JP2005319386A - Method for suppressing swelling - Google Patents

Method for suppressing swelling Download PDF

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JP2005319386A
JP2005319386A JP2004138883A JP2004138883A JP2005319386A JP 2005319386 A JP2005319386 A JP 2005319386A JP 2004138883 A JP2004138883 A JP 2004138883A JP 2004138883 A JP2004138883 A JP 2004138883A JP 2005319386 A JP2005319386 A JP 2005319386A
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activated sludge
bactericide
swelling
treatment system
microorganisms
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Takuji Yamamoto
山本琢二
Hideomi Matsuoka
松岡英臣
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Seiko PMC Corp
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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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for treating swelling in a system for an activated sludge process solving the swelling by a bactericide, complementing a decrease in process performance caused by damage to activated sludge due to the bactericide by introducing at least one or more kinds of microbes, without reducing a waste water treatment performance, and capable of swiftly and continuously suppressing the swelling. <P>SOLUTION: In the method for suppressing the swelling characterized by introducing the bactericide and at least one or more kinds of microbes to the system for the activated sludge process by leaving a space, it is preferable that the bactericide is a chlorine-based oxidation type bactericide, and further, to dose the bactericide to a sludge separation tank and/or a sludge recirculation line as a dosing place, and introduce the microbes into an aeration tank. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、糸状性細菌に由来する活性汚泥処理システムにおける膨化抑制方法に関する。 The present invention relates to a method for suppressing swelling in an activated sludge treatment system derived from filamentous bacteria.

活性汚泥処理システムとは、少なくとも活性汚泥をある濃度に保ち、空気または酸素を曝気して好気的に排水中の有機物を酸化分解する曝気槽を含むシステムであり、活性汚泥処理システムでは、主として細菌によって構成される活性汚泥によって排水中の有機物を分解している。該活性汚泥には原生動物、後生動物を含んでいる場合もある。活性汚泥処理システムには様々な方法があるが、活性汚泥の存在形態はフロックと生物膜の2種類に大別される。例えば表面曝気や散気によって空気を曝気する標準曝気法、酸素を曝気する酸素曝気法、水圧によって溶存酸素を増加せしめる深層曝気法では、活性汚泥はフロックで存在する。回転円盤法や流動担体法、接触酸化法では、活性汚泥はセラミック多孔質やハニカム、高分子ポリマー、樹脂といった担体表面に生物膜として存在する。 The activated sludge treatment system is a system including an aeration tank that keeps at least a concentration of activated sludge and aerated air or oxygen to oxidatively decompose organic matter in wastewater. In the activated sludge treatment system, Organic matter in waste water is decomposed by activated sludge composed of bacteria. The activated sludge may contain protozoa and metazoans. There are various types of activated sludge treatment systems, but the existence form of activated sludge is roughly divided into two types: floc and biofilm. For example, in the standard aeration method in which air is aerated by surface aeration and aeration, the oxygen aeration method in which oxygen is aerated, and the deep layer aeration method in which dissolved oxygen is increased by water pressure, activated sludge is present as floc. In the rotating disk method, the fluid carrier method, and the contact oxidation method, activated sludge exists as a biofilm on the carrier surface such as a ceramic porous material, honeycomb, polymer polymer, or resin.

活性汚泥の存在形態がフロックである場合には、活性汚泥処理システムは、曝気槽、汚泥分離槽、返送ラインから成る。通常、曝気槽の後に汚泥分離槽がおかれ、汚泥分離槽でフロックは重力沈降して固液分離されて、上澄は放流され、沈降したフロックは重力によって濃縮されて曝気槽へ返送ラインを通じて返送される。 When the activated sludge is present in the floc form, the activated sludge treatment system includes an aeration tank, a sludge separation tank, and a return line. Usually, a sludge separation tank is placed after the aeration tank. In the sludge separation tank, flocs are gravity settled and separated into solid and liquid, and the supernatant is discharged. Will be returned.

活性汚泥の存在形態が生物膜である場合には、ほとんど活性汚泥が流出しないために、活性汚泥を返送する目的の汚泥分離槽、返送ラインは通常設置されず、活性汚泥処理システムは、曝気槽だけから成る。 When activated sludge exists in the form of a biofilm, activated sludge hardly flows out, so the sludge separation tank and return line for returning activated sludge are not usually installed, and the activated sludge treatment system is an aeration tank. Consist only of.

