JPH07100483A - Method for treating activated sludge and treating agent for it - Google Patents

Method for treating activated sludge and treating agent for it

Info

Publication number
JPH07100483A
JPH07100483A JP25025091A JP25025091A JPH07100483A JP H07100483 A JPH07100483 A JP H07100483A JP 25025091 A JP25025091 A JP 25025091A JP 25025091 A JP25025091 A JP 25025091A JP H07100483 A JPH07100483 A JP H07100483A
Authority
JP
Japan
Prior art keywords
sludge
activated sludge
activated
treating
magnesium silicate
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
JP25025091A
Other languages
Japanese (ja)
Other versions
JP2811129B2 (en
Inventor
Akio Oguma
熊 昭 夫 小
Yasuo Mizoguchi
口 保 夫 溝
Kiyoshi Yotsuhashi
橋 泓 四
Masafumi Kusumi
見 雅 史 楠
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.)
WASEI SANGYO KK
Mizusawa Industrial Chemicals Ltd
Tokiwa Corp
Original Assignee
WASEI SANGYO KK
Mizusawa Industrial Chemicals Ltd
Tokiwa 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 WASEI SANGYO KK, Mizusawa Industrial Chemicals Ltd, Tokiwa Corp filed Critical WASEI SANGYO KK
Priority to JP25025091A priority Critical patent/JP2811129B2/en
Publication of JPH07100483A publication Critical patent/JPH07100483A/en
Application granted granted Critical
Publication of JP2811129B2 publication Critical patent/JP2811129B2/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

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Activated Sludge Processes (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To provide a method for treating an activated sludge, suitable to form a sludge with excellent denseness and settling properties and provide a composite treating agent for it. CONSTITUTION:In this composite treating agent, an aerobic bacterium, a microorganism enzyme and a fibrous magnesium silicate clay mineral with a specific surface of 100 to 350 m<2>/g, an oil absorption of 100 to 300ml/100g and a fiber length of 5 to 20mum are combined to an activated sludge. Bulking phenomenon in the activated-sludge process can be prevented from occurring by combining this composite treating agent and a sludge floc with excellent denseness, settling properties and dehydration properties is formed and ordinary trouble in the method for the activated-sludge process is dissolved.

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、排水の汚泥処理剤に関
し、より詳細には活性汚泥処理法において緻密性及び沈
降性等に優れた汚泥を形成させるに適した活性汚泥の処
理方法及びその処理剤に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge treatment agent for wastewater, and more particularly to a method for treating activated sludge suitable for forming sludge having excellent compactness and sedimentation property in the activated sludge treatment method and a method thereof. Regarding treatment agents.

【0002】[0002]

【従来の技術】従来より、都市下水、産業廃水として排
出される有機物等を含む廃水の処理方法として曝気等に
より空気を吹き込みながら有用微生物を繁殖させ、吸着
性に富む汚泥フロックを形成させ廃水中のBOD、CO
Dを下げると共に、汚泥フロックを沈降させて排水を処
理する、所謂活性汚泥法が広く採用されている。そのた
めに従来より汚泥に、無機凝集剤、有機高分子凝集剤、
有機物分解酵素及び無機多孔質体等を添加して汚泥フロ
ックの凝集性、沈降性、緻密性又は脱水性を改善させる
ことが行なわれている。
2. Description of the Related Art Conventionally, as a method for treating wastewater containing organic substances and the like discharged as municipal wastewater and industrial wastewater, useful microorganisms are propagated by blowing air by aeration and the like to form sludge flocs with high adsorbability to form wastewater. BOD, CO
A so-called activated sludge method is widely adopted, in which D is lowered and sludge flocs are settled to treat wastewater. Therefore, conventionally, in sludge, inorganic flocculant, organic polymer flocculant,
It has been practiced to improve the cohesiveness, sedimentation property, compactness or dehydration property of sludge flocs by adding an organic matter decomposing enzyme, an inorganic porous material and the like.

【0003】例えば、特開平1−99696号公報には
生汚泥中に存在する増殖菌体を構成する難分解性の蛋白
質を分解させる酵素を添加させて、糸状性細菌の繁殖に
よるバルキング現象を防止させることが記載されてい
る。また、特開昭62−186997号及び特公昭62
−46237号公報にはバルキング現象の状態にある活
性汚泥に、微生物を吸着する無機多孔質体と有機高分子
凝集剤とを併用させ、汚泥の凝集ならびに分離効果を向
上させることが記載されている。
[0003] For example, Japanese Patent Laid-Open No. 1-99696 discloses adding a enzyme that decomposes a hardly-degrading protein that constitutes a proliferating microbial cell present in raw sludge to prevent the bulking phenomenon due to the propagation of filamentous bacteria. It is described to do. In addition, JP-A-62-186997 and JP-B-62
JP-A-46237 describes that an activated sludge in the state of bulking is used in combination with an inorganic porous material that adsorbs microorganisms and an organic polymer flocculant to improve the sludge flocculation and separation effects. .

