JP4375265B2 - Microbial acclimatization method and organic wastewater treatment method with acclimatized microorganisms - Google Patents

Microbial acclimatization method and organic wastewater treatment method with acclimatized microorganisms Download PDF

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JP4375265B2
JP4375265B2 JP2005088092A JP2005088092A JP4375265B2 JP 4375265 B2 JP4375265 B2 JP 4375265B2 JP 2005088092 A JP2005088092 A JP 2005088092A JP 2005088092 A JP2005088092 A JP 2005088092A JP 4375265 B2 JP4375265 B2 JP 4375265B2
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正廣 青井
洋介 中村
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Sumitomo Chemical Co Ltd
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    • 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
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Description

本発明は、有機性排水の生物学的処理における微生物の馴養方法および馴養した微生物による有機性排水の処理方法に関するものである。   The present invention relates to a method for acclimatizing microorganisms in biological treatment of organic wastewater, and a method for treating organic wastewater with acclimatized microorganisms.

下水、し尿等の生活系排水や、食品加工工場、化学工業等の製造プロセスから排出される有機物を含有する排水の処理方法が種々提案されている。その中で最も汎用的な方法としては活性汚泥法が挙げられる。活性汚泥法は、好気性微生物である汚泥が浮遊する生物処理槽内に、有機物を含有した排水を供給し、空気で曝気することにより、浮遊汚泥を構成する微生物により排水中の有機物を酸化分解する方法である。   Various treatment methods for domestic wastewater such as sewage and human waste, and wastewater containing organic matter discharged from manufacturing processes such as food processing factories and chemical industries have been proposed. Among them, the activated sludge method is mentioned as the most versatile method. In the activated sludge method, wastewater containing organic matter is supplied to a biological treatment tank where sludge, which is an aerobic microorganism, floats, and aerated with air, so that the organic matter in the wastewater is oxidatively decomposed by microorganisms that constitute the suspended sludge. It is a method to do.

かかる微生物とは一般に25〜37℃を好適な生育温度とするものが多く存在している。微生物の活性は水温が10℃上昇すると、処理活性は約2倍高くなることから、排水中に含有する有機物を生物学的に処理する方法において、微生物の活性からみれば水温を高く設定する方が有利である。しかしながら水温が40℃を超えると微生物を構成しているタンパクの変性や酵素の失活により活性が著しく低下し、処理水水質を悪化させてしまうため、一般に生物処理施設では処理水温度を40℃以下に保持して運転されている(非特許文献1参照。)。   Many such microorganisms generally have a suitable growth temperature of 25 to 37 ° C. When the water temperature rises by 10 ° C, the activity of microorganisms increases about twice as high, so in the method of biologically treating organic matter contained in wastewater, the water temperature should be set higher from the viewpoint of the activity of microorganisms. Is advantageous. However, when the water temperature exceeds 40 ° C., the activity of the protein is significantly reduced due to the denaturation of the proteins constituting the microorganisms and the inactivation of the enzyme, and the quality of the treated water is deteriorated. The following operation is performed (see Non-Patent Document 1).

近年においては地球規模の温暖化現象の影響で気温が上昇し、とりわけ夏季において活性汚泥施設の処理水温度が上昇したり、また食品加工工場や化学工場等では、日常的に高水温の排水が排出されたりする場合が多々あり、このような高温度の排水が流入することによって生物処理槽内の温度が著しく上昇、時として処理水温度が40℃を超え、処理水水質を著しく悪化させることがある。かかる問題に対し、一般的には活性汚泥槽に大量の冷却水を注水して処理水温度を下げるといった方法や、流入排水を40℃以下にまで冷却して生物処理槽に供給する方法が開示されている(例えば、特許文献1参照。)。   In recent years, the temperature has risen due to the global warming phenomenon, and the temperature of the treated sludge facility has increased, especially in the summer. The temperature in the biological treatment tank rises remarkably due to the inflow of such high temperature waste water, sometimes the treatment water temperature exceeds 40 ° C, and the quality of the treatment water is remarkably deteriorated. There is. In general, a method of pouring a large amount of cooling water into an activated sludge tank to lower the temperature of the treated water and a method of cooling the influent wastewater to 40 ° C. or lower and supplying it to the biological treatment tank are disclosed. (For example, refer to Patent Document 1).

