JP3328139B2 - Method and apparatus for producing activated sludge - Google Patents

Method and apparatus for producing activated sludge

Info

Publication number
JP3328139B2
JP3328139B2 JP15829496A JP15829496A JP3328139B2 JP 3328139 B2 JP3328139 B2 JP 3328139B2 JP 15829496 A JP15829496 A JP 15829496A JP 15829496 A JP15829496 A JP 15829496A JP 3328139 B2 JP3328139 B2 JP 3328139B2
Authority
JP
Japan
Prior art keywords
activated sludge
extract
culture
tank
liquid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP15829496A
Other languages
Japanese (ja)
Other versions
JPH10488A (en
Inventor
進 中島
郁生 横山
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.)
Asahi Yukizai Corp
Original Assignee
Asahi Organic Chemicals Industry Co Ltd
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 Asahi Organic Chemicals Industry Co Ltd filed Critical Asahi Organic Chemicals Industry Co Ltd
Priority to JP15829496A priority Critical patent/JP3328139B2/en
Publication of JPH10488A publication Critical patent/JPH10488A/en
Application granted granted Critical
Publication of JP3328139B2 publication Critical patent/JP3328139B2/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
    • 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
    • Y02W10/20Sludge processing

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、生活雑排水、畜産
排水、水産加工排水、農産加工排水等の有機性排水を処
理するための活性汚泥の製造に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the production of activated sludge for treating organic wastewater such as household wastewater, livestock wastewater, processed marine wastewater, and processed agricultural wastewater.

【0002】[0002]

【従来の技術】従来、各種排水の生物的処理方法とし
て、活性汚泥法、散水ろ床等の好気的処理法及び無酸素
の条件下で分解処理する嫌気的処理法等が採用されてい
た。これらの処理法はいづれも、有機性排水を処理する
過程で自然に発生してくる微生物のみを利用して処理を
行うものである。しかしながら、これらの微生物に人為
的環境下で有機性排水を処理させることはいろいろな面
で限界に達しており、以下のような問題が発生してい
た。
2. Description of the Related Art Hitherto, as a biological treatment method of various wastewaters, an activated sludge method, an aerobic treatment method such as a trickling filter, an anaerobic treatment method of decomposing under anoxic conditions, and the like have been adopted. . In any of these treatment methods, treatment is performed using only microorganisms that naturally occur in the process of treating organic wastewater. However, treating these microorganisms with organic wastewater in an artificial environment has reached the limit in various aspects, and the following problems have occurred.

【0003】(1)有機性排水の処理の過程で低分子有
機酸、アンモニア、硫化水素、メルカプタン等の悪臭物
質が発生し周囲の環境を悪くしている。 (2)有機性排水の処理によって発生する汚泥の量が増
大し、その汚泥の処理に多くの費用が費やされている。 (3)発生した汚泥は、悪臭を再発生し、また濃縮不
良、脱水不良等により取り扱いが困難である。
(1) In the process of treating organic wastewater, malodorous substances such as low molecular weight organic acids, ammonia, hydrogen sulfide, and mercaptan are generated, and the surrounding environment is deteriorated. (2) The amount of sludge generated by the treatment of organic wastewater has increased, and a great deal of expense has been spent in treating the sludge. (3) The generated sludge regenerates an odor and is difficult to handle due to poor concentration, poor dehydration, and the like.

