JP3348904B2 - Recovery method of activated sludge tank capacity - Google Patents
Recovery method of activated sludge tank capacityInfo
- Publication number
- JP3348904B2 JP3348904B2 JP09377993A JP9377993A JP3348904B2 JP 3348904 B2 JP3348904 B2 JP 3348904B2 JP 09377993 A JP09377993 A JP 09377993A JP 9377993 A JP9377993 A JP 9377993A JP 3348904 B2 JP3348904 B2 JP 3348904B2
- Authority
- JP
- Japan
- Prior art keywords
- activated sludge
- bacteria
- wastewater
- sludge tank
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
Description
【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 its treatment capacity is reduced.
The present invention relates to a method for restoring normal processing ability 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 utilizing the organic matter decomposing action of aerobic microorganisms is extremely effective for the purification treatment of organic wastewater such as food factory wastewater, chemical factory wastewater, domestic wastewater, and urban sewage. Have been. 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, and while aeration is being performed to supply oxygen, microorganisms in the activated sludge are reduced by organic substances. Is disassembled.
【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、
H2O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。[0003] Activated sludge includes inorganic substances such as silicon,
Most consist of many types of microorganisms and macromolecular compounds produced extracellularly by the microorganisms. Microorganisms are mainly bacteria, yeasts, molds and protozoa, of which bacteria are in fact involved in the breakdown of organic matter. Other microorganisms are thought to be organisms that either degrade excess organic matter or coexist in the food chain. The organic matter in the treated organic wastewater is partially CO 2 , N 2 ,
It is completely decomposed to inorganic substances such as H 2 O, and part of it is used for bacterial growth. Since the amount of activated sludge in the activated sludge tank gradually increases due to the multiplied bacteria and the polymer compound produced by the bacteria, 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。[0004] The ability of activated sludge to decompose organic substances is not based on the action of a small number of microorganisms in the sludge, but is exerted by an extremely large number of microorganisms participating in the decomposition of organic substances in various aspects. is there. Therefore,
In an activated sludge tank in a stable and good operating condition,
Depending on the quality of the effluent that constantly flows in (ie, the type of nutrient source for the microorganism), a microflora unique to the activated sludge tank is formed. As described above, when the optimum activated sludge in terms of quality and quantity is not formed in the activated sludge tank, seed sludge is brought in from another activated sludge tank as needed, and sufficient activated sludge is sufficiently formed while inflowing wastewater. Wait for it to be done. This process, called acclimation, 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。[0005] The complex and subtle balance of bacterial flora in activated sludge exhibiting good organic matter resolution is based on the stability of the quality of the treated wastewater. If the fluctuation range of water quality is large, the wastewater treatment using activated sludge is hardly feasible. For example, if the pH of the wastewater to be treated drops sharply, the number of bacteria that cannot withstand the pH change immediately drops. The processing performance of the device is significantly reduced. Therefore, in the activated sludge method, the pH, BOD, inflow amount, etc. of the wastewater supplied to the activated sludge tank are adjusted by providing an adjustment tank before the activated sludge tank.
Water quality fluctuations are kept within a certain allowable range. However, due to the characteristics of industrial wastewater and municipal sewage, it is inevitable that unpredictable large or sudden fluctuations in water quality will occur, and water quality control tanks may fail. An accident can occur in which drainage of water quality, which is fatal to 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。[0006] When wastewater of undesired water quality flows in and the bacterial flora of the activated sludge suddenly changes and the wastewater treatment capacity is reduced, conventionally, the water quality of the inflowed wastewater is quickly returned to within a control range, and sometimes the activated water is activated. After replacing all the sludge with that of another activated sludge tank, it was necessary to wait for the activated sludge to recover its previous bacterial flora and quantity by habituation. However, in such a conventional method, it takes about one month or more long days before the activated sludge tank recovers its design capacity. In addition, it is necessary to prevent large economic losses due to such accidents and to prevent untreated wastewater from being discharged, and 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] The addition of nutrients generally preferred by bacteria, such as glucose, to the activated sludge tank for the purpose of shortening the number of days required for acclimation, requires that the nutrients are preferentially used by the bacteria 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 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。SUMMARY OF THE INVENTION It is an object of the present invention to reduce the bacterial sludge composition of activated sludge due to a sudden accident, as described above, so that the treatment capacity of the activated sludge tank is significantly reduced. It is to provide a way to recover in time.
【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。SUMMARY OF THE INVENTION The present invention, which has succeeded in achieving the above object, has an advantage that when the wastewater treatment capacity of the activated sludge decreases due to the fluctuation of the water quality of the wastewater flowing into the activated sludge tank, the number of bacteria is reduced by the fluctuation of the water quality. The bacteria in the sludge that has been drastically reduced are rapidly grown outside the activated sludge tank by individual cultivation using a complete nutrient medium, and are fed into the activated sludge tank to shorten the days required for acclimation. In advance, the activated sludge was collected from an activated sludge tank showing good wastewater treatment capacity, and a large number of bacteria involved in organic matter decomposition were separated from the collected activated sludge, and the characteristics of those bacteria were confirmed. It is something to keep.
