JPH0671287A - Bulking canceling agent for activated sludge - Google Patents

Bulking canceling agent for activated sludge

Info

Publication number
JPH0671287A
JPH0671287A JP4253713A JP25371392A JPH0671287A JP H0671287 A JPH0671287 A JP H0671287A JP 4253713 A JP4253713 A JP 4253713A JP 25371392 A JP25371392 A JP 25371392A JP H0671287 A JPH0671287 A JP H0671287A
Authority
JP
Japan
Prior art keywords
bulking
activated sludge
sludge
value
filamentous bacteria
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
JP4253713A
Other languages
Japanese (ja)
Other versions
JP2655032B2 (en
Inventor
Toshiharu Maruoka
俊晴 丸岡
Fumi Minami
文 南
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.)
Shikoku Chemicals Corp
Original Assignee
Shikoku Chemicals 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 Shikoku Chemicals Corp filed Critical Shikoku Chemicals Corp
Priority to JP4253713A priority Critical patent/JP2655032B2/en
Publication of JPH0671287A publication Critical patent/JPH0671287A/en
Application granted granted Critical
Publication of JP2655032B2 publication Critical patent/JP2655032B2/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

  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Activated Sludge Processes (AREA)

Abstract

PURPOSE:To efficiently cancel bulking resulted from the generation of filiform micro-organism in a waste water treatment plant using activated-sludge process. CONSTITUTION:By adding the bulking canceling agent containing alkyl pyridinium halide as an effective component to an activated-sludge treatment plant in 0.05-5 pt.wt. per 100 pt.wt. solid matter of activated sludge, the filiform micro-organism is sterilized and the bulking of the activated sludge is canceled.

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、廃水処理装置における
活性汚泥のバルキングの解消剤に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a bulking eliminator for activated sludge in a wastewater treatment system.

【0002】[0002]

【従来の技術】一般生活排水、工場排水等の有機物質を
含有する廃水の処理方法として、活性汚泥法が広く採用
されている。活性汚泥法は処理すべき廃水と微生物の集
合体である活性汚泥を接触させることにより、有機物を
吸収・分解除去させる曝気工程と、活性汚泥を処理水と
の比重差を利用して処理水から沈降分離させる分離工程
から構成されている。しかし、その処理過程において活
性汚泥が膨化し、処理水に対する汚泥の比重が減少する
ことに起因して、分離工程における処理水と活性汚泥の
分離が円滑に行われなくなる現象が頻繁に発生する。
2. Description of the Related Art The activated sludge method has been widely adopted as a method for treating wastewater containing organic substances such as general domestic wastewater and factory wastewater. The activated sludge method uses an aeration process that absorbs and decomposes and removes organic matter by contacting the wastewater to be treated with activated sludge, which is an aggregate of microorganisms, and the activated sludge is treated from the treated water using the difference in specific gravity between the treated water and the treated water. It is composed of a separation process for sedimentation separation. However, the activated sludge expands in the treatment process, and the specific gravity of the sludge with respect to the treated water decreases, so that the phenomenon that the treated water and the activated sludge cannot be smoothly separated in the separation step frequently occurs.

【0003 】このような現象はバルキングと呼ばれ、特
に膨化の原因が糸状性細菌の繁殖によるバルキングの場
合には、活性汚泥の沈降性が極端に低下し、ひどい状態
になると、汚泥が処理水と共に溢流して、放流先の水質
汚染が発生するばかりでなく、廃水処理装置の継続的使
用が不可能になるおそれがあった。
Such a phenomenon is called bulking, and particularly when the cause of expansion is bulking due to the growth of filamentous bacteria, the sedimentation of the activated sludge is extremely lowered, and when the sludge becomes terrible, the sludge becomes treated water. At the same time, there is a risk that not only the water will be spilled out but water pollution at the discharge destination will occur, but also continuous use of the wastewater treatment device will be impossible.