【0004】このような問題を解決するために種々の装
置が開発されているが代表的な装置としてリアクター方
式の活性汚泥の製造装置が特開平7−124580号公
報や特公平5−10999号公報等に開示されている。
これらは、リアクター内に収納されている微生物培養剤
(培養剤又は微生物代謝回路誘導剤)と、培養される被
培養液(又は有機性廃水)とを混合接触し、浄化能力の
高い有用菌を効率良く培養したり、又微生物の代謝反応
を有機性廃水の浄化に好効率の代謝回路に変換するため
の装置である。これらの装置で培養された微生物を各種
有機性排水処理に利用することにより、前述の悪臭や汚
泥の質的悪化等の諸問題を解消できるというものであ
る。
Various apparatuses have been developed to solve such problems. As a typical apparatus, a reactor type activated sludge producing apparatus is disclosed in Japanese Patent Application Laid-Open No. 7-124580 and Japanese Patent Publication No. 5-10999. Etc.
These are mixed contact of a microorganism culturing agent (a culturing agent or a microorganism metabolic circuit inducer) housed in a reactor with a liquid to be cultured (or an organic wastewater) to form useful bacteria having a high purification ability. It is a device for efficiently culturing and converting the metabolic reaction of microorganisms into a metabolic circuit that is efficient for purification of organic wastewater. By utilizing microorganisms cultured in these devices for various organic wastewater treatments, it is possible to solve the above-mentioned problems such as the bad odor and the deterioration of the quality of sludge.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、これら
の装置には目詰まりという問題がある。これらの装置は
いづれも微生物培養剤と被培養液とを直接接触してお
り、時間の経過とともに微生物培養剤の表面、微生物培
養剤間の隙間及び微生物培養剤を保持するための金網や
パンチングメタル等の隙間に被培養液中の固着物質や塊
状物質等が次第に蓄積する。蓄積が進行すると目詰まり
も相乗的に進行し、被培養液と微生物培養剤との接触が
不良となったり、被培養液の酸素濃度が不均一になる等
して、リアクターの処理効率が低下してくる。また目詰
まりを起こした微生物培養剤や金網等を定期的に洗浄、
交換等しなければならなくなり、それだけ維持管理の煩
雑さ及びランニングコストの増大につながることにな
る。
However, these devices have a problem of clogging. All of these devices directly contact the microbial culture medium and the medium to be cultured, and with the passage of time, the surface of the microbial culture medium, the gap between the microbial culture medium, and a wire mesh or punching metal for holding the microbial culture medium In the gaps of the culture medium, the adhered substance and the lump substance in the culture solution gradually accumulate. As the accumulation progresses, clogging also progresses synergistically, resulting in poor contact between the liquid to be cultured and the microbial culture medium and the uneven oxygen concentration in the liquid to be cultured, resulting in a decrease in the processing efficiency of the reactor. Will come. Periodically clean the clogged microbial culture media and wire mesh
It is necessary to replace the battery, which leads to complicated maintenance and running costs.

【0006】もう一つの問題は、微生物培養剤が減耗す
るということである。特に特公平5−10999に開示
されている装置に見られる問題である。この装置は、微
生物培養剤の下方側から曝気を行なっており、空気泡の
流れが直接微生物培養剤へ衝突するために、微生物培養
剤の減耗が早まる構造となっている。従って減耗した分
量の微生物培養剤は新たに補充する必要が生じるためそ
れだけ維持管理に手間がかかり、ランニングコストも高
くなる。
Another problem is that the microbial culture is depleted. This is a problem particularly found in the device disclosed in Japanese Patent Publication No. 5-10999. This device performs aeration from the lower side of the microorganism culture agent, and has a structure in which the flow of air bubbles directly collides with the microorganism culture agent, so that the depletion of the microorganism culture agent is accelerated. Therefore, it is necessary to newly replenish the depleted amount of the microorganism cultivation agent, so that maintenance and management are troublesome and the running cost is also increased.

【0007】本発明は以上のような従来技術の問題点に
鑑みなされたものでその目的は、目詰まりの心配がな
く、かつ微生物培養剤の減耗を最小限に抑えることによ
り、培養効率に優れ、維持管理の簡略化及びランニング
コストの減少を可能にした活性汚泥の製造方法及び装置
を提供することにある。
[0007] The present invention has been made in view of the above-mentioned problems of the prior art, and has as its object to improve the cultivation efficiency by eliminating the risk of clogging and minimizing the depletion of the microorganism culture medium. Another object of the present invention is to provide a method and an apparatus for producing activated sludge, which enable simplified maintenance and reduced running costs.