【0004】[0004]

【発明が解決しようとする課題】しかしながら従来よ
り、活性汚泥法による廃水処理において、その処理条件
に適切さを欠き、糸状性細菌が多数繁殖し過ぎ、いわゆ
るバルキング現象を引き起こし汚泥フロックが嵩だかに
なったり、汚泥フロックが細かく分散して凝集しなかっ
たり、また汚泥の粘性が高く緻密性を欠く汚泥フロック
が形成されたりしてフロックの沈降及び緻密性を低下さ
せる等の種々のトラブルを発生させている。その結果、
排水処理の能力を著しく低下させ、処利水のBOD、C
ODを十分に低下させることが出来ず、未だ根本的な解
決がなされていないのが実情である。
However, conventionally, in the wastewater treatment by the activated sludge method, the treatment conditions are not suitable and a large number of filamentous bacteria multiply, which causes a so-called bulking phenomenon and the sludge flocs become bulky. Sludge flocs are finely dispersed and do not aggregate, and sludge flocs with high viscosity and lack of compactness are formed, causing various troubles such as sedimentation of flocs and deterioration of compactness. ing. as a result,
The capacity of wastewater treatment is significantly reduced, and the treated water BOD, C
The reality is that the OD cannot be lowered sufficiently and a fundamental solution has not yet been made.

【0005】従って本発明の目的は、活性汚泥に対して
好気性バクテリヤ及び/又は微生物酵素を添加させて、
汚泥の活性を低下させずに糸状性細菌の繁殖し過ぎを防
止し、所謂バルキング現象を防止しつつ、汚泥中に繊維
状のケイ酸マグネシウム粘土鉱物を接触させて、緻密性
及び沈降性に優れた汚泥フロックを形成させることを特
徴とする活性汚泥の処理方法を提供するにある。
Therefore, an object of the present invention is to add aerobic bacteria and / or microbial enzymes to activated sludge,
Prevents overproliferation of filamentous bacteria without lowering the activity of sludge and prevents the so-called bulking phenomenon, while contacting fibrous magnesium silicate clay mineral in sludge, it is excellent in compactness and sedimentation Another object of the present invention is to provide a method for treating activated sludge, which is characterized by forming sludge flocs.

【0006】本発明の他の目的は、上記の活性汚泥の処
理法に用いる好気性バクテリヤ及び/又は微生物酵素、
好気性バクテリヤの栄養剤及び繊維状のケイ酸マグネシ
ウム粘土鉱物を組合せて成る活性汚泥用の処理剤を提供
するにある。
Another object of the present invention is to use aerobic bacteria and / or microbial enzymes for the above-mentioned method for treating activated sludge,
There is provided a treatment agent for activated sludge, which comprises a combination of a nutrient for aerobic bacteria and a fibrous magnesium silicate clay mineral.

【0007】[0007]

【課題を解決するための手段】本発明者によれば、種々
の無機質担持体の内でも三次元の鎖状構造を有する、所
謂繊維状の無機質多孔質体であるセピオライト及びアタ
パルジャイト等を微生物細菌が繁茂する有機質分散体に
添加すると、その分散液が凝集しセピオライトと共にこ
の有機質が沈降する現象を見出した。この知見を活性汚
泥処理に利用出来ないか鋭意検討した結果、沈降性に優
れた汚泥フロックが得られることを見出し本発明にいた
ったものである。
According to the present inventors, microbial bacteria such as sepiolite and attapulgite, which are so-called fibrous inorganic porous materials having a three-dimensional chain-like structure among various inorganic carriers, can be used. It was found that when added to an organic dispersion in which the organic matter flourishes, the dispersion aggregates and the organic matter settles together with sepiolite. As a result of diligent studies on whether this finding can be used for treatment of activated sludge, the inventors have found that sludge flocs having excellent sedimentation properties can be obtained, and have reached the present invention.

【0008】本発明によれば、活性汚泥に対して、必要
に応じて(A)好気性バクテリヤ、(B)窒素、リン及
びカリ成分からなる(A)に対する栄養剤、(C)微生
物酵素を添加させて成る該汚泥混合物系に、(D)BE
T法比表面積が100乃至300m^2 /gの範囲にあ
る繊維状のケイ酸マグネシウム粘土鉱物を接触させ、該
汚泥混合物を沈降させることを特徴とする活性汚泥の処
理方法及びその処理剤が提供される。
According to the present invention, (A) an aerobic bacterium, (B) a nutrient for (A) consisting of nitrogen, phosphorus and potassium components, and (C) a microbial enzyme are added to the activated sludge as required. The sludge mixture system formed by adding (D) BE
A method for treating activated sludge and a treating agent therefor, which comprises contacting a fibrous magnesium silicate clay mineral having a T method specific surface area in the range of 100 to 300 m ^ 2 / g to precipitate the sludge mixture. To be done.

【0009】また本発明の最も好適な態様では、活性汚
泥に対して、本発明の処理方法のハンドリング性を向上
させるためから、(A)、(B)及び(C)を予めワン
パックにした処理剤と(D)とを組合わせて使用するこ
とが提供される。また更には、より好ましくは(A)、
(B)及び(C)を(D)に担持させたワンパック型の
複合処理剤を使用することが提供される。
In the most preferred embodiment of the present invention, (A), (B) and (C) are pre-packed in one pack in order to improve the handling property of the treatment method of the present invention for activated sludge. It is provided to use the treatment agent in combination with (D). Furthermore, more preferably (A),
It is provided to use a one-pack type composite treating agent in which (B) and (C) are carried on (D).