【0004】このようなバルキングを解消する方法とし
ては、廃水処理の活性汚泥中に糸状性細菌を異常繁殖さ
せないために、尿素あるいはアミノ酸類を添加する方法
(特開昭52−8665号公報)、あるいは尿素及びリン酸ソ
ーダを添加して窒素及び燐分を調製する方法等が提案さ
れている。しかしながら、これらの方法は処理に長期間
を必要とする上に薬剤コストが高くつき、しかも効果が
判然としないなどの難点があった。
As a method of eliminating such bulking, a method of adding urea or amino acids in order to prevent abnormal growth of filamentous bacteria in activated sludge of wastewater treatment (Japanese Patent Laid-Open No. 52-8665), Alternatively, a method has been proposed in which urea and sodium phosphate are added to prepare nitrogen and phosphorus. However, these methods have drawbacks in that the treatment requires a long period of time, the cost of the drug is high, and the effect is unclear.

【0005】また汚泥中の浮遊物質を沈降させるため
に、ベントナイト、クリストバライト等を添加する方法
(特開昭60−175599号公報)、あるいは塩化第二鉄、ポ
リ塩化アルミニウム及びカチオン系高分子等の凝集剤を
添加する方法が知られている。これらの方法は速効的な
沈降性改良効果はあるが、糸状性細菌に対する殺菌作用
を有していないため根本的な解消につながらず、薬剤を
連続的に添加する必要があり、多量の薬剤を使用しなけ
ればならないという欠点があった。
Further, a method of adding bentonite, cristobalite or the like in order to settle suspended matter in sludge (JP-A-60-175599), or ferric chloride, polyaluminum chloride and cationic polymers, etc. A method of adding a coagulant is known. Although these methods have a rapid improving effect on sedimentation property, they do not have a bactericidal action against filamentous bacteria and therefore do not lead to a fundamental solution. It had the drawback of having to be used.

【0006】さらに、糸状性細菌を殺菌することにより
バルキングを解消させる方法としては、塩酸クロルヘキ
シジン、グルコン酸及びクロルヘキシジンの混合物を添
加する方法(特公平1-37364 号公報)、ジアルキルアミ
ン、アンモニア及びエピハロヒドリンとの反応、あるい
はポリアルキレンポリアミンとエピハロヒドリンとの反
応によって得られる水溶性陽イオン性重合体を添加する
方法(特開昭63−218299号及び特開平2-169096号公報)
が提案されているが、これらの薬剤は何れも糸状性細菌
の殺菌効果を発揮する有効濃度を維持するためには、多
量の薬剤を連続的に添加する必要があり他の有用な活性
汚泥菌に対しても殺菌効果を示すほか、環境に対する影
響及び経済性に難点があった。
Further, as a method of eliminating bulking by sterilizing filamentous bacteria, a method of adding a mixture of chlorhexidine hydrochloride, gluconic acid and chlorhexidine (Japanese Patent Publication No. 1-37364), dialkylamine, ammonia and epihalohydrin Method of adding water-soluble cationic polymer obtained by reaction with polyalkylene polyamine and epihalohydrin (JP-A-63-218299 and JP-A-2-169096)
However, in order to maintain an effective concentration at which any of these agents exerts the bactericidal effect of filamentous bacteria, it is necessary to continuously add a large amount of the agent, and other useful activated sludge fungi. In addition to exhibiting a bactericidal effect, there were problems in environmental impact and economical efficiency.

【0007】なお、前記以外にバルキングを解消する方
法として、塩素ガス、次亜塩素酸ナトリウム、過酸化水
素あるいはオゾンを添加する方法も知られているが、塩
素ガスは毒性が強く取扱いが困難であり、且つこれらの
薬剤は活性汚泥中の微生物に対しても悪影響があるの
で、使用に際しての投入量の算定が難しく、専門的な知
識を必要とするため、一般的に普及するには至っていな
いのが現状である。
In addition to the above, as a method of eliminating bulking, a method of adding chlorine gas, sodium hypochlorite, hydrogen peroxide or ozone is also known, but chlorine gas is highly toxic and difficult to handle. Since these chemicals also have an adverse effect on the microorganisms in the activated sludge, it is difficult to calculate the input amount at the time of use and specialized knowledge is required, so it has not been widely spread. is the current situation.

