganic substances such as silicon,
Most are composed of many kinds of microorganisms and macromolecular compounds produced extracellularly by the microorganisms. Microorganisms are mainly bacteria, yeasts, molds, and protozoa, of which bacteria are actually involved in the decomposition of organic matter. Other microorganisms are thought to be organisms that either decompose excess organic matter or are symbiotic in the context of the food chain. The organic matter in the organic wastewater to be treated is partly CO 2 , N 2 ,
Inorganic substances such as H 2 O are completely decomposed, and some of them are used for bacterial growth. Since the amount of activated sludge in the activated sludge tank gradually increases due to the grown bacteria and the polymer compound produced by it, excess activated sludge is appropriately taken out of the tank.

【0004】活性汚泥が有する有機物分解能力は、汚泥
中の一部少数の微生物の作用に基づくものではなく、き
わめて多数の微生物が様々な局面で有機物分解に関与す
ることにより発揮されているものである。したがって、
安定かつ良好な運転状態にある活性汚泥槽においては、
定常的に流入する排水の質(すなわち微生物にとっての
栄養源の種類)に応じて、その活性汚泥槽に特有の微生
物相が形成されている。このように質および量において
最適な活性汚泥が活性汚泥槽中に形成されていない場合
は、必要に応じて他の活性汚泥槽から種汚泥を持ち込
み、排水を流入させながら好ましい活性汚泥が十分形成
されるのを待つ。馴養と呼ばれるこの過程は、新たに運
転を開始する活性汚泥槽の場合で約30〜180日間を
必要とするのが普通である。
The ability of the activated sludge to decompose organic matter is not based on the action of a small number of microorganisms in the sludge, but is exerted by the involvement of an extremely large number of microorganisms in various aspects to decompose organic matter. is there. Therefore,
In an activated sludge tank that is stable and in good operating condition,
A microbial flora peculiar to the activated sludge tank is formed depending on the quality of effluent that constantly flows in (that is, the type of nutrient source for microorganisms). In this way, when the optimal activated sludge in terms of quality and quantity is not formed in the activated sludge tank, seed sludge is brought in from other activated sludge tanks as necessary and sufficient activated sludge is formed while inflowing wastewater. Wait to be done. This process, called acclimatization, usually requires about 30-180 days for a newly activated activated sludge tank.

【0005】良好な有機物分解能を示している活性汚泥
における細菌相の複雑かつ微妙なバランスは、処理する
排水の質の安定性の上に成り立っている。水質の変動幅
が大きいと、活性汚泥を利用する排水処理はほとんど成
り立たない。たとえば、処理する排水のpHが急激に低
下すると、そのpH変化に耐えられない細菌の数は直ち
に激減し、それによる細菌数減少は汚泥中細菌全体から
見れば僅かであっても、活性汚泥槽の処理能力は著しく
低下してしまう。そのため、活性汚泥法においては、活
性汚泥槽の前段に調整槽を設けることにより、活性汚泥
槽に供給する排水のpH、BOD、流入量等を調整し、
水質変動を一定の許容範囲内に抑えることが行われてい
る。しかしながら、工場排水や都市下水の性質上、予測
不可能な大幅または突発的な水質変動があるのは避けら
れないし、水質調整槽が故障することもあるから、水質
管理限界を超えた、活性汚泥中の細菌にとっては致命的
な水質の排水が処理槽に流入する事故が起こり得る。
The complex and delicate balance of bacterial flora in activated sludge, which exhibits good organic matter degrading, rests on the stability of the quality of the wastewater to be treated. If the fluctuation range of water quality is large, the wastewater treatment using activated sludge is hardly feasible. For example, when the pH of the wastewater to be treated drops sharply, the number of bacteria that cannot tolerate the change in pH is drastically reduced, and the decrease in the number of bacteria due to this is a slight amount of bacteria in sludge. The processing capacity of will be significantly reduced. Therefore, in the activated sludge method, by adjusting the tank before the activated sludge tank, the pH, BOD, inflow amount, etc. of the wastewater supplied to the activated sludge tank are adjusted,
Water quality fluctuations are kept within a certain allowable range. However, due to the nature of factory effluents and municipal sewage, it is unavoidable that there will be unpredictable large or sudden changes in water quality, and water quality control tanks may fail. An accident may occur in which wastewater of a water quality that is fatal to the bacteria inside flows into the treatment tank.