【0008】[0008]

【課題を解決するための手段】本発明によれば、上記の
課題を解決するため、抽出液用溶媒を抽出槽内で微生物
培養剤と接触させて抽出液を生成し、得られた抽出液を
培養槽に移し、ここで被培養液と混合させ好気的条件下
で培養して活性汚泥を生成する、活性汚泥の製造方法
と、抽出液用溶剤の流入口と抽出液の流出口とを有し内
部に微生物培養剤が収納されている抽出槽と、前記抽出
液流出口に接続される抽出液流入口と被培養液流入口と
を有し内部に散気装置が設けられている培養槽とからな
る活性汚泥の製造装置とが提供される。
According to the present invention, in order to solve the above-mentioned problems, an extract is produced by bringing a solvent for an extract into contact with a microorganism culturing agent in an extraction tank. Into an incubation tank, where it is mixed with the liquid to be cultured and cultured under aerobic conditions to produce activated sludge, a method for producing activated sludge, an inlet for an extractant solvent and an outlet for an extract. And an extraction tank in which a microbial culture medium is stored, an extractant inlet connected to the extract outlet, and a culture inlet, and an air diffuser is provided therein. An apparatus for producing activated sludge comprising a culture tank.

【0009】尚、本発明における「活性汚泥」とは、活
性汚泥法で使用される「微生物活性の高い汚泥」ではな
く、微生物培養剤の作用による被培養液の微生物活性を
高めた培養液や有用菌が培養された培養液及び代謝回路
の変換した微生物が培養された培養液等を意味する。
The "activated sludge" in the present invention is not a "sludge having a high microbial activity" used in the activated sludge method, but a culture solution in which the microbial activity of a liquid to be cultured is increased by the action of a microbial culture agent. It refers to a culture solution in which useful bacteria are cultured, a culture solution in which microorganisms whose metabolic circuit is converted are cultured, and the like.

【0010】[0010]

【発明の実施の形態】以下、本発明について、実施態様
を示す図面に基づき説明するが、本発明が本実施態様に
限定されないことは言うまでもない。図1において、1
は抽出槽で、2は培養槽であり、抽出液移送管3により
両槽が連通されている。4は円筒状に構成された抽出槽
本体であり、5は抽出槽本体4内部にその内壁と隙間が
ないように配設され、微生物培養剤6が充填される円筒
体である。円筒体5の上下は開口しており、その上下端
部分には金網あるいはパンチングメタル等からなる底板
7及び天板8が取り付け、微生物培養剤6を円筒体5内
に収納する働きをしている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described with reference to the drawings showing embodiments, but it is needless to say that the present invention is not limited to the embodiments. In FIG. 1, 1
Denotes an extraction tank, 2 denotes a culture tank, and both tanks are connected by an extract transfer pipe 3. Reference numeral 4 denotes a cylindrical extraction tank main body, and reference numeral 5 denotes a cylindrical body which is disposed inside the extraction tank main body 4 so as not to have a gap with its inner wall, and is filled with a microorganism culturing agent 6. The upper and lower ends of the cylindrical body 5 are open, and a bottom plate 7 and a top plate 8 made of wire mesh or punched metal are attached to the upper and lower ends thereof, and serve to store the microorganism culture agent 6 in the cylindrical body 5. .