【0010】[0010]

【作用】本発明の活性汚泥の処理方法は、通常において
活性汚泥法が抱えている汚泥の不安定性を解決するため
に、活性汚泥に対して好気性バクテリヤ及び/又は微生
物酵素を添加することによって、汚泥の活性を低下させ
ず且つ汚泥の粘性を高めずにしかも糸状性細菌の繁殖し
過ぎを防止し、いわゆるバルキング現象が防止された汚
泥系にし、又はバルキング現象が防止されつつある汚泥
系にして、次いで繊維状のケイ酸マグネシウム粘土鉱物
であるセピオライト等をこの汚泥系に接触させることに
よって、汚泥を緻密性及び沈降性さらには脱水性に優れ
たフロックに形成させることを特徴とする活性汚泥の処
理方法である。
The method for treating activated sludge of the present invention comprises adding aerobic bacteria and / or microbial enzymes to the activated sludge in order to solve the instability of the sludge that the activated sludge method normally has. , Without reducing the activity of the sludge and without increasing the viscosity of the sludge, and preventing the overgrowth of filamentous bacteria, to a sludge system in which the so-called bulking phenomenon is prevented, or a sludge system in which the bulking phenomenon is being prevented. Then, activated sludge characterized in that the sludge is formed into flocs excellent in compactness, sedimentation property and dehydration property by contacting the sludge system with fibrous magnesium silicate clay mineral sepiolite etc. Is the processing method of.

【0011】この排水処理の目的は、活性汚泥を沈降し
やすい汚泥フロックに形成させ且つその形成汚泥フロッ
クが緻密で脱水しやすいものにすることである。また下
水処理場や各排水処理場で利用されているこの活性汚泥
処理法の主役は、あくまで有機汚水中の有機成分を分解
させる微生物酵素である。従ってこの活性汚泥処理法に
おいては、特に上記したように汚泥の活性を低下させず
に、しかも糸状性細菌が繁殖し過ぎないように調整し
て、所謂バルキング現象を防止することが、この活性汚
泥処理法が抱える問題を解消するための重要課題なので
ある。何故ならばこのような対策が効果的に活性汚泥に
なされれば、その効果として容易に予想されることは汚
泥の沈降が促進され、よくある沈殿槽からの汚泥流出も
防止され、また難分解成分等の処理水への流入が防止さ
れることから、従ってバルキング現象を起こさないよう
に活性汚泥に予め前処理的調整を施すことが必要なので
ある。
The purpose of this wastewater treatment is to form activated sludge into sludge flocs that are easy to settle, and to make the formed sludge flocs dense and easy to dehydrate. The main role of this activated sludge treatment method used in sewage treatment plants and wastewater treatment plants is microbial enzymes that decompose organic components in organic wastewater. Therefore, in this activated sludge treatment method, it is particularly important to prevent the so-called bulking phenomenon by adjusting so that the activity of the sludge is not lowered and the filamentous bacteria are not overgrown as described above. It is an important issue to solve the problems of treatment methods. The reason is that if such measures are effectively applied to activated sludge, it is easily expected that the effect will facilitate sludge settling, prevent sludge outflow from common settling tanks, and prevent persistent decomposition. Since components and the like are prevented from flowing into the treated water, it is therefore necessary to pre-treat the activated sludge in advance so that the bulking phenomenon does not occur.

【0012】しかしながら、上記のとうり活性汚泥処理
法が微生物処理であることからすれば、この排水処理工
程を人為的に制御することは、極めて困難と言える。本
発明においては、この問題を解決するために活性汚泥に
対して、(A)好気性バクテリヤ、(B)窒素、リン及
びカリ成分からなる(A)に対する栄養剤及び(C)微
生物酵素等を添加してなる工程が、正しく活性汚泥を安
定化させる上記の前処理的調整であって、次いでこのよ
うに安定化された汚泥混合物に(D)なるBET法比表
面積が100乃至300m^2 /gの範囲にあるセピオ
ライト及びアタパルジャイト等の繊維状のケイ酸マグネ
シウム粘土鉱物を接触させると該汚泥混合物が凝集し汚
泥がフロック化して沈降するものである。
However, it can be said that it is extremely difficult to artificially control this wastewater treatment step because the above-mentioned shaving activated sludge treatment method is a microbial treatment. In the present invention, in order to solve this problem, (A) an aerobic bacterium, (B) a nutrient for (A) consisting of nitrogen, phosphorus and potassium components, and (C) a microbial enzyme are added to the activated sludge. The step of adding is the above-mentioned pretreatment adjustment to properly stabilize the activated sludge, and the sludge mixture thus stabilized (D) has a BET specific surface area of 100 to 300 m ^ 2 / When fibrous magnesium silicate clay minerals such as sepiolite and attapulgite in the range of g are brought into contact with each other, the sludge mixture agglomerates and the sludge flocs to settle.

【0013】本発明において(A)なる好気性バクテリ
ヤは、汚泥の活性を低下させずに、糸状性細菌の繁殖し
過ぎを防止するためのものである。又(C)なる微生物
酵素は、活性汚泥中に含まれる難分解有機成分を分解し
処理水質を悪化させないために作用するものである。ま
た(A)及び(C)の作用によって汚泥の粘性が低下さ
せられる。更に(B)なる窒素、リン及びカリ成分は
(A)の栄養剤として必要なものである。従って、活性
汚泥に予め上記のような機能を組合わせて成る前処理的
調整によって活性汚泥を安定化させることが本発明の第
一の特徴である。
The aerobic bacterium (A) in the present invention is for preventing the overproliferation of filamentous bacteria without lowering the activity of sludge. Further, the microbial enzyme (C) acts to decompose the hardly decomposable organic components contained in the activated sludge so as not to deteriorate the treated water quality. Further, the effects of (A) and (C) reduce the viscosity of sludge. Further, the nitrogen, phosphorus and potassium components (B) are necessary as nutrients for (A). Therefore, the first feature of the present invention is to stabilize the activated sludge by pretreatment adjustment made by previously combining the activated sludge with the above-mentioned functions.