【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。Hereinafter, the method of the present invention will be described in detail. Activated sludge in an activated sludge tank exhibiting a good wastewater treatment capacity contains a large number of bacteria as described above, which share a plurality of processes of organic matter decomposition. For example, proteins are converted into N 2 gas from amino acids via acetyl-CoA, organic acids, and NH 4 +, and are converted again into amino acids to become bacterial cell components. 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, as many useful bacteria as possible are collected in each step of the above-mentioned organic matter decomposition.
In addition, it is necessary to confirm the characteristics of each of the collected bacteria and group them. Specifically, a number of pure strains which are regarded as pure strains are isolated from normal activated sludge in accordance with an ordinary method for separating bacteria, and their characteristics are examined. No identification of bacterial species is required. The characteristics of bacteria are examined, for example, for the following items.
【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. Whether or not the strain is capable of decomposing major organic matter in wastewater (this indicates whether the strain is a primary decomposer for organic matter in wastewater). B. The ability to decompose organic matter into inorganic matter (CO 2 , N 2, etc.) (whether or not the strain is the final decomposer for organic matter in wastewater). C. Whether or not the activated sludge has the ability to maintain the preferable physical properties (floc-forming ability) (this indicates whether or not the activated sludge has the ability to form a floc for facilitating separation and discharge of the treatment liquid as well as simple organic substance resolution). D. The speed of growth in the wastewater to be treated (this allows
It has a high ability to decompose, absorb, and use organic matter, indicating that it is likely to become a priority bacterium in activated sludge.) E. FIG. The abundance ratio in activated sludge-constituting bacteria (the higher the abundance ratio, the higher the resolution is not necessarily higher, but it greatly affects the physical properties of the 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 determined according to 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 not intended to remove nitrogen compounds, it is not important to confirm the ability to decompose nitrogen compounds to N 2 gas, but to emphasize the ability to decompose and remove carbohydrates. From the above, it is possible to confirm in which scene of the 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, a resistance test is performed on each bacterium against fluctuations in water quality of the wastewater to be treated. The test items are determined in consideration of the type of wastewater to be treated, the type of activated sludge treatment method, the surrounding environment of the facility, and the like. For example, confirm the following characteristics. a. Resistance to pH changes b. Resistance of the wastewater to be treated to changes in BOD c. Resistance to accumulation of organic matter decomposition reaction intermediate products (organic acid, NO 2 − , NH 4 + , P, etc.) in the activated sludge tank d. Toxic substances for bacteria (organic solvents, surfactants,
Resistance to heavy metal ions, fats and oils, etc. 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 the classified bacteria are further classified from the viewpoint of resistance to fluctuations in water quality. (Secondary classification). The classified bacteria are stored in a state where they can be cultured at any time after confirming a medium and culture conditions suitable for growing the bacteria.
【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 fluctuation in the water quality of the treated wastewater flowing into the activated sludge tank and the activated sludge is damaged and there is an accident that significantly reduces the wastewater treatment capacity, the contents of the water quality fluctuation are immediately confirmed. (If the water quality remains out of the management range, eliminate the identified 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 known that the bacteria are presumed to have died or the number of bacteria has been drastically reduced. Therefore, those bacteria are selected from the above-mentioned preserved strains (the resistance which became the standard for the secondary classification). Select with reference to the results of the sex test). Selection is performed for each group strain of the primary classification. Then, the plurality of selected strains are individually cultured under suitable culture conditions using a medium suitable for them. Cultivation of individual strains using a suitable medium and culture conditions is carried out in a short period of about 5 to 7 days for organic matter-degrading bacteria growing in a complete nutrient medium containing glucose, to about 1000 times the number of inoculum. Can be done.
【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。If a sufficient number of bacteria is obtained to restore the abundance ratio in normal activated sludge, the culture as it is or the cells separated from the culture can be transferred to an activated sludge tank having the above-mentioned reduced capacity. To The input amount is the amount required to restore the activated sludge of the bacterial composition before the accident, the percentage of each bacterium in the isolated bacteria, the total number of heterotrophic bacteria in the activated sludge, the death rate of the heterotrophic bacteria due to the accident (Measured separately)
Although it is desirable to determine in consideration of such factors, the purpose of shortening the acclimatization period can be achieved without calculating so strictly.
As a result, the bacterial composition of the activated sludge in the tank is almost returned to the state before the accident, and thereafter, by performing acclimation for a very short time, the wastewater treatment capacity of the treatment tank can be completely recovered.