【0011】円筒体5に充填される微生物培養剤6は、
活性汚泥を製造するための有効な成分を含有した物質で
あり、具体的にはペレット状の有用微生物培養剤、遠赤
外線セラミック、岩石、鉱物、腐植物を含む物質、有用
菌以外の微生物に抗菌作用を有する物質及びこれらの混
合物等が好適なものとして挙げられるが、これに限定さ
れるものではない。抽出槽本体4の上部側には抽出液の
溶媒9が流入するための流入口10、余分な溶媒または
抽出液を抽出槽本体4から排出するためのオーバーフロ
ー用排水口11及び抽出槽本体4に流入する溶媒9の流
入量を設定するための水位センサー12が設けられてい
る。
The microorganism culturing agent 6 filled in the cylindrical body 5 is
A substance containing an effective ingredient for producing activated sludge.Specifically, it is a useful microbial culture agent in the form of pellets, far-infrared ceramics, rocks, minerals, substances containing humus, and antibacterial against microorganisms other than useful bacteria. Suitable substances include substances having an effect and mixtures thereof, but are not limited thereto. On the upper side of the extraction tank main body 4, an inflow port 10 through which the solvent 9 of the extraction liquid flows, an overflow drain port 11 for discharging excess solvent or extract from the extraction tank main body 4, and an extraction tank main body 4. A water level sensor 12 for setting the inflow amount of the flowing solvent 9 is provided.

【0012】ここで使用される溶媒9は微生物培養剤6
から有効な成分を抽出する働きをするものであり、具体
的には水や下水処理施設内の処理水、生下水、曝気槽内
混合液、嫌気槽内混合液等が挙げられ単独あるいは混合
して使用される。又、特に前記腐植物を含んだ物質から
主に有機成分を抽出する場合には、溶媒のpHを中性又は
アルカリ性側に設定すると抽出効率が良くなる。
The solvent 9 used here is a microorganism culturing agent 6
It works to extract effective components from water, specifically, water or treated water in a sewage treatment facility, raw sewage, a mixed solution in an aeration tank, a mixed solution in an anaerobic tank, and the like, alone or mixed. Used. In particular, in the case where mainly organic components are extracted from the substance containing the humus, the extraction efficiency is improved by setting the pH of the solvent to a neutral or alkaline side.

【0013】13は抽出槽本体4の外部に設けられた循
環流発生装置であり、円筒体5の上下位置で抽出槽本体
4と接続されている循環流管14,15と連結されてい
る。循環流発生装置13は、抽出槽本体4内に循環流を
強制的に発生させ、溶媒9と微生物培養剤6とを効率的
に接触させることにより、抽出効率を大幅に高める作用
をしている。図1においては、循環流は反時計まわり方
向(矢印)の例が示されているが、時計回り方向として
も構わない。循環流発生装置としては、エアリフトポン
プや水流ポンプ等があるが、循環流を発生できるもので
あればいずれでもよい。もちろん、抽出効率の高い微生
物培養剤を使用するとき、あるいは緩慢に抽出したい場
合等は、前記循環流発生装置を設置せずに静置状態で抽
出してもかまわない。
Reference numeral 13 denotes a circulating flow generator provided outside the main body 4 of the extraction tank, which is connected to circulating flow pipes 14 and 15 connected to the main body 4 of the extraction tank at upper and lower positions of the cylindrical body 5. The circulating flow generating device 13 has a function of forcibly generating a circulating flow in the extraction tank main body 4 and effectively bringing the solvent 9 and the microorganism culturing agent 6 into contact with each other, thereby greatly improving the extraction efficiency. . FIG. 1 shows an example in which the circulating flow is in a counterclockwise direction (arrow), but may be in a clockwise direction. Examples of the circulating flow generator include an air lift pump and a water flow pump, but any device can be used as long as it can generate a circulating flow. Of course, when a microorganism culturing agent having high extraction efficiency is used or when it is desired to perform extraction slowly, the extraction may be performed in a stationary state without installing the circulating flow generator.

【0014】また、図2に示すように、抽出槽本体4の
内部に撹拌装置16を設けるとさらに抽出効率が良くな
る。また図3に示すように、ドーナツ型円筒体17内側
の中空部分の中央に撹拌装置を設置し、溶媒に強制的な
回転流を発生させることにより、溶媒と微生物培養剤と
の接触を効率良く行わせることもできる。
Further, as shown in FIG. 2, when the stirring device 16 is provided inside the extraction tank main body 4, the extraction efficiency is further improved. As shown in FIG. 3, a stirrer is installed in the center of the hollow portion inside the donut-shaped cylinder 17 to generate a forced rotational flow in the solvent, so that the contact between the solvent and the microorganism culturing agent is efficiently performed. It can also be done.