【0008】[0008]

【発明が解決しようとする課題】本発明の目的は、少量
の薬剤使用によってバルキングを解消し、且つ活性汚泥
中の微生物及び処理水に影響を与えることなくバルキン
グを解消しうる薬剤を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a chemical agent capable of eliminating bulking by using a small amount of the chemical agent and eliminating the bulking agent without affecting the microorganisms in the activated sludge and the treated water. It is in.

【0009】[0009]

【課題を解決するための手段】本発明者等は、このよう
な事情に鑑みバルキングが発生している活性汚泥を広く
採取して種々の試験を行った結果、アルキルピリジニウ
ムハライドの糸状性細菌に対する殺菌作用がバルキング
の解消に有効であり、しかも活性汚泥中の微生物及び処
理水には影響を与えないことを見い出し、本発明を完遂
するに至った。
[Means for Solving the Problems] In view of such circumstances, the present inventors extensively collected activated sludge in which bulking has occurred and conducted various tests. As a result, the alkylpyridinium halide was tested against filamentous bacteria. It was found that the bactericidal action is effective in eliminating bulking, and that it does not affect the microorganisms in the activated sludge and the treated water, and the present invention has been completed.

【0010】本発明に用いられるアルキルピリジニウム
ハライドは、化1に示される一般式で表されるものであ
り、その代表的なものとしては、エチルピリジニウムブ
ロマイド、n−ブチルピリジニウムクロライド、ドデシ
ルピリジニウムクロライド、ヘキサデシルピリジニウム
クロライド及びヘキサデシルピリジニウムブロマイド等
が挙げられる。これらアルキルピリジニウムハライド
は、塩化アルキルとピリジンを加熱攪拌下に反応させ、
反応終了後、生成物を水蒸気蒸留して未反応ピリジンを
除去し、再結晶させることにより得られる。
The alkylpyridinium halide used in the present invention is represented by the general formula shown in Chemical formula 1, and representative examples thereof include ethylpyridinium bromide, n-butylpyridinium chloride, dodecylpyridinium chloride, Hexadecylpyridinium chloride, hexadecylpyridinium bromide and the like can be mentioned. These alkylpyridinium halides are obtained by reacting alkyl chloride with pyridine under heating and stirring,
After completion of the reaction, the product is obtained by subjecting the product to steam distillation to remove unreacted pyridine and recrystallization.

【0011】[0011]

【化1】 [Chemical 1]

【0012】本発明のバルキング解消剤の使用に当たっ
ては、糸状性バルキングが発生している活性汚泥処理装
置の曝気槽及び返送汚泥ライン等に、粉末状のバルキン
グ解消剤を直接活性汚泥に添加するか、バルキング解消
剤を水に溶解させた溶液を滴下または投入、あるいは無
機多孔質担体に含浸させて添加するなどの方法が用いら
れる。
In the use of the bulking elimination agent of the present invention, whether the powdered bulking elimination agent is directly added to the activated sludge in the aeration tank of the activated sludge treatment device in which filamentous bulking is generated, the returning sludge line, etc. A method in which a solution in which a bulking canceling agent is dissolved in water is dropped or added, or an inorganic porous carrier is impregnated and added is used.

【0013】本発明のバルキング解消剤の使用に当たっ
て、添加される本バルキング解消剤の量は、糸状性細菌
の繁殖状況により異なるが、通常は活性汚泥の乾燥固形
分100重量部に対して0.05〜5重量部の割合にな
るように添加すればよい。この際に添加される本バルキ
ング解消剤が0.05重量部未満の場合は、糸状性細菌
に対する殺菌作用が低いため糸状性バルキングの解消は
困難であり、5重量部を超える場合は活性汚泥菌に悪影
響が現れ、正常な処理が行われなくなるので好ましくな
い。
The amount of the bulking-eliminating agent added in the use of the bulking-eliminating agent of the present invention varies depending on the growth status of filamentous bacteria, but it is usually 0.1% based on 100 parts by weight of the dry solid content of the activated sludge. It may be added in an amount of 05 to 5 parts by weight. If the bulking eliminating agent added at this time is less than 0.05 parts by weight, it is difficult to eliminate the filamentous bulking because the bactericidal action against filamentous bacteria is low, and if it exceeds 5 parts by weight, activated sludge fungi are used. Is adversely affected and normal processing cannot be performed, which is not preferable.