糸状性細菌は、活性汚泥の堅固なフロックや生物膜の骨格を形成する重要な構造因子である。しかしながら活性汚泥処理システムにおいて排水の水質やある条件下で、糸状性細菌は異常に優勢となり、膨化を引き起こすことがある。膨化がおきると、活性汚泥の存在形態がフロックの場合、かさ密度の低下により処理水質の悪化を引き起こすことがあり、また生物膜の場合、担体の目詰まりや糸状性細菌の成長によって生物膜が剥離して処理水質を悪化させる等のトラブルが生じることがある。 Filamentous bacteria are important structural factors that form a firm floc of activated sludge and a biofilm skeleton. However, in the activated sludge treatment system, the filamentous bacteria become abnormally dominant and may cause swelling under certain water conditions and conditions. When swelling occurs, if the activated sludge is flocs, the treated water quality may be deteriorated due to a decrease in bulk density, and in the case of biofilms, the biofilms may become clogged with carriers or grow filamentous bacteria. Troubles such as exfoliation and deterioration of treated water may occur.

従来膨化の抑制方法としてノニオン性界面活性剤とアニオン性界面活性剤(例えば、特許文献1参照)、ノニオン性界面活性剤と第4アンモニウム塩のカチオン性界面活性剤を添加する方法(例えば、特許文献2参照)が提案されている。これらの方法はノニオン性界面活性剤、アニオン性界面活性剤自体がType0041、Nostocoida limicola等の糸状性細菌の増殖因子となったり、界面活性剤としての性質から使用量が多いと発泡を引き起こすことがある。
特開平11−216484号公報 特開平08−103788号公報
Conventional methods of suppressing swelling include a nonionic surfactant and an anionic surfactant (see, for example, Patent Document 1), a method of adding a nonionic surfactant and a cationic surfactant of a quaternary ammonium salt (for example, a patent) Reference 2) has been proposed. In these methods, nonionic surfactants and anionic surfactants themselves may become growth factors for filamentous bacteria such as Type0041 and Nostocoida limicola, and foaming may occur if the amount used is large due to the property as a surfactant. is there.
Japanese Patent Laid-Open No. 11-216484 Japanese Unexamined Patent Publication No. 08-103788

また、従来次亜塩素酸塩や二酸化塩素に例示される塩素系酸化型殺菌剤を用いて糸状性細菌を殺菌する方法も知られているが、塩素系酸化型殺菌剤が活性汚泥そのものにもダメージを与える為に活性汚泥処理システムの処理性能が低下する問題があった。また塩素系酸化型殺菌剤処理後に再び糸状性細菌が優勢となり膨化が生じてしまうことが多く、根本的な解決策ではない。 In addition, a method of sterilizing filamentous bacteria using a chlorine-based oxidizing fungicide exemplified by hypochlorite and chlorine dioxide is also known, but the chlorine-based oxidizing fungicide is also applied to activated sludge itself. There was a problem that the treatment performance of the activated sludge treatment system deteriorated due to damage. In addition, filamentous bacteria become dominant again after the treatment with a chlorine-based oxidizing disinfectant and often cause swelling, which is not a fundamental solution.

更に糸状性細菌に対して特異的な溶菌能を有するバチルス(Bacillus)属(例えば、特許文献3参照)、アシネトバクター(Acinetobacter)属(例えば、特許文献4参照)の特定株やその培養物のように微生物を添加する膨化抑制方法が提案されている。しかし、この様な膨化抑制方法は、活性汚泥処理システムが既に多量の優占微生物によって占められている為に、多量の微生物の添加が必要であるため莫大な費用がかかり、また添加開始から効果が現れるまでに長期間を要することが多い。
特開平06−007154号公報 特開平06−063587号公報
Furthermore, specific strains of Bacillus genus (see, for example, Patent Document 3) and Acinetobacter genus (for example, see Patent Document 4) having specific lytic ability against filamentous bacteria and cultures thereof There has been proposed a method for suppressing swelling by adding microorganisms. However, such a swelling suppression method is very expensive because the activated sludge treatment system is already occupied by a large amount of dominant microorganisms, and a large amount of microorganisms must be added. It often takes a long time to appear.
Japanese Patent Laid-Open No. 06-007154 Japanese Unexamined Patent Publication No. 06-063587