また、溶解性の有機物を含有する排水の好気的な生物処理方法において、生物処理槽内の温度を45℃以上に維持する方法が開示されている(特許文献2参照。)。   Moreover, the method of maintaining the temperature in a biological treatment tank at 45 degreeC or more is disclosed in the aerobic biological treatment method of the waste_water | drain containing a soluble organic substance (refer patent document 2).

しかしながら、前記方法では、大量の冷却水を注水するために処理槽が大型化するとか、流入排水若しくは生物処理槽内の処理液を冷却若しくは加熱するための費用も高くなるという問題がある。
排水温度の上昇や気温の上昇によって生物処理槽内の処理液が、一般には微生物の生育には好ましくないとされている40℃を超え45℃未満になっても、設備や運転費用をあまり掛けずに、有機性排水を効率的に処理することができる方法が望まれている。
「活性汚泥法と維持管理」第5版、株式会社産業用水調査会、平成6年5月24日、p59,p227 特開平8−155475号公報 特開2004−268023号公報
However, the above-described method has a problem that the treatment tank becomes large in order to inject a large amount of cooling water, and the cost for cooling or heating the treatment liquid in the inflow waste water or the biological treatment tank is high.
Even if the treatment liquid in the biological treatment tank exceeds 40 ° C and lower than 45 ° C, which is generally considered unfavorable for the growth of microorganisms, due to the rise in drainage temperature and temperature, it takes much equipment and operating costs. Therefore, a method capable of efficiently treating organic wastewater is desired.
“Activated sludge method and maintenance management” 5th edition, Industrial Water Research Committee, May 24, 1994, p59, p227 JP-A-8-155475 JP 2004-268023 A

本発明の目的は、一般には微生物の生育には好ましくないとされている40℃を超え45℃未満になっても、設備や運転費用をあまり掛けずに、有機性排水を効率的に処理することができる微生物の馴養方法および馴養した微生物による有機性排水の処理方法を提供する。   The object of the present invention is to efficiently treat organic wastewater without much equipment and operating costs even if it exceeds 40 ° C and lower than 45 ° C, which is generally considered undesirable for the growth of microorganisms. Provided are a method for acclimatizing microorganisms and a method for treating organic wastewater by the acclimatized microorganisms.

そこで本発明者は、かかる状況に鑑み、微生物の生育には好ましくないとされている温度環境においても、排水中に含有する有機物を微生物により効率的に分解処理する方法について鋭意検討した結果、微生物を40℃以下の温度環境と40℃を超え45℃未満の温度環境に順次繰り返して晒して馴養した微生物とし、次いで生物処理槽内の温度を40℃を超え45℃未満に保持することによって、40〜45℃の温度環境の排水中に含有する有機物を効率的に分解処理できることを見出し、本発明に至った。   Therefore, in view of such circumstances, the present inventor has conducted intensive studies on a method for efficiently decomposing organic matter contained in wastewater by microorganisms even in a temperature environment that is considered undesirable for the growth of microorganisms. By gradually exposing to a temperature environment of 40 ° C. or less and a temperature environment of more than 40 ° C. and less than 45 ° C., and then maintaining the temperature in the biological treatment tank above 40 ° C. and less than 45 ° C. The present inventors have found that organic substances contained in waste water having a temperature environment of 40 to 45 ° C. can be efficiently decomposed, and have led to the present invention.

すなわち本発明は、排水中に含有する有機物を好気的に分解処理する際に使用する微生物を、40℃以下の温度環境と40℃を超え45℃未満の温度環境に順次繰り返して晒すことを特徴とする微生物の馴養方法である。
また、排水中に含有する有機物を微生物により好気的に分解処理するに際し、微生物を40℃以下の温度環境と40℃を超え45℃未満の温度環境に順次繰り返して晒して馴養した微生物とし、次いで生物処理槽内の温度を40℃を超え45℃未満に保持することを特徴とする有機性排水の処理方法である。
That is, the present invention is to repeatedly expose microorganisms used when aerobically decomposing organic substances contained in wastewater to a temperature environment of 40 ° C. or less and a temperature environment of more than 40 ° C. and less than 45 ° C. It is a characteristic method of acclimatizing microorganisms.
In addition, when the organic matter contained in the wastewater is aerobically decomposed by microorganisms, the microorganisms are subjected to repeated exposure to a temperature environment of 40 ° C. or less and a temperature environment of more than 40 ° C. and less than 45 ° C. Next, the organic waste water treatment method is characterized in that the temperature in the biological treatment tank is maintained at a temperature higher than 40 ° C. and lower than 45 ° C.