【0015】抽出槽1で得られた抽出液18は、水流ポ
ンプ19が接続された抽出液移送管3により抽出液の流
入口28を通って培養槽2へ移送される。20は、円筒
状に構成された培養槽本体であり、培養槽本体20の上
部側には汚泥のような被培養液21が流入する流入口2
2、余分な被培養液21を培養槽2外部に排出するオー
バーフロー用排水口23及び被培養液21と前記抽出液
18の流入量を規定するための水位センサー24が設け
られ、一方底部側には生成された活性汚泥を培養槽2外
部に取り出す取り出し口25が設けられている。
The extract 18 obtained in the extraction tank 1 is transferred to the culture tank 2 through an extract inlet port 28 by an extract transfer pipe 3 to which a water flow pump 19 is connected. Reference numeral 20 denotes a culture tank main body formed in a cylindrical shape, and an inflow port 2 through which a culture liquid 21 such as sludge flows into an upper portion of the culture tank main body 20.
2. An overflow drain 23 for discharging excess culture liquid 21 to the outside of the culture tank 2 and a water level sensor 24 for regulating the flow rates of the culture liquid 21 and the extract 18 are provided. Is provided with an outlet 25 for taking out the generated activated sludge to the outside of the culture tank 2.

【0016】また、培養槽2内を好気的環境に調整する
ために散気装置26が培養槽2内下部側に取りつけられ
ている。また、被培養液21を培養槽本体20内で均一
に循環させるための撹拌装置27が培養槽2内下部側中
央に取りつけられている。培養槽2には、基本的には微
生物培養剤6を収納しないが活性汚泥の製造能力を高め
る場合や、製造時間を短縮したい場合等には、適宜微生
物培養剤を投入してもよい。
In order to adjust the inside of the culture tank 2 to an aerobic environment, an air diffuser 26 is mounted on the lower side of the culture tank 2. A stirrer 27 for uniformly circulating the culture solution 21 in the culture vessel main body 20 is attached to the lower center of the culture vessel 2. The culture tank 2 does not basically contain the microorganism culture agent 6, but may be appropriately charged with a microorganism culture agent when the production capacity of activated sludge is to be increased or when the production time is desired to be reduced.

【0017】次に本実施態様の活性汚泥の製造装置の作
用について説明する。図1において、図示しないポンプ
等により溶媒9を溶媒流入口10から抽出槽1へ水位セ
ンサー12で設定した流量だけ流入させる。水位センサ
ー12の作動不良で規定量以上の溶媒9が抽出槽1に流
入した場合は、オーバーフロー排水口11から余分量の
溶媒9が抽出槽1外へ排出される。抽出槽1に、規定量
の溶媒9が流入した後、循環流発生装置13を作動さ
せ、溶媒9と微生物培養剤6とをタイマーで設定した時
間接触させる。溶媒9は微生物培養剤6の中や微生物培
養剤6間の隙間を通り、微生物培養剤6と接触し微生物
培養剤6の有効成分を溶解しながら循環させられ抽出液
18を生成させる。
Next, the operation of the apparatus for producing activated sludge of this embodiment will be described. In FIG. 1, a solvent 9 is caused to flow from a solvent inlet 10 into an extraction tank 1 by a pump (not shown) at a flow rate set by a water level sensor 12. When the solvent 9 in a specified amount or more flows into the extraction tank 1 due to malfunction of the water level sensor 12, an extra amount of the solvent 9 is discharged from the overflow drain 11 to the outside of the extraction tank 1. After a specified amount of the solvent 9 flows into the extraction tank 1, the circulating flow generator 13 is operated to bring the solvent 9 into contact with the microorganism culture agent 6 for a time set by a timer. The solvent 9 passes through the inside of the microbial culture medium 6 and the gap between the microbial culture medium 6, contacts the microbial culture medium 6, circulates while dissolving the active ingredient of the microbial culture medium 6, and generates the extract 18.