【0014】次いでこの汚泥混合物系とセピオライト等
の繊維状のケイ酸マグネシウム粘土鉱物とが接触する
と、緻密性及び沈降性且つ脱水性に優れた汚泥フロが形
成されることが本発明の第二の特徴である。
Then, when this sludge mixture system is brought into contact with a fibrous magnesium silicate clay mineral such as sepiolite, a sludge flo having excellent compactness, sedimentation and dehydration properties is formed. It is a feature.

【0015】本発明に用いるセピオライト及びアタパル
ジャイト等の繊維状のケイ酸マグネシウム粘土鉱物は、
三次元の鎖状の構造を有し、タルクのような二次元の結
晶構造物とは異なり、この鎖状構造の隙間にできる空孔
がBET法比表面積で100乃至350m^2 /gの範
囲になるような大きな比表面積を有し、しかも吸着作用
を有する多孔質の粘土鉱物である。またセピオライト等
は同じく多孔質粘土鉱物であるモンモリロナイトに代表
される通常の層状粘土鉱物とは異なり、水溶系で膨潤し
ないことも大きな特徴である。
Fibrous magnesium silicate clay minerals such as sepiolite and attapulgite used in the present invention are
It has a three-dimensional chain structure, and unlike two-dimensional crystal structures such as talc, the voids formed in the chain structure have a BET specific surface area of 100 to 350 m ^ 2 / g. It is a porous clay mineral that has a large specific surface area such that Unlike ordinary layered clay minerals represented by montmorillonite, which is also a porous clay mineral, sepiolite is also characterized in that it does not swell in water.

【0016】このようなセピオライトが持つ特徴によっ
て、本発明の第二の特徴をよく説明することが出来る。
即ち、繊維状であることが、通常の粘土鉱物に比べ汚泥
固形分との絡みをよくするし、またセピオライトが大き
な比表面積を有し、しかも吸着作用を有する多孔質の粘
土鉱物であることは、他の繊維状物に比べセピオライト
が汚泥固形分を吸着しやすい表面を有しているものとい
える。従ってその詳細は不明であるが、本発明の処理剤
が有するこれらの特徴ある要因が、活性汚泥中に分散し
ている汚泥有機質を凝集させ、この凝集フロックが核と
なり、更にこの核が繊維状粘土鉱物の汚泥固形分との絡
みによって緻密な多段フロックを形成し、しかも比重が
2. 4に見られるようにセピオライト自身が比較的に重
いことも要因となって、極めて沈降性に優れた汚泥フロ
ックが形成(後述する実施例1の
The second characteristic of the present invention can be well explained by the characteristic of such a sepiolite.
That is, being fibrous, the entanglement with the solid content of sludge is improved as compared with ordinary clay minerals, and sepiolite has a large specific surface area and is a porous clay mineral having an adsorption action. It can be said that sepiolite has a surface that is more likely to adsorb sludge solids than other fibrous materials. Therefore, although its details are unknown, these characteristic factors of the treatment agent of the present invention cause the sludge organic matter dispersed in the activated sludge to be aggregated, and the aggregated flocs become cores, and the cores are fibrous. Sludge with extremely excellent sedimentation properties, due to the fact that dense multi-stage flocs are formed by the entanglement with the solid content of sludge of clay minerals, and that the sepiolite itself is relatively heavy as shown in 2.4. Flock is formed (of Example 1 described later)

【表4】を参照)されるものと言える。Refer to [Table 4]).

【0017】[0017]

【発明の好適態様】本発明の処理剤は、(A)好気性バ
クテリヤ、(B)窒素、リン及びカリ成分からなる
(A)に対いする栄養剤、(C)微生物酵素及び(D)
BET法比表面積が100乃至350m^2 /gの範囲
にある繊維状のケイ酸マグネシウム粘土鉱物との組合せ
からなり、活性汚泥を処理するに際して、(A)、
(B)、(C)及び(D)を添加する順序としては
(A)、(B)、(C)を先に添加し、前述した前処理
的調整が十分に活性汚泥になされてから、(D)を添加
する方法が採用される。然しながらハンドリング性、各
成分の作用効果を考慮すると、本発明の最も好適な態様
は、汚泥に対して、(A)、(B)及び(C)を予めワ
ンパックにし、これに(D)を組合わせて使用する方法
が採用される。更にまた、より好ましくは(A)、
(B)及び(C)を(D)に担持させたワンパック型の
複合処理剤として使用する方法も採用できる。また特に
バルキング現象が問題にされない、所謂前処理的調整を
必要としない汚泥に対しては、(D)なる繊維状のケイ
酸マグネシウム粘土鉱物を単独で使用する方法も採用さ
れることは云うまでもないが、(A)及び(C)の付加
的作用である汚泥の粘性を低下させる効果を考慮する
と、特にバルキング現象が問題にされない活性汚泥に対
しても好ましくは、(D)に(A)、(B)及び(C)
を組合わせて使用するのが良い。
BEST MODE FOR CARRYING OUT THE INVENTION The treatment agent of the present invention comprises (A) an aerobic bacterium, (B) a nutrient for (A) consisting of nitrogen, phosphorus and potassium components, (C) a microbial enzyme and (D).
When the activated sludge is treated with (A), it is composed of a combination with a fibrous magnesium silicate clay mineral having a BET specific surface area in the range of 100 to 350 m 2 / g.
As the order of adding (B), (C) and (D), (A), (B) and (C) are added first, and after the above-mentioned pretreatment adjustment is sufficiently made into activated sludge, The method of adding (D) is adopted. However, considering the handling property and the action and effect of each component, the most preferred embodiment of the present invention is that the sludge (A), (B) and (C) is pre-packed into one pack, and (D) is added to this. A method of using them in combination is adopted. Furthermore, more preferably (A),
A method of using (B) and (C) as a one-pack type composite treatment agent in which (D) is supported can also be adopted. Further, it is needless to say that the method of using the fibrous magnesium silicate clay mineral (D) alone is also adopted for sludge in which the bulking phenomenon is not a problem and so-called pretreatment adjustment is not required. However, considering the effect of lowering the viscosity of sludge, which is an additional action of (A) and (C), it is preferable to use (A) in addition to (A) for activated sludge in which the bulking phenomenon is not a problem. ), (B) and (C)
It is better to use in combination.