【0014】[0014]

【作用】バルキングの発生原因となる糸状性細菌は、そ
の核となる鞘内細胞が鞘皮によって覆われており、一般
の微生物に比べて外的な影響を受けにくいものであり、
また鞘内細胞は鞘皮が破壊され、外部に遊離した状態で
も活発に活動し、糸状体の再形成を行うので、バルキン
グを解消するには、糸状性細菌の核となる鞘内細胞を死
滅させる必要がある。
[Function] The filamentous bacterium that causes bulking has cells in the sheath that are the core of the filamentous bacterium covered by a sheath, and is less susceptible to external influences than general microorganisms.
In addition, since the sheath cells are destroyed and the sheath cells are actively activated even when they are released to the outside to reform the filaments, the sheath cells that are the nucleus of filamentous bacteria are killed in order to eliminate bulking. Need to let.

【0015】活性汚泥に繁殖した糸状性細菌に対する殺
菌効果は、本発明のアルキルピリジニウムハライドを添
加したのち2〜5時間で現れ、鞘の中に規則正しく納ま
っている糸状性細菌の細胞が破壊される様子を観察する
ことができ、更に時間が経過すれば、鞘が各所で切断さ
れ細かな断片として遊離するのが観察できる。糸状性細
菌が殺菌されるにつれて、バルキングが解消され、活性
汚泥の沈降性を示す汚泥指標値(以下、SVI:Sluge
Volume Indexという)は急激に下がり、活性汚泥は沈降
性のよい正常な状態となる。
The bactericidal effect on the filamentous bacteria propagated in the activated sludge appears in 2 to 5 hours after the addition of the alkylpyridinium halide of the present invention, and destroys the cells of the filamentous bacteria regularly housed in the sheath. The appearance can be observed, and it can be observed that the sheath is cut at various places and released as fine fragments with the passage of time. As the filamentous bacteria are sterilized, the bulking is eliminated and the sludge index value showing the sedimentation property of the activated sludge (hereinafter, SVI: Sluge
The volume index) drops rapidly, and activated sludge is in a normal state with good sedimentation.

【0016】本発明のアルキルピリジニウムハライド
は、活性汚泥菌には影響を与えず、選択的に糸状性細菌
を死滅させることができる。アルキルピリジニウムハラ
イドは、第4級塩として優れた殺菌剤であることが知ら
れているが、活性汚泥の糸状性細菌を選択的に死滅させ
ることができる現象及び理由については解明する迄には
至っていない。
The alkylpyridinium halide of the present invention does not affect the activated sludge bacterium and can selectively kill filamentous bacteria. Alkylpyridinium halides are known to be excellent bactericides as quaternary salts, but it has not yet been elucidated about the phenomenon and the reason why filamentous bacteria in activated sludge can be selectively killed. Not in.

【0017】[0017]

【実施例】【Example】

(実施例1)活性汚泥の乾燥固形分(以下、MLSSと
いう)の値が1420ppm、SVIが180である団
地合併処理槽の活性汚泥10リットルを容量12.5リ
ットルの曝気槽に入れ、空気量7リットル/分で曝気を
行いながら、グルコース0.36g/リットル及びポリ
ペプトンの0.12g/リットルを含むように調整した
人工汚水を定量ポンプを用いて1日当たり10リットル
の割合で曝気槽に連続添加し、活性汚泥を培養したとこ
ろ、スフェロチルス・ナタンスが増殖し、6日後にはM
LSS値が1500ppm、SVI値が650のバルキ
ング活性汚泥になった。
(Example 1) 10 liters of activated sludge in the combined treatment tank of the housing complex having a dry solid content (hereinafter referred to as MLSS) of the activated sludge of 1420 ppm and an SVI of 180 was put into an aeration tank having a capacity of 12.5 liters, and the amount of air While performing aeration at 7 liters / minute, artificial sewage adjusted to contain glucose 0.36 g / liter and polypeptone 0.12 g / liter was continuously added to the aeration tank at a rate of 10 liters per day using a metering pump. Then, when activated sludge was cultivated, Spherocillus natans grew, and after 6 days M
The bulking activated sludge has an LSS value of 1500 ppm and an SVI value of 650.