【0019】[0019]
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 Activated sludge 3000 mg MLSS / l, BOD-SS load 0.05 kg / kg / day, wastewater organic matter concentration, using two bench-scale batch activated sludge tanks (volume 10 liters) for treating protein-based food factory wastewater 1200 mg / l, pH
Aerobic treatment was performed under the conditions of 6.8, and the state reached a BOD removal rate of 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 the activated sludge tank was collected, and the bacteria were separated by the following procedure. First, the activated sludge was homogenized with a homogenizer, and the obtained activated sludge suspension was diluted with sterile physiological saline to prepare diluents having five concentrations in the range of 10 4 to 10 8. The mixture is mixed with 10 ml of agar plate medium and cultured at 25 ° C. for 3 to 10 days. The procedure of separating the expressed colonies on a daily basis and inoculating them on a standard agar medium is repeated several times. On day 10 of the culture, 109 colonies / plate of bacterial colonies were obtained on the 10 6- fold diluted wastewater agar medium.
A total of 67 colonies were randomly picked using a random number table in four stages on day 5, day 7, day 7, and day 10.
Each colony was replanted twice on 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 performed for each strain,
Based on the number of days of colony expression and the results of the property test, 8 strains were
The strains were divided into groups, and the strains in each group were ranked in three stages based on pH resistance. Date of colony expression Gram stain Cytochrome oxidase test Catalase test Saccharolysis 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。Specific substance degradation test (wastewater medium and raw material extract in food factory process) Cell morphology microscopy (confirmation of the presence or absence of a structure that causes floc formation) nitrate reduction ability test pH resistance test (7. A wastewater whose pH is adjusted stepwise within the range of 2 to 4.4 is prepared, and the same amount of bacterial cells is inoculated into the wastewater.
Incubate with shaking at 5 ° C for 3-7 days. During this time, the remaining amount of the organic matter to be decomposed is quantified daily. Thereafter, all strains were freeze-dried or stored 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, the two activated sludge tanks in operation are:
Wastewater of pH 4.0 was supplied for 2 hours in anticipation of an accident in the preceding pH adjustment tank. As a result, the pH in the tank decreased from 6.8 to 4.4. The operation was restarted after the pH of the supplied wastewater was returned to 6.8, but the BOD removal rate had dropped to 66%. Thereafter, one of the two activated sludge tanks continued the conventional acclimatization operation for which natural recovery was expected 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 processing capacity according to the present invention. That is, a bacterial group belonging to the group having the weakest pH resistance is selected from the above-mentioned stock strains, and furthermore, the resolution of organic matter in wastewater is high and cytochrome oxidase / catalase positive (energy is obtained using oxygen). This indicates that there is a cytochrome-based enzyme 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.)
And from the group within 3 days of colony expression,
Two strains of morphologically different gram-negative bacilli, two strains of gram-negative bacilli having similar characteristics and morphologically different from the group having 3 to less than 5 days of colony expression, and morphologically colonized and isolated One strain was selected from a group of bacteria that accounted for about 36% of the strains, for a total of 5 strains, and they were combined with peptone 0.5.
%, Yeast extract 0.25%, glucose 0.1%, pH 7.
0 liquid medium for 7 days. Then, each culture was centrifuged to collect the cells, and the cells were weighed in an amount necessary for restoring the activated sludge to one having the same bacterial composition as the activated sludge before the pH was lowered. It was put in. In addition, the required input amount was confirmed by the percentage of each bacterium in 67 strains of bacteria initially separated from the activated sludge, the number of heterotrophic bacteria in the activated sludge (1.09 × 10 8 cell / ml), and separately confirmed. It was calculated from the obtained heterotrophic bacteria kill rate (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 introduction of the cultured strain and restarting the operation, the BOD removal rate recovered to 93%, and the number of days required for recovery was 9 days in total. On the other hand, another activated sludge tank which is expected to recover the processing capacity by simple acclimation has 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。As described above, according to the present invention, the bacteria whose number of bacteria has been reduced due to water quality fluctuations are rapidly grown in a culture device different from the activated sludge tank and then injected into the activated sludge tank. The treatment capacity of the activated sludge tank, which has been lowered, can be recovered in a much shorter number of days than before.
Claims (1)
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. Activated sludge is collected from an activated sludge tank exhibiting a good wastewater treatment capacity, a large number of bacteria involved in organic matter decomposition are separated from the collected activated sludge, and the characteristics of those bacteria are confirmed. And when the activated sludge is degraded due to water quality fluctuations of the wastewater flowing into the activated sludge tank and the wastewater treatment capacity is reduced, there is no resistance to the water quality fluctuations among the separated and preserved bacteria. Selecting a confirmed bacterium, culturing the bacterium in a complete nutrient medium, and introducing the grown cells into the activated sludge tank for acclimation; and recovering the processing capacity of the activated sludge tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09377993A JP3348904B2 (en) | 1993-03-30 | 1993-03-30 | Recovery method of activated sludge tank capacity |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP09377993A JP3348904B2 (en) | 1993-03-30 | 1993-03-30 | Recovery method of activated sludge tank capacity |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06277686A JPH06277686A (en) | 1994-10-04 |
| JP3348904B2 true JP3348904B2 (en) | 2002-11-20 |
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ID=14091912
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP09377993A Expired - Fee Related JP3348904B2 (en) | 1993-03-30 | 1993-03-30 | Recovery method of activated sludge tank capacity |
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| Country | Link |
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