【0018】次に、図示しないポンプ等により汚泥のよ
うな被培養液21を流入口22から培養槽2へ水位セン
サー24で規定した量だけ流入させる。水位センサー2
4の作動不良で規定量以上の被培養液21が培養槽2に
流入した場合は、オーバーフロー排水口23から余分量
の被培養液21が培養槽2外へ排出される。培養槽2内
に規定量の被培養液21が流入した後、前記生成された
抽出液18を水流ポンプ19により抽出液移送管3を介
して水位センサー24で規定された量だけ培養槽2へ移
送させる。この場合も、水位センサー24の作動不良で
規定量以上の抽出液18が流入した場合は、オーバーフ
ロー排水口23から余分量の抽出液18が培養槽2外部
に排出される。
Next, a culture liquid 21 such as sludge is caused to flow into the culture tank 2 from the inflow port 22 by an amount not specified by the water level sensor 24 by a pump or the like (not shown). Water level sensor 2
When the culture medium 21 having a predetermined amount or more flows into the culture tank 2 due to the operation failure of Step 4, an excessive amount of the culture medium 21 is discharged out of the culture tank 2 from the overflow drain 23. After a specified amount of the culture solution 21 flows into the culture tank 2, the generated extract 18 is supplied to the culture tank 2 by the water flow pump 19 via the extract transfer pipe 3 by an amount specified by the water level sensor 24. Transfer. Also in this case, when the extract 18 in a specified amount or more flows in due to the malfunction of the water level sensor 24, an extra amount of the extract 18 is discharged from the overflow drain 23 to the outside of the culture tank 2.

【0019】規定量の抽出液18が培養槽2へ移送され
た後は、抽出槽1内には培養槽2に移送した抽出液量分
が減少しているので、前記説明した様に流入口10から
新たに溶媒9を抽出槽1へ補充させ、再度抽出を開始す
る。次に、培養槽2において被培養液21と抽出液18
の混合溶液を好気的条件下で効率良く培養させるため
に、散気装置26及び撹拌装置27を作動させる。タイ
マーで設定した時間培養させ、目的とする活性汚泥を生
成させる。
After the specified amount of the extract 18 has been transferred to the culture tank 2, the amount of the extract transferred to the culture tank 2 is reduced in the extraction tank 1. The solvent 9 is newly replenished to the extraction tank 1 from 10, and the extraction is started again. Next, the culture solution 21 and the extract 18 are
In order to efficiently culture the mixed solution under the aerobic condition, the air diffuser 26 and the stirring device 27 are operated. Incubate for the time set by the timer to generate the desired activated sludge.

【0020】生成された活性汚泥は、取り出し口25か
ら培養槽2外部へと取出され各種有機性排水の浄化に利
用される。この場合取出される活性汚泥の量は、種汚泥
を残すことから培養槽2の容量に対し半量程度とするこ
とが好ましい。培養槽2にて減少した活性汚泥分は、被
培養液21及び新たに生成された抽出液18により補充
される。この一連の工程がタイマーで設定した時間毎に
繰り返される。
The generated activated sludge is taken out from the take-out port 25 to the outside of the culture tank 2 and used for purifying various organic wastewater. In this case, the amount of the activated sludge to be taken out is preferably about half the capacity of the culture tank 2 to leave seed sludge. The activated sludge reduced in the culture tank 2 is replenished by the liquid to be cultured 21 and the newly generated extract 18. This series of steps is repeated every time set by the timer.