従来の膨化抑制方法である界面活性剤の添加は、溶菌作用により活性汚泥処理システムの処理水の透視度、SS濃度、生物化学的酸素消費量(BOD)、化学的酸素消費量(COD)といった管理値の悪化や発泡を引き起こす等、操業性を低下させることがあり、微生物の添加は、活性汚泥処理システムが既に多量の優占微生物によって占められている為に添加開始から効果が現れるまでに長期間、1ヶ月以上を要することがあった。また、殺菌剤の添加は、膨化を改善すると同時に活性汚泥そのものにもダメージを与えるため、活性汚泥の崩壊、活性汚泥処理システムの処理性能が低下することがあった。このため、活性汚泥処理システムの操業性を低下させず、即効性のある膨化抑制方法が求められている。   The addition of a surfactant, which is a conventional method for suppressing swelling, includes the transparency of treated water of an activated sludge treatment system, SS concentration, biochemical oxygen consumption (BOD), chemical oxygen consumption (COD) due to lysis. The operability may be reduced, such as causing deterioration of the control value and foaming, and the addition of microorganisms is effective from the start of addition because the activated sludge treatment system is already occupied by a large amount of dominant microorganisms. It may take more than one month for a long time. In addition, the addition of the disinfectant improves the expansion and at the same time damages the activated sludge itself, so that the activated sludge collapses and the treatment performance of the activated sludge treatment system may be lowered. For this reason, there is a demand for a method for suppressing swelling that is immediately effective without reducing the operability of the activated sludge treatment system.

(1)殺菌剤と少なくとも1種以上の微生物を間隔をあけて活性汚泥処理システムに添加することを特徴とする膨化抑制方法、
(2)殺菌剤が塩素系酸化型殺菌剤である前記(1)の膨化抑制方法、
(3)殺菌剤を汚泥分離槽及び/又は返送汚泥ラインに添加する前記(1)又は(2)の膨化抑制方法、
(4)少なくとも1種以上の微生物を曝気槽に添加する前記(1)〜(3)のいずれかの膨化抑制方法。
(1) A swelling suppression method characterized by adding a bactericide and at least one or more microorganisms to an activated sludge treatment system at intervals,
(2) The swelling suppression method according to the above (1), wherein the bactericide is a chlorine-based oxidized bactericide.
(3) The method for suppressing expansion of (1) or (2), wherein a disinfectant is added to the sludge separation tank and / or the return sludge line.
(4) The swelling suppression method according to any one of (1) to (3), wherein at least one type of microorganism is added to the aeration tank.

本発明の活性汚泥処理システムにおける膨化の処理方法は、殺菌剤によって膨化を解消し、殺菌剤による活性汚泥へのダメージによる処理性能の低下を、少なくとも1種以上の微生物を添加することによって補完し、排水処理能力を低下させること無く、迅速かつ継続的に膨化を抑制することが可能となる。 The expansion treatment method in the activated sludge treatment system of the present invention eliminates expansion by a disinfectant, and supplements a decrease in treatment performance due to damage to the activated sludge by the disinfectant by adding at least one microorganism. It is possible to quickly and continuously suppress expansion without reducing the wastewater treatment capacity.

本発明の殺菌剤としては、例えば塩素ガス、次亜塩素酸、次亜塩素酸塩、二酸化塩素、及びサラシ粉等の塩素系酸化型殺菌剤、過酸化水素等の過酸化物、オゾン、並びにジメチルアミンエピクロルヒドリン、及びポリジメチルアミノエチルアクリレートのメチルクロライドによる4級化物等の高分子カチオンポリマーを挙げられるが、塩素系酸化型殺菌剤が好ましく、特に次亜塩素酸塩が好ましい。殺菌剤は1種単独でも使用できるし、2種以上を組み合わせて使用することができる。 Examples of the disinfectant of the present invention include chlorine-based oxidative disinfectants such as chlorine gas, hypochlorous acid, hypochlorite, chlorine dioxide, and salash powder, peroxides such as hydrogen peroxide, ozone, and Polymeric cationic polymers such as quaternized products of dimethylamine epichlorohydrin and polydimethylaminoethyl acrylate with methyl chloride can be mentioned. Chlorine oxidation type disinfectants are preferable, and hypochlorite is particularly preferable. One type of bactericidal agent can be used alone, or two or more types can be used in combination.