【0006】好ましくない水質の排水が流入し、活性汚
泥の細菌相が急変して排水処理能力が低下した場合、従
来は、速やかに流入排水の水質を管理範囲内に復帰させ
たのち、ときには活性汚泥をすべて他の活性汚泥槽のも
のと入れ替えるなどしてから、馴養によって活性汚泥が
従前の細菌相と量を回復するのを待つしかなかった。し
かしながら、このような従来の方法では、活性汚泥槽が
設計能力を回復するまでに約1カ月またはそれ以上の長
時日を要する。そして、このような事故による大きな経
済的損失を防止し、また未処理排水を排出する事態にな
るのを防止する必要上、従来の活性汚泥法による排水処
理では多くの安全対策およびバックアップ設備が必要で
あった。
When wastewater of undesired water quality flows in and the bacterial flora of the activated sludge suddenly changes and the wastewater treatment capacity deteriorates, conventionally, the quality of the inflowing wastewater is quickly returned to within the control range and sometimes activated. After replacing all the sludge with that of other activated sludge tanks, I had no choice but to wait for the activated sludge to recover the conventional bacterial flora and amount by acclimation. However, in such a conventional method, it takes about one month or more long time for the activated sludge tank to recover its design capacity. In addition, in order to prevent a large economic loss due to such an accident and prevent the situation where untreated wastewater is discharged, many safety measures and backup facilities are required for wastewater treatment by the conventional activated sludge method. Met.

【0007】馴養に要する日数を短縮する目的で、グル
コース等、細菌が一般的に好む栄養素を活性汚泥槽に添
加することは、最も増殖能力の高い細菌群によってその
栄養素が優先的に利用されてしまうため、活性汚泥量の
回復には有効であっても、細菌構成の点ではかえって好
ましくない変化をもたらす。
[0007] For the purpose of shortening the number of days required for acclimatization, it is necessary to add nutrients generally favored by bacteria such as glucose to the activated sludge tank because the nutrients are preferentially used by the bacterial group having the highest growth ability. Therefore, even if it is effective in recovering the amount of activated sludge, it brings about an undesirable change in terms of bacterial composition.

【0008】[0008]

【発明が解決しようとする課題】本発明の目的は、上述
のように突発的な事故により活性汚泥の細菌構成が変化
して活性汚泥槽の処理能力が著しく低下したときそれを
従来よりも短期間に回復させる方法を提供することにあ
る。
DISCLOSURE OF THE INVENTION The object of the present invention is, as described above, when the bacterial composition of activated sludge is changed due to a sudden accident and the treatment capacity of the activated sludge tank is remarkably reduced, it can be treated in a shorter period than before. It is to provide a way to recover in the meantime.

【0009】[0009]

【課題を解決するための手段】上記目的を達成すること
に成功した本発明は、活性汚泥槽に流入する排水の水質
変動により活性汚泥の排水処理能力が低下したとき、水
質変動によって菌数が激減した汚泥中細菌を、活性汚泥
槽の外で完全栄養培地を用いる個別培養により速やかに
増殖させ、それを活性汚泥槽に投入することにより馴養
に要する日数を短縮するものであって、そのために、あ
らかじめ、良好な排水処理能力を示している活性汚泥槽
から活性汚泥を採取し、採取された活性汚泥から有機物
分解に関与している細菌多数を分離し、それらの細菌の
特性を確認して保存しておくものである。
The present invention succeeded in achieving the above-mentioned object, and when the wastewater treatment capacity of activated sludge is reduced due to the fluctuation of the water quality of the wastewater flowing into the activated sludge tank, the number of bacteria is changed due to the fluctuation of the water quality. The bacteria in the sludge that has been drastically reduced are rapidly proliferated by individual culture using a complete nutrient medium outside the activated sludge tank, and the number of days required for acclimatization is shortened by introducing it into the activated sludge tank. In advance, we collected activated sludge from an activated sludge tank that showed good wastewater treatment capacity, separated many bacteria involved in the decomposition of organic matter from the collected activated sludge, and confirmed the characteristics of those bacteria. It is something to save.