【0018】本発明において(A)なる成分は好気性バ
クテリヤ(放線菌群)、硝酸化成菌、一般好気性細菌で
あり、また(C)なる微生物酵素は、通常(A)に含ま
せて使用するが活性汚泥中に残留している有機高分子質
物を分解させる酵素であり、これによって処理水中のC
ODを低減(後述の実施例1の
In the present invention, the component (A) is an aerobic bacterium (actinomycetes group), a nitrifying bacterium, or a general aerobic bacterium, and the microbial enzyme (C) is usually used by being contained in (A). However, it is an enzyme that decomposes the organic polymer that remains in the activated sludge.
Reduction of OD (of Example 1 described later)

【表5】を参照)させることができ、例えばプロテア−
ゼ、リゾチ−ム、セルラ−ゼ、アミラ−ゼ等をこの目的
のために添加する。また生汚泥中には増殖菌体を構成す
る難分解性の蛋白質が多量に含まれるため、プロテア−
ゼを添加することが好適であり、また汚泥に含まれるそ
の他の有機高分子質の種類に応じて、例えばセルラ−
ゼ、アミラ−ゼなどを併用することもよい。
(See Table 5)), for example, Protea
Zease, lysozyme, cellulase, amylase and the like are added for this purpose. In addition, since raw sludge contains a large amount of persistent proteins that constitute the microbial cells,
It is preferable to add zirconium, and depending on the type of other organic polymer contained in the sludge, for example,
It is also possible to use ze, amylase and the like together.

【0019】また更に(D)なる成分として使用する繊
維状の粘土鉱物には、一般にホルマイト鉱物(セピオラ
イト、アタパルジャイト、パリゴルスカイト)等の三層
構造で多孔質の繊維状鉱物、ハロイサイト、アスベスト
等の二層構造の繊維状鉱物、又は鹿沼土、赤玉土などを
含む火山性の繊維状鉱物が用いられる。また必要に応じ
てこの繊維状粘土鉱物にゼオライト、又は酸性白土に代
表される吸着性の粘土鉱物やクリストバライト、石英、
長石等の岩石類を併用してもよい。
Furthermore, the fibrous clay mineral used as the component (D) is generally a two-layered porous fibrous mineral such as holmite mineral (sepiolite, attapulgite, palygorskite), halloysite, asbestos and the like. Layered fibrous minerals, or volcanic fibrous minerals including Kanuma soil and Akadama soil are used. If necessary, this fibrous clay mineral may be zeolite, or an adsorbent clay mineral typified by acid clay, cristobalite, quartz,
Rocks such as feldspar may be used together.

【0020】本発明において、より好ましくはセピオラ
イト、アタパルジャイトのごとく比表面積が大きく、吸
着性を有する繊維状の粘土鉱物が好適に使用される。例
えばセピオライトは、(OH2)4(OH)4Mg 8Si12O
30・6〜8H2 Oの化学組成を持ち、タルクのような二
次元の結晶構造物がレンガを交互に積み重ねたような鎖
状の結晶構造を形成している。このような三次元の鎖状
粘土鉱物は、モンモリロナイト族粘土鉱物に属し、三層
構造を有するベントナイトで代表される層状粘土鉱物と
は異なり、膨潤現象を起こさないのが特徴である。また
この鎖状の隙間に出来た空孔によって繊維状であるが他
の繊維状鉱物とは異なり大きな比表面積と吸着性を有す
ることも大きな特徴である。
In the present invention, more preferably, fibrous clay minerals having a large specific surface area and adsorbability such as sepiolite and attapulgite are preferably used. For example, sepiolite is (OH2) 4 (OH) 4Mg8Si12O
It has a chemical composition of 30.6 to 8H2O, and a two-dimensional crystal structure such as talc forms a chain crystal structure like bricks stacked alternately. Such a three-dimensional chain clay mineral belongs to the montmorillonite group clay mineral, and is different from the layered clay mineral represented by bentonite having a three-layer structure in that it does not cause a swelling phenomenon. In addition, it is fibrous due to the pores formed in the chain-like gap, but unlike other fibrous minerals, it also has a large specific surface area and adsorptivity.