本発明方法によれば、微生物の生育には好ましくないとされている40〜45℃の温度環境においても、排水中に含有する有機物を効率的に処理することができる微生物を得ることができ、またこの微生物を使用して、40〜45℃の温度環境において排水中に含有する有機物を効率的に処理することができる。   According to the method of the present invention, even in a temperature environment of 40 to 45 ° C., which is considered unfavorable for the growth of microorganisms, microorganisms capable of efficiently treating organic substances contained in wastewater can be obtained, Moreover, the organic substance contained in waste_water | drain can be efficiently processed using this microorganism in the temperature environment of 40-45 degreeC.

以下、本発明を詳細に説明する。
本発明における有機性排水としては、有機物を含有する排水であって、下水、し尿等の生活系排水や食品加工工場や化学工業等の特定の有機物を含有する排水等が挙げられる。かかる有機性排水中に含有する有機物の種類は特に限定しないが、一般には炭水化物、糖類、有機酸等の易分解性の有機物が挙げられる。
Hereinafter, the present invention will be described in detail.
Examples of the organic waste water in the present invention include waste water containing organic matter, such as domestic waste water such as sewage and human waste, waste water containing specific organic matter such as food processing factory and chemical industry. Although the kind of organic substance contained in this organic waste water is not specifically limited, Generally, easily decomposable organic substances such as carbohydrates, sugars, and organic acids are exemplified.

本発明方法で使用される微生物は、排水中の有機物を好気的に分解せしめる微生物であれば特に限定されるものではなく、一般的な活性汚泥施設で用いられている微生物である。
この微生物は、上記したとおり、水温が40℃を超えると微生物を構成しているタンパクの変性や酵素の失活により処理活性が著しく低下する。
微生物の生育には好ましくないとされている40℃を超え45℃未満という温度環境(以下、中高温環境と称す。)でも、排水中の有機物を効率的に分解処理するためには、微生物を中高温環境に順応させる必要がある。
The microorganism used in the method of the present invention is not particularly limited as long as it is a microorganism that aerobically decomposes organic matter in wastewater, and is a microorganism used in a general activated sludge facility.
As described above, when the water temperature exceeds 40 ° C., the treatment activity of this microorganism is significantly reduced due to the denaturation of the protein constituting the microorganism and the deactivation of the enzyme.
In order to efficiently decompose organic matter in wastewater, the microorganism must be used even in a temperature environment exceeding 40 ° C. and less than 45 ° C., which is considered undesirable for the growth of microorganisms. It is necessary to adapt to medium and high temperature environment.

微生物を中高温環境に順応させる微生物の馴養方法としては、一般には微生物が生育するのに好適な温度環境から徐々に目標とする中高温環境まで上昇させる方法が用いられる。
しかしながら、微生物の好適環境から徐々に昇温して行くと、40℃を超える温度領域に到達したときに、微生物が新しい環境にうまく適応できずに処理活性が低下し、一時的に処理水水質が悪化する。悪化した処理水水質は次第に微生物が中高温環境に適応するにともなって処理活性が向上し、処理水水質が回復してくるが、処理活性の変動が大きく、必ずしも満足できる方法とは言えない。
As a method of acclimatizing microorganisms to adapt microorganisms to medium-high temperature environments, generally, a method of gradually raising the temperature from a temperature environment suitable for growing microorganisms to a target medium-high temperature environment is used.
However, if the temperature is gradually raised from a suitable environment of microorganisms, when the temperature reaches a temperature exceeding 40 ° C., the microorganisms cannot adapt well to the new environment and the treatment activity decreases, and the quality of the treated water temporarily Gets worse. The deteriorated treated water quality gradually improves as the microorganisms adapt to the medium and high temperature environment, and the treated water quality is recovered. However, the treatment activity varies greatly and is not always a satisfactory method.