【0010】以下、本発明の方法につき詳述する。良好
な排水処理能力を示している活性汚泥槽中の活性汚泥に
は、前述のように多数の細菌が存在し、それらが有機物
分解の複数の過程を分担している。たとえばタンパク質
は、アミノ酸からアセチルCoA、有機酸、NH4 +を経
由してN2ガス化になったり再びアミノ酸になって菌体
構成成分になったりするが、この分解過程のそれぞれ
に、特有の細菌が関与する。
The method of the present invention will be described in detail below. As described above, a large number of bacteria are present in the activated sludge in the activated sludge tank, which has a good wastewater treatment capacity, and these bacteria are responsible for a plurality of processes of organic matter decomposition. For example, a protein becomes an N 2 gasification from an amino acid via acetyl CoA, an organic acid, and NH 4 + , or becomes an amino acid again to become a bacterial cell constituent component. Bacteria are involved.

【0011】本発明実施のためには、まず上記有機物分
解の各過程について、有用細菌をなるべく多数採取し、
さらに、採取した各細菌について、それらの特性を確認
しグループ分けしておくことが必要である。具体的に
は、正常な活性汚泥から細菌分離の常法に従って純粋菌
株と目されるものを多数単離し、それらの特性を調べ
る。菌種の同定は不要である。細菌の特性は、たとえば
次のような項目について調べる。
In order to carry out the present invention, first, as many useful bacteria as possible are collected in each process of the above organic substance decomposition,
Furthermore, it is necessary to confirm the characteristics of each of the collected bacteria and divide them into groups. Specifically, a large number of pure strains, which are regarded as pure strains, are isolated from normal activated sludge according to a conventional method for separating bacteria, and their characteristics are examined. Identification of the bacterial species is unnecessary. For the characteristics of bacteria, for example, the following items are examined.

【0012】A.排水中の主要有機物に対する分解能力
の有無(これにより、その菌株が排水中有機物に対する
一次分解者か否かがわかる)。 B.有機物を最終的に無機物(CO2、N2等)に分解す
る能力の有無(これにより、その菌株が排水中有機物に
対する最終分解者か否かがわかる)。 C.活性汚泥の好ましい物性(フロック形成性)を維持
する能力の有無(これにより、単なる有機物分解能だけ
でなく、処理液を分離排出しやすくするためのフロック
形成能力があるか否かがわかる)。 D.処理する排水中における増殖の速さ(これにより、
有機物を分解、吸収、利用する能力が高く、活性汚泥中
の優先菌になりやすいか否かがわかる)。 E.活性汚泥構成細菌中での存在比率(存在比率が高い
ものほど分解能も高いとは限らないが、何らかの形で活
性汚泥の物性に影響するところが大きい)。
A. Presence or absence of decomposing ability for major organic matter in wastewater (this indicates whether the strain is a primary decomposer for organic matter in wastewater). B. Presence or absence of the ability to finally decompose organic matter into inorganic matter (CO 2 , N 2, etc.) (this indicates whether or not the strain is the final decomposer for organic matter in wastewater). C. Presence or absence of ability to maintain preferable physical properties (floc forming property) of activated sludge (this makes it possible to determine not only mere organic matter decomposing ability but also flock forming ability for facilitating separation and discharge of treated liquid). D. Propagation speed in wastewater to be treated
It has a high ability to decompose, absorb, and use organic matter, and it is easy to see whether it tends to become priority bacteria in activated sludge). E. Abundance in activated sludge-forming bacteria (higher abundance does not necessarily mean higher resolution, but it has a great influence on the physical properties of activated sludge in some way).

【0013】どのような項目を重視するかは、活性汚泥
処理方法の種類、処理の目的等に合わせて決める。たと
えば、窒素化合物の除去を目的としない好気性活性汚泥
槽の場合には、窒素化合物をN2ガスまで分解する能力
の確認は重要でなく、炭水化物の分解除去能力を重視す
る。以上により、活性汚泥が示す多くの能力のどの場面
でその細菌が関与しているかが確認できる。
The items to be emphasized are decided depending on the type of the activated sludge treatment method, the purpose of the treatment and the like. For example, in the case of an aerobic activated sludge tank which is not intended to remove nitrogen compounds, confirmation of the ability to decompose nitrogen compounds to N 2 gas is not important, but the ability to decompose and remove carbohydrates is emphasized. From the above, it is possible to confirm in which of the many capabilities of activated sludge the bacteria are involved.