【0018】この状態において、ヘキサデシルピリジニ
ウムクロライド一水和物40mgを曝気槽に均一に添加
し、これから24時間後の活性汚泥はMLSS値が14
00ppm、SVI値が220であった。この時の糸状
性細菌の様子を観察するとスフェロチルス・ナタンスの
細胞は鞘内で収縮し、一部の細胞は鞘から脱落している
様子が見られた。
In this state, 40 mg of hexadecylpyridinium chloride monohydrate was uniformly added to the aeration tank, and 24 hours after this, the activated sludge had an MLSS value of 14
It was 00 ppm and the SVI value was 220. When the appearance of filamentous bacteria at this time was observed, it was found that the cells of Spherocillus natans contracted in the sheath, and some cells fell out of the sheath.

【0019】3日後の活性汚泥はMLSS値が1660
ppm、SVI値が140まで低下しており、沈降性の
よい活性汚泥になっていた。この時の糸状性細菌の様子
を観察すると糸状性細菌の鞘が各所で切断され断片とな
って活性汚泥のフロックから遊離していた。また、鞘内
の細胞はほとんど鞘から脱落していた。
The activated sludge after 3 days has an MLSS value of 1660.
The ppm and SVI values were reduced to 140, and the activated sludge had a good sedimentation property. When the appearance of filamentous bacteria at this time was observed, the filamentous bacterial sheaths were cut at various places and became fragments, which were liberated from the flocs of the activated sludge. Most of the cells in the sheath were shed from the sheath.

【0020】6日後の活性汚泥のSVI値は120〜1
40で安定しており、沈降性の良好な状態が維持されて
いた。糸状性細菌の様子を観察したところ新たな糸状性
細菌の生育は認められなかった。また、この試験期間中
の処理水の水質はBOD値が20ppm以下を維持して
おり、本発明のバルキング解消剤の添加による処理機能
への悪影響は全くなかった。
The SVI value of the activated sludge after 6 days is 120 to 1
It was stable at 40, and the state of good sedimentation was maintained. When the appearance of filamentous bacteria was observed, new filamentous bacteria did not grow. Further, the water quality of the treated water during this test period had a BOD value of 20 ppm or less, and the addition of the bulking elimination agent of the present invention had no adverse effect on the treatment function.

【0021】(実施例2)実施例1において用いたのと
同じ連続処理系で糸状性細菌を培養し、スフェロチルス
・ナタンスとタイプ021Nのバルキング汚泥(MLS
S値:1420ppm、SVI:520)を得た。次い
で、ドデシルピリジニウムクロライド30mgを曝気槽
に均一に添加し、活性汚泥の培養を継続した。18時間
後の活性汚泥はMLSS値が1300ppm、SVI値
が320であった。この時の糸状性細菌の様子を観察す
ると実施例1と同様の状態が確認できた。
(Example 2) Filamentous bacteria were cultured in the same continuous treatment system as used in Example 1, and Spherocillus natans and type 021N bulking sludge (MLS) were used.
S value: 1420 ppm, SVI: 520) were obtained. Next, 30 mg of dodecylpyridinium chloride was uniformly added to the aeration tank, and the culture of activated sludge was continued. The activated sludge after 18 hours had an MLSS value of 1300 ppm and an SVI value of 320. When the appearance of filamentous bacteria at this time was observed, the same state as in Example 1 could be confirmed.