微生物の馴養過程において、微生物の処理活性が低下し、処理水水質が悪化したとしても、該活性汚泥施設の排水規制値以下の処理水水質であれば、そのまま放流してもよいが、規制値を超える処理水水質であれば、該処理水を一時的に貯留槽に溜めておき、微生物が前記温度環境に順応した後、一時貯留した処理水を生物処理槽に通水し、再処理をして放流することもできる。しかしながら、十分な大きさの貯留槽の設置は、費用または敷地上の制約があって困難なことが多く、また有機性排水の処理能力に余力がない場合にも、この方法では十分に対応ができない。   Even if the treatment activity of microorganisms decreases and the quality of treated water deteriorates in the acclimatization process of microorganisms, if the treated water quality is lower than the wastewater regulation value of the activated sludge facility, it may be discharged as it is. If the quality of the treated water exceeds 50 ° C., the treated water is temporarily stored in a storage tank, and after the microorganisms have adapted to the temperature environment, the temporarily stored treated water is passed through the biological treatment tank for reprocessing. It can also be released. However, it is often difficult to install a sufficiently large storage tank due to cost or site constraints, and this method is sufficient even when there is not enough capacity for organic wastewater treatment. Can not.

本発明においては、微生物を、40℃以下の温度環境(以下、中温環境と称す。)と中高温環境に順次繰り返して晒して馴養する。
このようにして馴養された微生物を使用し、生物処理槽内を中高温環境に保持することによって有機性排水を効率的に処理することができる。
中温環境と中高温環境の温度差は特に限定されないが、温度差を大きくするほど中高温環境に晒したときの微生物の処理活性が低下しやすくなる傾向があり、通常、約10℃以下が好ましい。
In the present invention, microorganisms are acclimatized by repeatedly exposing them to a temperature environment of 40 ° C. or lower (hereinafter referred to as an intermediate temperature environment) and an intermediate temperature environment.
Organic wastewater can be treated efficiently by using microorganisms acclimatized in this manner and maintaining the inside of the biological treatment tank in a medium-high temperature environment.
The temperature difference between the medium temperature environment and the medium temperature environment is not particularly limited, but as the temperature difference is increased, the treatment activity of the microorganisms when exposed to the medium temperature environment tends to decrease, and usually about 10 ° C. or less is preferable. .

生物処理槽を前記中温環境から中高温環境にするための加温方法は特に制限されないが、通常、流入排水または生物処理槽内にスチームを吹き込んで直接加熱する方法、および流入排水および/または生物処理槽内処理水を熱交換器などにより間接的に加熱する方法が挙げられる。
また、中高温環境から中温環境にするための冷却方法も特に制限されないが、地下水などを生物処理槽に供給する方法、および流入排水および/または生物処理槽内処理水を熱交換器などで間接的に冷却する方法が挙げられる。さらに昼夜間の気温の変化を利用して生物処理槽内の温度を制御する方法はエネルギー的にも有利であり特に好ましく用いられる。
The heating method for changing the biological treatment tank from the medium temperature environment to the medium high temperature environment is not particularly limited. Usually, steam is blown directly into the inflow wastewater or the biological treatment tank, and the inflow wastewater and / or the organism. A method of indirectly heating the treated water in the treatment tank with a heat exchanger or the like can be mentioned.
In addition, the cooling method for changing from a medium to high temperature environment to a medium temperature environment is not particularly limited, but a method of supplying groundwater to a biological treatment tank and indirect wastewater and / or treated water in the biological treatment tank with a heat exchanger or the like. The method of cooling automatically is mentioned. Furthermore, the method of controlling the temperature in the biological treatment tank using the change in the temperature of daytime and nighttime is advantageous in terms of energy and is particularly preferably used.

中温環境または中高温環境に保持する時間は特に限定されないが、通常、1分から3日間、好ましくは1〜24時間の範囲である。中高温環境に保持する時間が1分未満では、微生物の中高温環境への馴養効果が得られ難く、また3日以上では微生物の処理活性が低下する可能性がある。また、中温環境に保持する時間が3日間以上では、微生物の中高温環境への馴養効果が得られ難く、また1分以下では微生物の処理活性が低下する可能性がある。   The time for maintaining in the medium temperature environment or medium temperature environment is not particularly limited, but is usually in the range of 1 minute to 3 days, preferably 1 to 24 hours. If the time for maintaining in the medium and high temperature environment is less than 1 minute, it is difficult to obtain the acclimatization effect to the medium and high temperature environment of the microorganism, and if it is more than 3 days, the treatment activity of the microorganism may be reduced. In addition, if the time for maintaining in the medium temperature environment is 3 days or more, it is difficult to obtain the acclimatization effect to the medium temperature environment of the microorganism, and if it is 1 minute or less, the treatment activity of the microorganism may be reduced.