【0014】次に、各細菌について、被処理排水の水質
変動に対する抵抗性試験を行う。試験項目は、被処理排
水の種類、活性汚泥処理法の種類、施設の周辺環境等も
考慮して決定する。たとえば次のような特性を確認す
る。 a.pH変化に対する抵抗性 b.被処理排水のBODの変化に対する抵抗性 c.活性汚泥槽における有機物分解反応中間生成物(有
機酸、NO2 -、NH4 +、P等)の蓄積に対する抵抗性 d.細菌にとっての毒性物質(有機溶媒、界面活性剤、
重金属イオン、油脂等)に対する抵抗性 e.温度変化に対する抵抗性
Next, for each bacterium, a resistance test against the water quality fluctuation of the wastewater to be treated is conducted. The test items are determined in consideration of the type of wastewater to be treated, the type of activated sludge treatment method, and the environment surrounding the facility. For example, confirm the following characteristics. a. Resistance to pH changes b. Resistance of treated wastewater to changes in BOD c. Resistance to accumulation of intermediate products of organic substance decomposition reaction (organic acid, NO 2 , NH 4 + , P, etc.) in activated sludge tank d. Toxic substances for bacteria (organic solvents, surfactants,
Resistance to heavy metal ions, fats and oils) e. Resistance to temperature changes

【0015】上述のようにして確認された特性に基づ
き、すべての細菌をまず有機物分解特性の観点から分類
し(一次分類)、分類された各細菌をさらに対水質変動
抵抗性の観点から分類する(二次分類)。分類された細
菌は、それを増殖させるのに適した培地と培養条件を確
認した上で、いつでも培養可能な状態にして保存する。
Based on the characteristics confirmed as described above, all bacteria are first classified from the viewpoint of organic matter decomposition characteristics (primary classification), and each classified bacteria is further classified from the viewpoint of resistance to water quality fluctuation. (Secondary classification). The classified bacteria are stored in a state in which they can be cultivated at any time after confirming the medium and the culture conditions suitable for growing them.

【0016】活性汚泥槽に流入する被処理排水の水質に
大幅な変動があって活性汚泥がダメージを受け、排水処
理能力が著しく低下する事故があった場合は、速やかに
水質変動の内容を確認する(水質が管理範囲から外れた
ままになっているときは確認された原因を排除して水質
を安定させる。)。
If there is a large change in the quality of the wastewater to be treated that flows into the activated sludge tank and the activated sludge is damaged and the wastewater treatment capacity is significantly reduced, check the contents of the change in water quality immediately. (If the water quality remains out of the control range, eliminate the confirmed cause and stabilize the water quality.)

【0017】一方、確認された水質変動の内容から、死
滅ないしは菌数が激減したと推定される細菌がわかるか
ら、それを前述の保存菌株の中から選び出す(二次分類
の基準となった抵抗性試験の結果を参照して選択す
る)。選択は、一次分類の各群菌株について行う。そし
て、選出された複数の菌株を個々に、それらに好適な培
地を用い好適培養条件で培養する。個々の菌株について
好適な培地および培養条件を採用して行う培養は、グル
コースを含む完全栄養培地で増殖する有機物分解細菌の
場合、約5〜7日という短期間で種菌数の約1000倍
まで増殖させることができる。
On the other hand, from the contents of the confirmed water quality fluctuations, it is possible to identify bacteria that are presumed to have been killed or the number of bacteria has been drastically reduced. Therefore, they are selected from the above-mentioned preserved strains (resistance as a criterion for secondary classification). Select by referring to the results of the sex test). Selection is performed for each group of strains in the primary classification. Then, the plurality of selected strains are individually cultured under a suitable culture condition using a suitable medium for them. Cultivation using a suitable medium and culture conditions for individual strains can grow up to about 1000 times the inoculum number in a short period of about 5 to 7 days in the case of organic matter-degrading bacteria that grow in a complete nutrient medium containing glucose. Can be made.