【0022】3日後の活性汚泥はMLSS値が1460
ppm、SVI値が180であり、6日後ではMLSS
値が1670ppm、SVI値は140であった。糸状
性バルキングは解消されており、沈降性の良い状態が維
持できた。また、新たな糸状性細菌の生育は認められな
かった。この試験期間中の処理水の水質はBOD値が2
0ppm以下を維持しており、処理機能への悪影響は全
くなかった。
The activated sludge after 3 days has an MLSS value of 1460.
ppm and SVI values are 180, and MLSS after 6 days
The value was 1670 ppm and the SVI value was 140. Filamentous bulking was eliminated and good sedimentation was maintained. In addition, the growth of new filamentous bacteria was not observed. The quality of treated water during this test period has a BOD value of 2
It was maintained at 0 ppm or less, and had no adverse effect on the processing function.

【0023】(実施例3)実施例1において用いたのと
同じ連続処理系で糸状性細菌を培養し、スフェロチルス
・ナタンスとタイプ021Nのバルキング汚泥(MLS
S値:1030ppm、SVI:920)を得た。次い
で、n−ブチルピリジニウムクロライド150mgを曝
気槽に均一に添加し、活性汚泥の培養を継続した。15
時間後の活性汚泥はMLSS値が1100ppm、SV
I値が460であった。この時の糸状性細菌の様子を観
察すると実施例1と同様の状態が確認できた。
(Example 3) Filamentous bacteria were cultured in the same continuous treatment system as used in Example 1 to obtain Spherocillus natanus and type 021N bulking sludge (MLS).
S value: 1030 ppm, SVI: 920) were obtained. Next, 150 mg of n-butylpyridinium chloride was uniformly added to the aeration tank, and the culture of activated sludge was continued. 15
MLSS value of activated sludge after 1 hour is 1100ppm, SV
The I value was 460. When the appearance of filamentous bacteria at this time was observed, the same state as in Example 1 could be confirmed.

【0024】3日後ではMLSS値が1240ppm、
SVI値が240であり、6日後ではMLSS値が14
10ppm、SVI値は160であった。糸状性バルキ
ングは解消されており、沈降性の良い状態が維持でき
た。また、新たな糸状性細菌の生育は認められなかっ
た。この試験期間中の処理水の水質はBOD値が20p
pm以下を維持しており、処理機能への悪影響は全くな
かった。
After 3 days, the MLSS value was 1240 ppm,
The SVI value is 240, and the MLSS value is 14 after 6 days.
10 ppm, SVI value was 160. Filamentous bulking was eliminated and good sedimentation was maintained. In addition, the growth of new filamentous bacteria was not observed. The quality of the treated water during this test had a BOD value of 20p.
The pm level was maintained, and there was no adverse effect on the processing function.

【0025】(実施例4)MLSS値が1700pp
m、SVI値が230である団地合併処理槽の活性汚泥
10リットルを実施例1において用いたのと同じ処理装
置に入れ、曝気を行いながら、グルコース0.55g/
リットル及びエールリッヒ肉エキス0.12g/リット
ルを含むように調整した人工汚水を定量ポンプを用いて
1日当たり10リットルの割合で曝気槽に連続添加し、
活性汚泥を培養したところ、タイプI−5及びII−4
(糸状性細菌は河野らの分類による)のバルキング汚泥
となり、MLSS値が1620ppm、SVI値が52
0となった。
(Example 4) MLSS value is 1700 pp
m, SVI value of 230 10g of activated sludge of the combined treatment tank of the housing complex was put in the same treatment equipment as used in Example 1, while performing aeration, glucose 0.55g /
Liters and Ehrlich meat extract 0.12 g / liter of artificial sewage adjusted to be continuously added to the aeration tank at a rate of 10 liters per day using a metering pump,
When activated sludge was cultivated, types I-5 and II-4
(Filamentous bacteria are classified by Kono et al.) As bulking sludge with MLSS value of 1620ppm and SVI value of 52.
It became 0.

【0026】ここで、ヘキサデシルピリジニウムクロラ
イド一水和物50mgを曝気槽に均一に添加した。添加
から15時間後の活性汚泥はMLSS値が1780pp
m、SVI値が340であった。この時の糸状性細菌の
様子を観察するとタイプI−5及びII−4の細胞は鞘内
で収縮している様子が見られ、糸状性細菌に対する殺菌
作用が確認できた。
Here, 50 mg of hexadecylpyridinium chloride monohydrate was uniformly added to the aeration tank. The activated sludge 15 hours after the addition has an MLSS value of 1780 pp
m, SVI value was 340. When the appearance of filamentous bacteria at this time was observed, it was observed that the cells of types I-5 and II-4 were contracting in the sheath, and the bactericidal action against filamentous bacteria could be confirmed.