中温環境と中高温環境の繰り返し回数も特に制限なく、それぞれの温度環境に保持する時間によっても異なるが、通常、1〜30回、好ましくは1〜10回の範囲である。   The number of repetitions of the medium temperature environment and the medium temperature environment is also not particularly limited, and is usually in the range of 1 to 30 times, preferably 1 to 10 times, although it varies depending on the time of holding in each temperature environment.

微生物を中温環境と中高温度環境に、順次繰り返し晒すことにより、微生物の処理活性を低下させることなく微生物を馴養することができる理由は定かではないが、以下のとおりと考えられる。微生物は種々の微生物の集合体であり、中温環境に耐性を有する微生物(以下、中温菌と称する。)と中高温環境に耐性を有する微生物(以下、中高温菌と称する。)とは共生しており、中温環境においては中温菌が優占化し、中高温環境では中高温菌が優占化する。中温菌は中高温環境に晒されても短時間であれば耐性を持っていることから、短期間中高温環境に晒し、速やかに中温環境に戻すことによって、中温菌はあまり死滅若しくは衰退することなく、維持される。一方、ごく短時間でも中高温環境に晒すことによって、中高温菌が増殖若しくは活性化してくる。中温環境と中高温度環境とを順次繰り返すことによって、あまり処理活性を変動させることなく、次第に中高温菌が優占化してくる。   Although it is not clear why microorganisms can be acclimatized without decreasing the treatment activity of microorganisms by sequentially exposing the microorganisms to an intermediate temperature environment and an intermediate high temperature environment, it is considered as follows. A microorganism is an aggregate of various microorganisms, and a microorganism having resistance to a medium temperature environment (hereinafter referred to as “medium temperature bacteria”) and a microorganism having resistance to a medium temperature environment (hereinafter referred to as “medium temperature bacteria”) coexist. In the middle temperature environment, mesophilic bacteria dominate, and in the middle temperature environment, mesophilic bacteria dominate. Since mesophilic bacteria are resistant to medium-high temperature environments for a short period of time, exposure to high-temperature environments for a short period of time and quick return to medium-temperature environments can cause mesophilic bacteria to die or decline much. Not maintained. On the other hand, when exposed to a medium-high temperature environment for a very short time, medium-high temperature bacteria grow or become activated. By repeating the medium temperature environment and the medium and high temperature environment sequentially, the medium and high temperature bacteria gradually become dominant without significantly changing the treatment activity.

微生物を馴養する際の通水方法としては、有機性排水を断続的に通水する回分法、および有機性排水を連続的に通水する連続法が挙げられる。   Examples of the water passing method when acclimatizing microorganisms include a batch method in which organic waste water is passed intermittently and a continuous method in which organic waste water is passed continuously.

有機性排水を処理する際の方法としても、生物処理槽内温度を中高温環境に保持し、有機性排水を断続的に通水して生物学的に処理する回分法、および有機性排水を連続的に通水しながら生物学的に処理する連続法が挙げられる。また、生物処理槽内温度を中温環境と中高温環境を順次繰り返し変動させながら生物学的に処理する方法でもよい。   As a method for treating organic wastewater, a batch method in which the temperature in the biological treatment tank is maintained in a medium to high temperature environment, the organic wastewater is intermittently passed and biologically treated, and the organic wastewater is treated. A continuous method of biological treatment while continuously passing water is mentioned. Alternatively, a biological treatment method may be used in which the temperature in the biological treatment tank is repeatedly changed between an intermediate temperature environment and an intermediate temperature environment in order.

なお微生物の馴養および/または有機性排水の処理期間中において、生物処理槽内のpHは使用する微生物の生育可能な範囲であれば特に制限されないが、通常、6〜10範囲、好ましくは6〜9範囲である。生物処理槽内処理水が前記pH範囲を超えるようであれば、適宜アルカリまたは酸を添加し、前記pH範囲内にする。アルカリとしては、水酸化ナトリウム、炭酸ナトリウム等が挙げられる。酸としては、硫酸等が挙げられる。   In addition, during the acclimatization of microorganisms and / or the treatment period of organic wastewater, the pH in the biological treatment tank is not particularly limited as long as the microorganisms to be used can grow, but is usually in the range of 6 to 10, preferably 6 to 6. Nine ranges. If the treated water in the biological treatment tank exceeds the pH range, an alkali or acid is added as appropriate to bring the pH within the pH range. Examples of the alkali include sodium hydroxide and sodium carbonate. Examples of the acid include sulfuric acid.