【0018】正常な活性汚泥における存在比率を回復さ
せるのに十分な菌数が得られたならば、培養物をそのま
ま、または培養物から分離した菌体を、上記能力低下を
起こした活性汚泥槽に投入する。投入量は、事故前の細
菌構成の活性汚泥を復元するのに必要な量を、分離菌中
での各細菌の存在比率、活性汚泥中の従属栄養細菌総
数、事故による従属栄養細菌の死滅率(別途測定する)
等を勘案して決定することが望ましいが、それほど厳密
に計算しなくても、馴養期間短縮の目的は達成される。
これにより槽内活性汚泥の細菌構成はほぼ事故前の状態
に復帰するから、以後、ごく短期間の馴養を行うことに
より、処理槽の排水処理能力を完全に回復させることが
できる。
Once a sufficient number of bacteria has been obtained to restore the abundance ratio in normal activated sludge, the culture as it is or the bacterial cells separated from the culture are treated with the activated sludge tank in which the above-mentioned capacity deterioration has occurred. Throw in. The input amount is the amount necessary to restore the activated sludge of bacterial composition before the accident, the abundance of each bacterium in the isolate, the total number of heterotrophic bacteria in the activated sludge, and the death rate of heterotrophic bacteria due to the accident. (Measure separately)
It is desirable to make a decision taking into consideration the above, but the goal of shortening the acclimatization period can be achieved without rigorous calculation.
As a result, the bacterial composition of the activated sludge in the tank is almost restored to the state before the accident. Therefore, the effluent treatment capacity of the treatment tank can be completely restored by acclimation for a very short period thereafter.

【0019】[0019]

【実施例】【Example】

実施例1 タンパク質系食品工場廃水を処理対象とし、ベンチスケ
ール回分式活性汚泥槽(容積10リットル)2基によ
り、活性汚泥3000mgMLSS/l、BOD-SS負荷
0.05kg/kg・日、廃水有機物濃度1200mg/l、pH
6.8の条件で好気処理を行い、BOD除去率95%の
状態に達した。
Example 1 Protein-based food factory wastewater was treated, and two bench-scale batch-type activated sludge tanks (volume: 10 liters) were used to activate activated sludge 3000 mg MLSS / l, BOD-SS load 0.05 kg / kg-day, wastewater organic matter concentration. 1200 mg / l, pH
Aerobic treatment was carried out under the conditions of 6.8, and the BOD removal rate reached 95%.

【0020】この活性汚泥槽の活性汚泥の一部を採取
し、次の手順で細菌分離を行なった。まず活性汚泥をホ
モジナイザーで均一化し、得られた活性汚泥懸濁液を滅
菌生理食塩水で希釈し104〜108の範囲で5段階の濃
度の希釈液を調製し、各希釈液1mlを廃水寒天平板培地
10mlに混釈して25℃で3〜10日間培養する。発現
したコロニーを継日的に分離し、標準寒天培地に接種す
る操作を数回繰り返す。106倍希釈の廃水寒天培地に
培養10日目で109コロニー/プレートの細菌コロニ
ーが得られ、この中から、コロニーが確認された培養3
日目、5日目、7日目、10日目の4段階に分けて合計
67コロニーを、乱数表を用いてランダムに釣菌した。
各コロニーは標準寒天培地に2回植えかえて、67株の
活性汚泥由来細菌を得た。
A part of the activated sludge in this activated sludge tank was sampled, and bacteria were separated by the following procedure. First, the activated sludge is homogenized with a homogenizer, and the resulting activated sludge suspension is diluted with sterile physiological saline to prepare a diluted solution having a concentration of 5 steps within a range of 10 4 to 10 8 , and 1 ml of each diluted solution is used as waste water. Pour 10 ml of agar plate medium and incubate at 25 ° C for 3 to 10 days. The operation of isolating the expressed colonies daily and inoculating the standard agar medium is repeated several times. On the 10th day of culture, 109 colonies / plate of bacterial colonies were obtained on the 10 6- fold diluted waste water agar medium. From among these, cultures in which colonies were confirmed 3
A total of 67 colonies were randomly picked by using a random number table in four stages on the 5th, 7th and 10th days.
Each colony was replanted twice in a standard agar medium to obtain 67 strains of activated sludge-derived bacteria.

【0021】次いで各菌株について下記の試験を行い、
コロニー発現日数および性質試験の結果を基に菌株を8
群に分け、さらに各群菌株をpH抵抗性に基づき3段階
にランク付けした。 コロニー発現日 グラム染色性 チトクロームオキシダーゼ試験 カタラーゼ試験 糖類分解性試験(OFテストおよびグルコース、寒天、
デンプン、セルロース、グリセロール) タンパク質分解性試験(ペプトン、コラーゲン、カゼイ
ン、肝臓抽出物、心筋抽出物)
Next, the following tests were carried out for each strain,
8 strains were selected based on the number of days of colony development and the results of characterization tests.
The strains were divided into groups, and the strains in each group were ranked in three stages based on pH resistance. Colony expression day Gram stainability Cytochrome oxidase test Catalase test Sugar degradation test (OF test and glucose, agar,
Starch, cellulose, glycerol) Proteolytic test (peptone, collagen, casein, liver extract, myocardial extract)