【0021】抽出槽1に収納される微生物培養剤6の充
填量は、微生物培養剤6の種類により適当に調整される
が、微生物培養剤6として腐植物を含む物質を使用する
場合は、抽出槽1の容量に対し重量比で1:50前後に
設定することが好ましい。また、抽出時間、培養時間は
使用する微生物培養剤6に応じて適宜調整することがで
きる。特に、微生物培養剤6として腐植物を含む物質を
用いる場合は、抽出時間、培養時間とも24時間以上と
することが好ましい。もちろん、抽出時間と培養時間を
同じにする必要はなく、培養時間が抽出時間と比較して
短い場合は、培養回数:抽出回数を2:1等に適宜設定
することも可能である。また、培養槽2での抽出液量と
汚泥量の比率は、1:10から1:1の間に設定するこ
とが好ましいが、これに限定されない。
The amount of the microbial culture agent 6 to be stored in the extraction tank 1 is appropriately adjusted depending on the type of the microbial culture agent 6. It is preferable to set the weight ratio of the tank 1 to about 1:50. Further, the extraction time and the culture time can be appropriately adjusted according to the microorganism culture agent 6 to be used. In particular, when a substance containing a humic substance is used as the microorganism culturing agent 6, it is preferable that both the extraction time and the culturing time be 24 hours or more. Of course, it is not necessary to make the extraction time and the culturing time the same, and when the culturing time is shorter than the extraction time, the number of culturing times: the number of culturing times can be appropriately set to 2: 1 or the like. The ratio between the amount of extract and the amount of sludge in the culture tank 2 is preferably set between 1:10 and 1: 1, but is not limited to this.

【0022】また、以上示した実施態様ではこれらの一
種の過程をバッチ方式により説明したが、連続方式にし
ても構わない。即ち、抽出槽1に溶媒9を連続して流入
させ、抽出槽1からオーバーフローした抽出液を連続し
て培養槽2に移送して、かつ培養槽2からオーバーフロ
ーした活性汚泥を連続的に取出し、各種有機性排水の浄
化に利用することも可能である。
Further, in the embodiment described above, one kind of these processes has been described by the batch system, but may be a continuous system. That is, the solvent 9 is continuously flowed into the extraction tank 1, the extract liquid overflowing from the extraction tank 1 is continuously transferred to the culture tank 2, and the activated sludge overflowing from the culture tank 2 is continuously taken out. It can also be used to purify various organic wastewaters.

【0023】次に本発明の活性汚泥の製造装置を排水処
理施設に設置した例を図4に示す。排水処理施設内に流
入してきた有機性排水は、スクリーン、沈殿池及び微生
物等による処理を行う反応工程を経由して、沈殿工程で
処理水と汚泥とに分離される。処理水の一部は、抽出液
の溶媒として利用されるために抽出槽内に取り込まれ、
また汚泥は濃縮工程で濃縮後、一部を被培養液として利
用するために培養槽内に取り込まれる。抽出液により活
性化され、製造された活性汚泥は反応工程中の各処理槽
へと戻され、結果的に全工程に活性汚泥の濃度が高ま
り、処理効率を高めるものである。
Next, FIG. 4 shows an example in which the activated sludge production apparatus of the present invention is installed in a wastewater treatment facility. The organic wastewater that has flowed into the wastewater treatment facility is separated into treated water and sludge in the sedimentation step via a screen, a sedimentation pond, and a reaction step for performing treatment with microorganisms and the like. Part of the treated water is taken into the extraction tank to be used as a solvent for the extract,
After the sludge is concentrated in the concentration step, a part of the sludge is taken into the culture tank to be used as a liquid to be cultured. The activated sludge activated and produced by the extract is returned to each treatment tank in the reaction step, and as a result, the concentration of the activated sludge is increased in all the steps, thereby increasing the treatment efficiency.