本発明の殺菌剤の活性汚泥処理システムへの添加場所は、殺菌剤と微生物を間隔をあけて添加すれば活性汚泥処理システムのどの場所でもよいが、汚泥分離槽及び/又は返送汚泥ラインに添加することが好ましい。また、添加量は曝気槽混合液に対して、有効成分として0.03〜200mg/lの濃度となるように添加することが好ましい。添加の回数は連続的でも間欠的でもよく、1回/日の添加であってもよい。 The place for adding the disinfectant of the present invention to the activated sludge treatment system may be any place in the activated sludge treatment system as long as the disinfectant and the microorganism are added at intervals, but added to the sludge separation tank and / or the return sludge line. It is preferable to do. Moreover, it is preferable to add so that it may become a density | concentration of 0.03-200 mg / l as an active ingredient with respect to an aeration tank liquid mixture. The number of additions may be continuous or intermittent, and may be once / day.

本発明における微生物としては、細菌、細菌の芽胞、細菌の休眠子、カビ、酵母、原生動物等どのような微生物でも使用することができる。この中でもバチルス(Bacillus)属、シュードモナス(Pseudomonas)属の微生物を使用することが好ましい。また、これら微生物は2種以上を混合しているものが好ましく、微生物の培養物をそのまま用いてもよい。これらの微生物の中でも、増殖速度が速く、酵素を多量に生産し、排水水質に適合した微生物を含んでいることが好ましく、このような微生物として星光PMC株式会社が販売する微生物製剤MC−002,MC−003、MC−004、MC−005、MC−006、MC−008、MC−038等を挙げることができる。これらの微生物は、粉体のまま直接活性汚泥処理システムに使用する事もできるが、バッチ式または連続式の培養タンクで培養し、微生物群が分泌した酵素や多糖類、微生物を含む培養物として活性汚泥処理システムに使用することもできる。 As the microorganism in the present invention, any microorganisms such as bacteria, bacterial spores, bacterial diapauses, molds, yeasts, protozoa and the like can be used. Among these, it is preferable to use microorganisms belonging to the genus Bacillus and Pseudomonas. These microorganisms are preferably those in which two or more kinds are mixed, and the culture of the microorganisms may be used as it is. Among these microorganisms, it is preferable that the microorganisms have a high growth rate, produce a large amount of enzyme, and contain microorganisms suitable for the quality of wastewater. Microbial preparation MC-002 sold by Seiko PMC Co., Ltd. as such microorganisms. MC-003, MC-004, MC-005, MC-006, MC-008, MC-038, etc. can be mentioned. These microorganisms can be used directly in the activated sludge treatment system in powder form, but they are cultured in a batch or continuous culture tank, and as a culture containing enzymes, polysaccharides, and microorganisms secreted by the microorganism group. It can also be used in an activated sludge treatment system.

本発明における微生物の活性汚泥処理システムへの添加場所は、殺菌剤と微生物を間隔をあけて添加すれば活性汚泥処理システムのどの場所でもよいが、微生物を曝気槽に添加することが好ましく、活性汚泥乾燥重量1に対して、培養菌体又は培養物重量として0.005〜2.0となるように添加することが好ましい。添加の回数は連続的でも間欠的でもよく、1回/日の添加であってもよい。 The place for adding microorganisms to the activated sludge treatment system in the present invention may be any place in the activated sludge treatment system as long as a disinfectant and microorganisms are added at intervals, but it is preferable to add microorganisms to the aeration tank. It is preferable to add to the sludge dry weight 1 so that the cultured cell or culture weight is 0.005 to 2.0. The number of additions may be continuous or intermittent, and may be once / day.

本発明で殺菌剤と微生物を間隔をあけて添加するとは、殺菌剤と微生物の添加を同時に行わないで順次これらのいずれかを最初に添加し次いで他方を添加することをいい、汚泥分離槽で殺菌剤を添加し、曝気槽で微生物を添加するように十分な間隔をあけることが好ましい。 In the present invention, adding a disinfectant and microorganisms at intervals means that one of these is added first without adding the disinfectant and microorganisms at the same time, and then the other is added. It is preferable to add a disinfectant and leave a sufficient interval so as to add microorganisms in the aeration tank.