【0022】特有物質分解性試験(廃水培地および食品
工場工程中の原料抽出物) 細胞形態検鏡(フロック形成の要因となる構造物の有無
を確認) 硝酸還元能試験 pH抵抗性試験(7.2〜4.4の範囲でpHを段階的に調
整された廃水を用意し、これに同量の菌体を接種して2
5℃で3〜7日間振盪培養する。この間、分解される有
機物残量を継日的に定量する。 その後、全菌株は、凍結乾燥するか、低温保存と継代培
養の繰り返しにより、種菌として保存した。
Degradation test for specific substances (raw water medium and raw material extract in food factory processes) Cell morphology microscopy (check for the presence of structures that cause floc formation) Nitrate reduction test pH resistance test (7. Prepare a wastewater whose pH is adjusted stepwise in the range of 2 to 4.4, and inoculate this with the same amount of bacterial cells.
Incubate with shaking at 5 ° C for 3 to 7 days. During this period, the remaining amount of decomposed organic matter is quantified daily. Thereafter, all strains were freeze-dried or were preserved as inoculum by repeated low temperature storage and subculture.

【0023】一方、運転中の上記2基の活性汚泥槽に、
前段pH調整槽の事故を想定してpH4.0の廃水を2時
間供給した。それにより、槽内pHは、6.8であったも
のが4.4まで低下した。供給する廃水のpHを6.8に
戻して運転を再開したが、BOD除去率は66%に低下
していた。この後、2基の活性汚泥槽のうち一方は、比
較のため自然回復を期待する従来どおりの馴養運転を続
けた。
On the other hand, in the above two activated sludge tanks in operation,
Assuming an accident in the former pH adjusting tank, waste water of pH 4.0 was supplied for 2 hours. As a result, the pH in the tank was lowered from 6.8 to 4.4. The pH of the waste water supplied was returned to 6.8 and the operation was restarted, but the BOD removal rate had dropped to 66%. After this, one of the two activated sludge tanks continued to be acclimatized as usual, expecting natural recovery for comparison.

【0024】別の活性汚泥槽に対しては、本発明による
処理能力回復を試みた。すなわち、前述の保存菌株の中
からpH抵抗性の最も弱いグループに属する細菌群を選
び出し、さらにその中から、廃水中有機物の分解能が高
く、チトクロームオキシダーゼ・カタラーゼ陽性(酸素
を利用してエネルギーを得るためのチトクローム系酵素
が存在すると共に酸素利用系で産生する毒性物質を分解
するカタラーゼが存在することを示し、有機物を好気的
に炭酸ガスまで分解する能力があることを意味する。)
であって、コロニー発現日数3日以内のグループより、
形態的に異なるグラム陰性桿菌を2株、同様の性質でコ
ロニー発現日数3日以上5日未満のグループより形態的
に異なるグラム陰性桿菌を2株、および形態的に定着性
の構造を有し分離菌株の約36%を占める細菌グループ
から1株、合計5株を選び、それらを、ペプトン0.5
%、酵母エキス0.25%、グルコース0.1%、pH7.
0の液体培地で7日間培養した。次いで各培養液を遠心
分離して菌体を採取し、それらを、pH低下前の活性汚
泥と同様の細菌構成のものに活性汚泥を復元するのに必
要な量だけ計量して、活性汚泥槽に投入した。なお、必
要投入量は、最初に活性汚泥から分離された細菌67株
中での各細菌の存在比率、活性汚泥中の従属栄養細菌数
(1.09×108cell/ml)、および別途確認された従
属栄養細菌死滅率(37%)より算出した。
For another activated sludge tank, an attempt was made to recover the treatment capacity according to the present invention. That is, from the above-mentioned preserved strains, a group of bacteria belonging to the weakest group of pH resistance was selected, and from them, the organic matter in wastewater was highly decomposable, and cytochrome oxidase / catalase positive (oxygen was used to obtain energy. It shows that there is a cytochrome enzyme for this and catalase that decomposes toxic substances produced in the oxygen utilization system, which means that it has the ability to aerobically decompose organic substances to carbon dioxide gas.)
And from the group within 3 days of colony expression,
2 strains of morphologically different Gram-negative bacilli, 2 strains of morphologically different gram-negative bacilli from a group with the same properties and colony expression days of 3 days or more but less than 5 days Choose one strain from the bacterial group, which accounts for about 36% of the strains, a total of 5 strains, and select them from peptone 0.5
%, Yeast extract 0.25%, glucose 0.1%, pH 7.
It was cultured in 0 liquid medium for 7 days. Next, each culture solution is centrifuged to collect the bacterial cells, and the amount of them is measured to restore the activated sludge to a bacterial composition similar to that of the activated sludge before pH reduction. I put it in. The required input amount is the ratio of each bacterium in 67 strains of bacteria isolated from the activated sludge, the number of heterotrophic bacteria in the activated sludge (1.09 × 10 8 cells / ml), and a separate confirmation. It was calculated from the killed heterotrophic bacteria (37%).