以下、実施例によって本発明をより詳細に説明するが、本発明は、かかる実施例によって限定されるものではない。   EXAMPLES Hereinafter, although an Example demonstrates this invention in detail, this invention is not limited by this Example.

比較例1
使用した処理装置の模式図を図1に示す。曝気槽1の内部に仕切板5が設けれ、上部から空気供給管3が曝気槽の底部に挿入されている。上部から排水Aが排水導入管2から活性汚泥を収容した曝気槽1に導入され、空気供給管3から空気Bが供給され、好気処理部11を循環しながら処理され、固液分離部12で活性汚泥を沈降分離し、処理水Cが処理水排出管4から排出される。
内容積1Lの曝気槽に化学工場の活性汚泥[MLSS濃度6700mg/L]を投入した。次いで空気を0.5L/分の条件で供給しながら、酢酸1.32g/L、硫酸アンモニウム1.29g/L、炭酸ナトリウム1.25g/L、リン酸0.11g/L、および塩化カルシウム(2水塩)0.70g/Lを含有する合成排水を4ml/分の条件で導入した。
曝気槽内温度を約32℃に保持して3日間処理を行った後、3〜7日毎に1〜2℃毎昇温しつつ微生物の馴養を行った。
なお、馴養期間中、適宜汚泥を抜出しMLSS濃度を約6000〜10000mg/L範囲に調整した。
馴養期間中、合成排水と処理液のTOC(全有機炭素)濃度を測定し、TOC除去率を求めた。結果を図2に示した。
処理水が40℃を超える温度環境に到達した時に、TOC除去率の低下が観察されたが、その後回復したが、変動が大きい。
Comparative Example 1
A schematic diagram of the processing apparatus used is shown in FIG. A partition plate 5 is provided inside the aeration tank 1, and an air supply pipe 3 is inserted into the bottom of the aeration tank from the top. Waste water A is introduced from the top into the aeration tank 1 containing activated sludge from the waste water introduction pipe 2, supplied with air B from the air supply pipe 3, processed while circulating through the aerobic treatment section 11, and the solid-liquid separation section 12. Then, activated sludge is settled and separated, and the treated water C is discharged from the treated water discharge pipe 4.
Activated sludge [MLSS concentration 6700 mg / L] from a chemical factory was put into an aeration tank with an internal volume of 1 L. Then, while supplying air at 0.5 L / min, acetic acid 1.32 g / L, ammonium sulfate 1.29 g / L, sodium carbonate 1.25 g / L, phosphoric acid 0.11 g / L, and calcium chloride (2 Water salt) Synthetic waste water containing 0.70 g / L was introduced under the condition of 4 ml / min.
After carrying out the treatment for 3 days while maintaining the temperature in the aeration tank at about 32 ° C., the microorganisms were habituated while increasing the temperature every 1-2 ° C. every 3-7 days.
During the acclimatization period, the sludge was appropriately extracted and the MLSS concentration was adjusted to a range of about 6000 to 10000 mg / L.
During the acclimatization period, the TOC (total organic carbon) concentration of the synthetic waste water and the treatment liquid was measured to determine the TOC removal rate. The results are shown in FIG.
When the treated water reached a temperature environment exceeding 40 ° C., a decrease in the TOC removal rate was observed, but it recovered thereafter, but the fluctuation is large.

実施例1
比較例1で用いたのと同様の曝気槽を用い、化学工場の活性汚泥を投入し、比較例1と同様に空気を供給しながら合成排水を導入した。
微生物の馴養は、図3に示すように中温環境と中高温環境を約24時間毎に7回繰り返し、その後中高温環境に保持した。TOC除去率を図3に示した。
微生物を、初めに中高温環境に晒した時に、一時的にTOC除去率が若干低下したが、直ちに回復した。その後の馴養期間中および処理期間中においては、TOC除去率は常に高いレベルで、変動も小さく推移した。
Example 1
The same aeration tank as used in Comparative Example 1 was used, activated sludge from a chemical factory was introduced, and synthetic wastewater was introduced while supplying air in the same manner as Comparative Example 1.
For acclimatization of microorganisms, as shown in FIG. 3, the medium temperature environment and the medium temperature environment were repeated seven times about every 24 hours, and then maintained in the medium temperature environment. The TOC removal rate is shown in FIG.
When the microorganisms were first exposed to a medium to high temperature environment, the TOC removal rate decreased slightly but recovered immediately. During the subsequent acclimatization period and treatment period, the TOC removal rate was always at a high level, and the fluctuation was small.