【0027】3日後の活性汚泥はMLSS値が2020
ppm、SVI値が170であり、6日後ではMLSS
値が2300ppm、SVI値は140であった。糸状
性バルキングは解消されており、沈降性の良い状態が維
持できた。また、新たな糸状性細菌の生育は認められな
かった。この試験期間中の処理水の水質はBOD値が2
0ppm以下を維持しており、処理機能への悪影響は全
くなかった。
The activated sludge after 3 days has an MLSS value of 2020.
ppm and SVI values are 170, and MLSS after 6 days
The value was 2300 ppm and the SVI value was 140. Filamentous bulking was eliminated and good sedimentation was maintained. In addition, the growth of new filamentous bacteria was not observed. The quality of treated water during this test period has a BOD value of 2
It was maintained at 0 ppm or less, and had no adverse effect on the processing function.

【0028】(比較例)実施例1及び実施例4におい
て、本発明のバルキング解消剤を添加しなかった以外は
全く同じ処理を行ったところ、バルキングの改善は全く
認められず、試験期間中のSVI値は500以上であ
り、沈降性の悪い状態のままであった。
(Comparative Example) In Example 1 and Example 4, the same treatment was carried out except that the bulking elimination agent of the present invention was not added, but no improvement in bulking was observed, and during the test period. The SVI value was 500 or more, and the sedimentation property remained poor.

【0029】[0029]

【発明の効果】本発明のバルキング解消剤を用いれば、
少量の薬剤の添加によりバルキングが解消できると共
に、活性汚泥中の微生物及び処理水に影響を与えること
なくバルキングを解消することが可能である。
By using the bulking elimination agent of the present invention,
It is possible to eliminate bulking by adding a small amount of chemicals, and it is possible to eliminate bulking without affecting the microorganisms in the activated sludge and the treated water.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 アルキルピリジニウムハライドを有効成
分とする活性汚泥のバルキング解消剤。
1. A bulking elimination agent for activated sludge containing an alkylpyridinium halide as an active ingredient.
JP4253713A 1992-08-27 1992-08-27 Activated sludge bulking remover Expired - Fee Related JP2655032B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4253713A JP2655032B2 (en) 1992-08-27 1992-08-27 Activated sludge bulking remover

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4253713A JP2655032B2 (en) 1992-08-27 1992-08-27 Activated sludge bulking remover

Publications (2)

Publication Number Publication Date
JPH0671287A true JPH0671287A (en) 1994-03-15
JP2655032B2 JP2655032B2 (en) 1997-09-17

Family

ID=17255117

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4253713A Expired - Fee Related JP2655032B2 (en) 1992-08-27 1992-08-27 Activated sludge bulking remover

Country Status (1)

Country Link
JP (1) JP2655032B2 (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4914411A (en) * 1972-06-12 1974-02-07
JPS539318A (en) * 1976-07-08 1978-01-27 Mitsubishi Gas Chem Co Inc Glowth inhibiting agent for microorganisms
JPS63218294A (en) * 1987-03-04 1988-09-12 Mitsubishi Monsanto Chem Co Process for preventing activated sludge from bulking
JPH01153604A (en) * 1987-12-11 1989-06-15 Dainippon Ink & Chem Inc Slime controller for petroleum fuel

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4914411A (en) * 1972-06-12 1974-02-07
JPS539318A (en) * 1976-07-08 1978-01-27 Mitsubishi Gas Chem Co Inc Glowth inhibiting agent for microorganisms
JPS63218294A (en) * 1987-03-04 1988-09-12 Mitsubishi Monsanto Chem Co Process for preventing activated sludge from bulking
JPH01153604A (en) * 1987-12-11 1989-06-15 Dainippon Ink & Chem Inc Slime controller for petroleum fuel

Also Published As

Publication number Publication date
JP2655032B2 (en) 1997-09-17

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