実施例
Thiothrix、Nostocoida limicolaによる膨化が生じている活性汚泥処理システムにおいて試験を実施した。殺菌剤として次亜塩素酸ナトリウムを有効塩素量として返送汚泥ラインに13mg/L添加し、活性汚泥処理システム内に残留塩素が検出されない程度に十分に添加間隔をあけて、星光PMC株式会社の微生物製剤MC−003の培養物を曝気槽に活性汚泥乾燥重量1に対して0.9を添加した。本実施例前の1ヶ月間の平均値(以下、「試験前」と略する)、本実施例後の1ヶ月間の平均値(以下、「試験中」と略する)における容積負荷、糸状性細菌レベル、COD低減率を表2に示す。なお、容積負荷は、曝気槽入り口のCOD濃度に1日に曝気槽に入る流量を乗じたものを、曝気槽容積で除して算出した。活性汚泥の糸状性細菌レベルの判定については、ジェンキンズ(Jenkins)法によって表1のように行った。糸状性細菌レベル4〜6は膨化によって活性汚泥フロックの沈降性が悪いことを示しており、糸状性細菌レベル3であれば問題なく操業できることを示している。COD低減率は、活性汚泥処理システムに入る前の時点のCOD値から最終的な排水時のCOD値の差を活性汚泥処理システムに入る前の時点のCOD値で割ったものを%表示したものである。COD値は過マンガン酸法によって測定した。
Example Tests were carried out in an activated sludge treatment system in which expansion by Thiothrix, Nostocoida limicola has occurred. Sodium hypochlorite as an effective chlorine amount as a disinfectant was added to the return sludge line at 13 mg / L, and a sufficient interval was added so that residual chlorine was not detected in the activated sludge treatment system. The culture of formulation MC-003 was added to the aeration tank at 0.9 to 1 activated sludge dry weight. Volume load, filament shape in the average value for one month before this example (hereinafter abbreviated as “before test”), average value for one month after this example (hereinafter abbreviated as “under test”) Table 2 shows the bacterial level and COD reduction rate. The volumetric load was calculated by multiplying the COD concentration at the inlet of the aeration tank by the flow rate entering the aeration tank for one day and dividing it by the aeration tank volume. The determination of the level of filamentous bacteria in the activated sludge was performed as shown in Table 1 by the Jenkins method. Filamentous bacteria levels 4 to 6 indicate that the activated sludge flocs have poor sedimentation due to swelling, and that filamentous bacteria level 3 can be operated without problems. The COD reduction rate is expressed as a percentage obtained by dividing the difference between the COD value at the time of final drainage from the COD value at the time before entering the activated sludge treatment system by the COD value at the time before entering the activated sludge treatment system. It is. The COD value was measured by the permanganic acid method.

Figure 2005319386
Figure 2005319386

Figure 2005319386
Figure 2005319386

試験前、試験中のデータを比較すると、試験中は容積負荷が増えているにもかかわらず活性汚泥処理システムの処理性能の低下は起こらず、次亜塩素酸ナトリウムの添加を開始してからすぐに膨化の指標となる糸状性細菌レベルの低下傾向が認められ、添加開始から2日後に糸状性細菌レベル4に低下した。添加開始から4日後に糸状性細菌レベルは沈降性に影響を与えないレベル3にまで低下し、膨化は解消された。試験後、微生物製剤MC−003の培養液の添加は継続し1ヶ月にわたって膨化は認められず、活性汚泥処理システムの処理性能は安定していた。 Comparing the data before and during the test, the activated sludge treatment system does not deteriorate in performance even though the volume load is increased during the test, and immediately after the start of the addition of sodium hypochlorite The tendency of the decrease in the level of filamentous bacteria as an index of swelling was observed, and the level decreased to the level of filamentous bacteria 2 days after the start of the addition. Four days after the start of the addition, the level of filamentous bacteria was lowered to level 3 which did not affect the sedimentation property, and swelling was eliminated. After the test, the addition of the culture solution of the microorganism preparation MC-003 was continued, and no swelling was observed over one month, and the treatment performance of the activated sludge treatment system was stable.

Claims (4)

殺菌剤と少なくとも1種以上の微生物を間隔をあけて活性汚泥処理システムに添加することを特徴とする膨化抑制方法。 A method for suppressing swelling, comprising adding a disinfectant and at least one microorganism to the activated sludge treatment system at intervals. 殺菌剤が塩素系酸化型殺菌剤であることを特徴とする請求項1に記載の膨化抑制方法。 The method according to claim 1, wherein the bactericide is a chlorine-based oxidized bactericide. 殺菌剤を汚泥分離槽及び/又は返送汚泥ラインに添加することを特徴とする請求項1又は2に記載の膨化抑制方法。 The method according to claim 1 or 2, wherein a disinfectant is added to the sludge separation tank and / or the return sludge line. 少なくとも1種以上の微生物を曝気槽に添加することを特徴とする請求項1〜3のいずれかに記載の膨化抑制方法。 The expansion method according to any one of claims 1 to 3, wherein at least one kind of microorganism is added to the aeration tank.
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