【0021】本発明においては、比表面積が100乃至
350m^2 /gの範囲にあり、吸油量が100乃至3
00ml/100gの範囲にあるセピオライトが好適に
使用される。 比表面積がこの範囲より小さいと汚泥の
凝集力が小さく、一方この範囲よりも大きくても、それ
以上の効果は得られない。また本発明に使用される繊維
状のセピオライトは、一般に繊維子経が0. 1乃至3μ
m、繊維子長が5乃至20μmであることが好ましい。
繊維子長がこの範囲よりも小さいと、緻密で沈降性のフ
ロックが形成されず、一方この範囲よりも大きいと、例
えば石綿のように嵩高となり汚泥上に浮き本発明の目的
を達成させることは困難である。
In the present invention, the specific surface area is 100 to 350 m ^ 2 / g and the oil absorption is 100 to 3
Sepiolite in the range of 00 ml / 100 g is preferably used. If the specific surface area is smaller than this range, the cohesive force of the sludge is small, while if it is larger than this range, no further effect can be obtained. The fibrous sepiolite used in the present invention generally has a fiber diameter of 0.1 to 3 μm.
m, and the fiber length is preferably 5 to 20 μm.
If the fiber length is smaller than this range, dense and sedimentary flocs are not formed, while if it is larger than this range, it becomes bulky like asbestos and floats on sludge to achieve the object of the present invention. Have difficulty.

【0022】また下記Also below

【表1】にセピオライト(110 ℃で2時間の乾燥品)の
一般的化学組成の一例を示す。
Table 1 shows an example of the general chemical composition of sepiolite (dried at 110 ° C. for 2 hours).

【表1】 セピオライトの一般的化学組成 SiO2 52.50 (重量%) Mg O 22.8 Al2 O3 1.7 Fe2 O3 0.8 Ca O 0.8 H2 O^+ 10.5 H2 O^- 11.0[Table 1] General chemical composition of sepiolite SiO2 52.50 (wt%) Mg O22.8 Al2 O3 1.7 Fe2 O3 0.8 Ca O 0.8 H2 O ^ + 10.5 H2 O ^ -11.0

【0023】本発明が対象とする汚泥は任意の汚泥であ
つてよく、例えば染色の晒し工程、澱粉製造工程、ビ−
ル、ラ−メン、カンズメ等の食品工業、食肉加工業及び
紙、パルプ等の製紙工業等の排水処理における活性汚泥
処理法に用いることができる。 汚泥中に配合使用する
場合の(A)及び(D)の配合量は、(A)の好気性バ
クテリヤについては、バクテリヤの種類によって異なる
が、活性汚泥当たり100乃至600ppm、特に20
0乃至500ppmであるのがよく、一方(D)の繊維
状の粘土鉱物は汚泥固形分当たり固形分として300乃
至1200ppm、特に400乃至1000ppmであ
るのがよい。両成分の配合量が上記範囲よりも少ない場
合には、緻密で沈降性に優れた汚泥フロックを形成させ
ることが困難であり、一方上記範囲よりも多くても格別
の利点は達成されず、処理コストの点ではかえあつて不
利となる。また(B)及び(C)については、まず
(B)は(A)の栄養剤でありその配合量は50乃至5
00ppmの範囲で添加される、(C)は5乃至300
ppmの範囲で使用される。
The sludge targeted by the present invention may be any sludge, for example, a bleaching step of dyeing, a starch manufacturing step, and a beer.
It can be used for an activated sludge treatment method in wastewater treatment such as food industry such as le, ramen, and quince, meat processing industry and paper industry such as paper and pulp. The blending amounts of (A) and (D) when blended and used in the sludge vary depending on the type of the aerobic bacterium of (A), but it is 100 to 600 ppm per activated sludge, especially 20
The solid content of the fibrous clay mineral (D) is preferably 300 to 1200 ppm, and more preferably 400 to 1000 ppm. If the blending amount of both components is less than the above range, it is difficult to form a sludge floc that is dense and has excellent sedimentation properties, while if it is more than the above range, no particular advantage is achieved. It is disadvantageous in terms of cost. Regarding (B) and (C), first, (B) is the nutritional supplement of (A), and its blending amount is 50 to 5
(C) added in the range of 00 ppm is 5 to 300
Used in the ppm range.

【0024】[0024]

【実施例1】晒し工場排水処理の下記する性状の活性汚
泥に対して、本発明の処理剤を用いてその処理効果を検
討した。
Example 1 The treatment effect of the activated sludge having the following properties in the bleaching factory wastewater treatment was examined by using the treatment agent of the present invention.

【0025】[0025]

【表2】 活性汚泥の性状 性状項目 測定値 MLSS mg/l 3、720 MLVSS mg/l 3、132 SVI 207 COD ppm 308 PH 7.7 透明度 3.9 色度 280[Table 2] Properties of activated sludge Property Item Measurement value MLSS mg / l 3, 720 MLVSS mg / l 3, 132 SVI 207 COD ppm 308 PH 7.7 Transparency 3.9 Chromaticity 280

【0026】4本の1L容量のメスシリンダ−に上記活
性汚泥を各1L採り、下記
1 L of each of the above activated sludge was placed in each of 4 1 L capacity graduated cylinders.