実施例2
比較例1で用いたのと同様の曝気槽を用い、化学工場の活性汚泥を投入し、比較例1と同様に空気を供給しながら合成排水を導入した。
微生物の馴養は、図4に示すように中温環境の保持時間を約16〜14時間、中高温環境の保持時間を約8〜10時間として3回繰り返した後、順次中高温環境の保持時間を延長、かつ中温環境の保持時間を短縮して行き、その後中高温環境に保持した。TOC除去率を図4に示した。
微生物の馴養期間中および処理期間中において、TOC除去率は常に高いレベルで、変動も小さく推移した。
Example 2
The same aeration tank as used in Comparative Example 1 was used, activated sludge from a chemical factory was introduced, and synthetic wastewater was introduced while supplying air in the same manner as Comparative Example 1.
As shown in FIG. 4, the acclimatization of microorganisms is repeated three times with a medium temperature environment holding time of about 16 to 14 hours and a medium temperature environment temperature holding time of about 8 to 10 hours. We extended and shortened the holding time of the medium temperature environment, and then maintained the medium temperature environment. The TOC removal rate is shown in FIG.
During the acclimation period and the treatment period of the microorganism, the TOC removal rate was always at a high level, and the fluctuation was small.

実施例で使用した処理装置の模式図である。It is a schematic diagram of the processing apparatus used in the Example. 比較例1の結果を示す図である。It is a figure which shows the result of the comparative example 1. 実施例1の結果を示す図である。It is a figure which shows the result of Example 1. 実施例2の結果を示す図である。It is a figure which shows the result of Example 2.

符号の説明Explanation of symbols

1 曝気槽
2 排水導入管
3 空気供給管
4 処理水排出管
5 仕切板
11 好気処理部
12 固液分離部
A 排水
B 空気
C 処理水


1 Aeration tank
2 Drainage introduction pipe 3 Air supply pipe 4 Treated water discharge pipe 5 Partition plate
11 Aerobic processing department
12 Solid-liquid separation part A Wastewater B Air C Treated water


Claims (4)

排水中に含有する有機物を好気的に分解処理する際に使用する微生物を、40℃以下の温度環境と40℃を超え45℃未満の温度環境に順次繰り返して晒すことを特徴とする微生物の馴養方法。   Microorganisms used for aerobically decomposing organic substances contained in wastewater are repeatedly exposed to a temperature environment of 40 ° C. or less and a temperature environment of more than 40 ° C. and less than 45 ° C. How to acclimatize. 40℃以下の温度環境および40℃を超え45℃未満の温度環境に晒す時間が、それぞれ1分から3日間で、繰り返す回数が1〜30回である請求項1記載の微生物の馴養方法。   The method for acclimatizing a microorganism according to claim 1, wherein the time of exposure to a temperature environment of 40 ° C or less and a temperature environment exceeding 40 ° C and less than 45 ° C is 1 minute to 3 days, respectively, and the number of repetitions is 1 to 30 times. 排水中に含有する有機物を微生物により好気的に分解処理するに際し、微生物を40℃以下の温度環境と40℃を超え45℃未満の温度環境に順次繰り返して晒して馴養した微生物とし、次いで生物処理槽内の温度を40℃を超え45℃未満に保持することを特徴とする有機性排水の処理方法。   When organic matter contained in wastewater is aerobically decomposed by microorganisms, microorganisms are subjected to repeated exposure to a temperature environment of 40 ° C. or less and a temperature environment of more than 40 ° C. and less than 45 ° C. A method for treating organic wastewater, characterized in that the temperature in the treatment tank is kept above 40 ° C and below 45 ° C. 40℃以下の温度環境および40℃を超え45℃未満の温度環境に晒す時間が、それぞれ1分から3日間で、繰り返す回数が1〜30回である請求項3記載の有機性排水の処理方法。 The method for treating organic waste water according to claim 3, wherein the time of exposure to a temperature environment of 40 ° C or less and a temperature environment exceeding 40 ° C and less than 45 ° C is 1 minute to 3 days, respectively, and the number of repetitions is 1 to 30 times.
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