【0025】培養菌株を投入し運転を再開してから2日
後、BOD除去率は93%に回復し、回復に要した日数
は合計9日間であった。一方、単なる馴養による処理能
力回復を期待した別の活性汚泥槽は、BOD除去率が9
3%まで回復するのに35日を要した。
Two days after the culture strain was added and the operation was restarted, the BOD removal rate recovered to 93%, and the total number of days required for recovery was 9 days. On the other hand, another activated sludge tank, which was expected to recover the treatment capacity by mere acclimatization, had a BOD removal rate of 9
It took 35 days to recover to 3%.

【0026】[0026]

【発明の効果】上述のように、水質変動によって菌数が
減少した細菌を活性汚泥槽とは別の培養装置で速やかに
増殖させて活性汚泥槽に投入する本発明によれば、水質
変動にともない低下した活性汚泥槽の処理能力を従来よ
りもはるかに短い日数で回復させることができる。
Industrial Applicability As described above, according to the present invention, the bacteria whose number of bacteria has been reduced due to water quality fluctuations are rapidly proliferated in a culture device different from the activated sludge tank and are introduced into the activated sludge tank. Along with this, it is possible to recover the lowered treatment capacity of the activated sludge tank in a much shorter time than before.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 良好な排水処理能力を示している活性汚
泥槽から活性汚泥を採取し、採取された活性汚泥から有
機物分解に関与している細菌多数を分離し、それらの細
菌の特性を確認して保存すること;および、活性汚泥槽
に流入する排水の水質変動により活性汚泥が変質して排
水処理能力が低下したとき、上記分離保存菌の中から上
記水質変動に対する抵抗性がないことが確認されている
細菌を選んでそれを完全栄養培地で培養し、増殖した菌
体を上記活性汚泥槽に投入して馴養を行うこと;を特徴
とする、活性汚泥槽の処理能力回復方法。
1. An activated sludge is collected from an activated sludge tank showing good wastewater treatment capacity, a large number of bacteria involved in the decomposition of organic matter are separated from the collected activated sludge, and the characteristics of those bacteria are confirmed. And, when the activated sludge is deteriorated due to the water quality fluctuation of the wastewater flowing into the activated sludge tank and the wastewater treatment capacity is reduced, there is no resistance to the water quality fluctuation among the isolated and preserved bacteria. A method for recovering the treatment capacity of an activated sludge tank, which comprises selecting a confirmed bacterium, culturing it in a complete nutrient medium, and introducing the grown bacterial cells into the activated sludge tank for acclimatization.
JP09377993A 1993-03-30 1993-03-30 Recovery method of activated sludge tank capacity Expired - Fee Related JP3348904B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
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JPH06277686A true JPH06277686A (en) 1994-10-04
JP3348904B2 JP3348904B2 (en) 2002-11-20

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Country Status (1)

Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015145866A1 (en) * 2014-03-27 2015-10-01 三菱重工業株式会社 Laundry wastewater biological treatment preparation, and device and method for treating laundry wastewater by using same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015145866A1 (en) * 2014-03-27 2015-10-01 三菱重工業株式会社 Laundry wastewater biological treatment preparation, and device and method for treating laundry wastewater by using same
JP2015188815A (en) * 2014-03-27 2015-11-02 三菱重工業株式会社 Biological treatment formulation for cleaning effluent, apparatus and method for treating cleaning effluent using the same
US10259733B2 (en) 2014-03-27 2019-04-16 Mitsubishi Heavy Industries, Ltd. Laundry wastewater biological treatment preparation, and device and method for treating laundry wastewater by using same

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