【表3】の条件で各処理剤を添加し、エア−ポンプで7
日間連続して曝気をし、その間の活性汚泥の経過を結果
として
Add each treating agent under the conditions of [Table 3], and use an air-pump to
Aeration was continued for days, and the progress of activated sludge during that period was the result.

【表4】、[Table 4],

【表5】、[Table 5],

【表6】に示した。The results are shown in [Table 6].

【0027】[0027]

【表3】 汚泥の処理条件〔処理剤添加量(mg/l)〕 実験番号 (A)剤 (B)剤 (D)剤 1 0 0 0 2 200 200 0 3 0 0 1、000 4 200 200 1、000 (A)剤:一般好気性細菌、硝酸化成菌、放射菌群であ
り(C)剤の微生物酵素(プロテア−ゼ、セルラ−ゼ)
を含む、(B)剤:N、P元素を含む微生物栄養剤、
(D)剤:セピオライト
[Table 3] Sludge treatment conditions [Amount of treatment agent added (mg / l)] Experiment number (A) agent (B) agent (D) agent 1 0 0 0 2 2 200 200 0 3 0 0 1, 1,000 4 200 200 1,000 (A) agent: general aerobic bacteria, nitrifying bacteria, radiobacterium group (C) agent microbial enzyme (protease, cellulase)
(B) agent containing: a microbial nutrient containing N and P elements,
(D) Agent: Sepiolite

【0028】[0028]

【表4】、[Table 4],

【表5】、[Table 5],

【表6】に示した結果から、活性汚泥の経時の性状を比
べると曝気処理だけの実験 1に比べると汚泥の発泡、
汚泥フロックの沈降性、COD及び処理水の透視度、色
度等の向上に、本発明の各処理剤の組合せの効果が発揮
されており、特に実験 4から明らかなように、バルキ
ング現象を起こさないように活性汚泥に予め前処理的調
整を施すこしたうえで(D)剤のセピオライトが汚泥の
沈降促進剤として作用していることが良く理解される。
From the results shown in [Table 6], when comparing the characteristics of the activated sludge with time, the foaming of the sludge was found, as compared with Experiment 1 in which only aeration treatment was performed.
The combination of the treating agents of the present invention is effective in improving the sedimentation property of sludge flocs, the COD, the transparency of treated water, the chromaticity, and the like. In particular, as is clear from Experiment 4, the bulking phenomenon is caused. It is well understood that the sepiolite of the agent (D) acts as a settling accelerator of the sludge after the activated sludge has been subjected to pretreatment adjustment so as not to exist.

【0029】[0029]

【表4】 汚泥のpH及びSV30 曝気日数 曝気前 1日目 3日目 7日目 pH SV30 pH SV30 pH SV30 pH SV30 実験番号 1 7.8 77 7.6 75 7.6 73 7.5 70 2 − − 7.8 70 7.6 60 7.3 54 3 − − 7.8 53 7.6 45 7.4 46 4 − − 7.8 50 6.5 43 6.3 45 SV30:活性汚泥スラリ−の静置30分後の活性汚泥ス
ラリ−容量に対する沈降汚泥の容量%
[Table 4] pH and SV30 aeration days of sludge Before aeration 1st day 3rd day 7th day pH SV30 pH SV30 pH SV30 pH SV30 Experiment number 1 7.8 77 7.6 75 7.6 73 7.5 70 2 − − 7.8 70 7.6 60 7.3 54 3 − − 7.8 53 7.6 45 7.4 46 4 − − 7.8 50 6.5 43 6.3 45 SV30: Volume of sedimented sludge relative to volume of activated sludge slurry after 30 minutes of standing of activated sludge slurry

【0030】[0030]

【表5】 汚泥のCOD及び発泡状況 曝気日数 1日目 2日目 4日目 7日目 COD 発泡状況 COD 発泡状況 COD 発泡状況 COD 発泡状況 実験番号 1 80 × 60 × 52 × 48 × 2 67 × 54 × 41 ○ 39 ○ 3 70 × 55 × 43 △ 41 ○ 4 66 × 53 × 41 ◎ 33 ◎ 発砲状況の評価 ◎:泡の発生なし ○:泡の発生はあるが粘り気のない透明な泡 △:泡の発生はあり、淡褐色の泡 ×:泡の発生はあり、粘り気の強い茶褐色の泡[Table 5] COD and foaming status of sludge Aeration days 1st day 2nd day 4th day 7th day COD Foaming status COD Foaming status COD Foaming status COD Foaming status Experiment No. 1 80 × 60 × 52 × 48 × 2 67 × 54 × 41 ○ 39 ○ 3 70 × 55 × 43 △ 41 ○ 4 66 × 53 × 41 ◎ 33 ◎ Evaluation of firing condition ◎: No foam formation ○: Bubble formation but non-sticky transparent foam △: Bubbles occur, light brown foam x: Bubbles occur, viscous brown foam

【0031】[0031]

【表6】 汚泥の透視度及び色度 曝気日数 曝気前 7日目 透視度 色度 透明度 色度 実験番号 1 3.9 280 16.2 180 2 − − 28.6 60 3 − − 27.0 70 4 − − 30.0 40 [Table 6] Sludge visibility and chromaticity Aeration days 7 days before aeration Fluorescence chromaticity Transparency Chromaticity Experiment No. 1 3.9 280 16.2 180 2 − − 28.6 60 3 − − 27.0 70 4 − − 30.0 40

【0032】[0032]

【発明の効果】本発明によれば、活性汚泥に対して好気
性バクテリヤ、微生物酵素及びセピオライト等の繊維状
のケイ酸マグネシウム粘土鉱物を組合せて処理すること
により、活性汚泥法におけるバルキング現象が防止され
ると共に、緻密性、沈降性及び脱水性に優れた汚泥フロ
ックが形成されことから、活性汚泥処理法の通常のトラ
ブルが解消される。
According to the present invention, activated sludge is treated with a combination of aerobic bacteria, microbial enzymes and fibrous magnesium silicate clay minerals such as sepiolite to prevent the bulking phenomenon in the activated sludge process. At the same time, sludge flocs having excellent compactness, sedimentation and dewatering properties are formed, so that the usual troubles in the activated sludge treatment method are eliminated.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 四 橋 泓 和歌山県伊都郡かつらぎ町佐野963の5 (72)発明者 楠 見 雅 史 和歌山県和歌山市楠見中80 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor, Yohashi Tsuyoshi, 963-5, Sano, Katsuragi-cho, Ito-gun, Wakayama Prefecture (72) Masashi Kusumi, Masashi Kusumi, Wakayama, Wakayama

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】活性汚泥に対し、必要に応じて汚泥を安定
化させるために(A)好気性バクテリヤ、(B)窒素、
リン及びカリ成分からなる(A)に対する栄養剤及び
(C)微生物酵素を添加して成る該汚泥混合物系に、
(D)BET法比表面積が100乃至350m^2 /g
の範囲にある繊維状のケイ酸マグネシウム粘土鉱物を接
触させ、汚泥を沈降させることを特徴とする活性汚泥の
処理方法。
1. In order to stabilize the activated sludge, if necessary, (A) aerobic bacteria, (B) nitrogen,
The sludge mixture system comprising a nutrient for (A) consisting of phosphorus and potash and (C) a microbial enzyme,
(D) BET method specific surface area of 100 to 350 m ^ 2 / g
A method for treating activated sludge, which comprises contacting fibrous magnesium silicate clay minerals in the range of 1 to settle the sludge.
【請求項2】(D)なる繊維状のケイ酸マグネシウム粘
土鉱物の繊維子長が5乃至20μmであることを特徴と
する請求項1記載の活性汚泥の処理方法。
2. The method for treating activated sludge according to claim 1, wherein the fibrous magnesium silicate clay mineral (D) has a fiber length of 5 to 20 μm.
【請求項3】 (A)好気性バクテリヤ、(B)窒素、
リン及びカリ成分からなる(A)に対する栄養剤、
(C)微生物酵素及び(D)BET法比表面積が100
乃至300m^2 /gの範囲にある繊維状のケイ酸マグ
ネシウム粘土鉱物を組合せて成ることを特徴とする活性
汚泥用の処理剤。
3. (A) an aerobic bacterium, (B) nitrogen,
A nutritional supplement for (A) consisting of phosphorus and potassium components,
(C) Microbial enzyme and (D) BET method specific surface area is 100
A treatment agent for activated sludge, which is characterized by comprising a combination of fibrous magnesium silicate clay minerals in the range of up to 300 m ^ 2 / g.
JP25025091A 1991-09-04 1991-09-04 Activated sludge treatment method and treatment agent Expired - Fee Related JP2811129B2 (en)

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JP2811129B2 JP2811129B2 (en) 1998-10-15

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WO2006115199A1 (en) * 2005-04-21 2006-11-02 Ibiden Co., Ltd. Method of treating wastewater containing organic compound
JP2010082516A (en) * 2008-09-30 2010-04-15 Nippon Paper Industries Co Ltd Anaerobic treatment method for pulp wastewater
US8658411B2 (en) 2005-04-21 2014-02-25 Ibiden Co., Ltd. Method of treating wastewater containing organic compound
CN108658404A (en) * 2018-05-15 2018-10-16 湖南金旅环保股份有限公司 A kind of solid union biological agent and preparation method thereof administered for black and odorous water in-situ sediment remediation
CN116355882A (en) * 2023-04-10 2023-06-30 北京电子科技职业学院 Biological enzyme preparation for controlling filamentous fungus expanded sludge and preparation method and application thereof

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004344741A (en) * 2003-05-21 2004-12-09 Nippon Soda Co Ltd Sewage treatment method
WO2006115199A1 (en) * 2005-04-21 2006-11-02 Ibiden Co., Ltd. Method of treating wastewater containing organic compound
JPWO2006115199A1 (en) * 2005-04-21 2008-12-18 イビデン株式会社 Treatment method for waste liquid containing organic matter
US8658411B2 (en) 2005-04-21 2014-02-25 Ibiden Co., Ltd. Method of treating wastewater containing organic compound
JP2010082516A (en) * 2008-09-30 2010-04-15 Nippon Paper Industries Co Ltd Anaerobic treatment method for pulp wastewater
CN108658404A (en) * 2018-05-15 2018-10-16 湖南金旅环保股份有限公司 A kind of solid union biological agent and preparation method thereof administered for black and odorous water in-situ sediment remediation
CN116355882A (en) * 2023-04-10 2023-06-30 北京电子科技职业学院 Biological enzyme preparation for controlling filamentous fungus expanded sludge and preparation method and application thereof
CN116355882B (en) * 2023-04-10 2023-11-10 北京电子科技职业学院 Biological enzyme preparation for controlling filamentous fungus expanded sludge and preparation method and application thereof

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