【0024】[0024]

【発明の効果】以上の説明から明らかなように本発明の
活性汚泥の製造方法及び装置によれば、微生物培養剤の
目詰まり、目詰まりに伴う培養効率の低下及び培養剤の
減耗を可能な限り少なくすることができる。従って、培
養剤の洗浄作業、交換作業等有する人材、時間等も大幅
に節減することが可能となり維持管理の簡略化及びラン
ニングコストの低減にも大きく貢献することから本発明
は極めて実用的なものである。
As is apparent from the above description, according to the method and apparatus for producing activated sludge of the present invention, clogging of a microorganism culture agent, reduction of culture efficiency due to clogging, and consumption of the culture agent can be achieved. It can be as small as possible. Therefore, the present invention is extremely practical because it is possible to greatly reduce human resources, time, and the like having a cleaning operation and a replacement operation of a culture medium, which greatly contributes to simplification of maintenance and reduction of running costs. It is.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明装置の一実施態様を示す活性汚泥の製造
装置の縦断面図である。
FIG. 1 is a longitudinal sectional view of an apparatus for producing activated sludge, showing one embodiment of the apparatus of the present invention.

【図2】本発明装置における抽出槽の他の例を示す縦断
面図である。
FIG. 2 is a longitudinal sectional view showing another example of the extraction tank in the apparatus of the present invention.

【図3】本発明装置における抽出槽のさらに他の例を示
す縦断面図である。
FIG. 3 is a vertical sectional view showing still another example of the extraction tank in the apparatus of the present invention.

【図4】本発明装置を排水処理施設に活用した場合の模
試図である。
FIG. 4 is a schematic diagram illustrating a case where the apparatus of the present invention is used in a wastewater treatment facility.

【符号の説明】[Explanation of symbols]

1…抽出槽 2…培養槽 3…抽出液移送管 4…抽出液本体 5…円筒体 6…微生物培養剤 7…底板 8…天板 9…溶媒 10…流入口 11…オーバーフロー用排水口 12…水位センサー 13…循環流発生装置 14…循環流管 15…循環流管 16…撹拌装置 17…ドーナツ型円筒体 18…抽出液 19…水流ポンプ 20…培養槽本体 21…被培養液 22…流入口 23…オーバーフロー用排水口 24…水位センサー 25…取り出し口 26…散気装置 27…撹拌装置 28…抽出液流入口 DESCRIPTION OF SYMBOLS 1 ... Extraction tank 2 ... Culture tank 3 ... Extract liquid transfer pipe 4 ... Extract liquid main body 5 ... Cylindrical body 6 ... Microorganism culture agent 7 ... Bottom plate 8 ... Top plate 9 ... Solvent 10 ... Inflow port 11 ... Overflow drain port 12 ... Water level sensor 13 ... Circulating flow generator 14 ... Circulating flow tube 15 ... Circulating flow tube 16 ... Stirring device 17 ... Doughnut type cylinder 18 ... Extracted liquid 19 ... Water flow pump 20 ... Culture tank body 21 ... Cultivated liquid 22 ... Inlet 23 ... overflow drain 24 ... water level sensor 25 ... outlet 26 ... diffuser 27 ... stirrer 28 ... extract liquid inlet

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平10−486(JP,A) 特開 平10−487(JP,A) 特開 平7−256269(JP,A) 特開 昭63−156598(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 3/12 C02F 3/00 C12N 1/00 ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-10-486 (JP, A) JP-A-10-487 (JP, A) JP-A-7-256269 (JP, A) JP-A-63- 156598 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) C02F 3/12 C02F 3/00 C12N 1/00

Claims (11)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 抽出液用溶媒を抽出槽内で微生物培養剤
と接触させて抽出液を生成し、得られた抽出液を培養槽
に移し、ここで被培養液と混合させ好気的条件下で培養
して活性汚泥を生成する、活性汚泥の製造方法。
1. A solvent for an extract is brought into contact with a microorganism culturing agent in an extraction tank to produce an extract, and the obtained extract is transferred to a culture tank, where it is mixed with a liquid to be cultured and subjected to aerobic conditions. A method for producing activated sludge, wherein the activated sludge is produced by culturing under activated sludge.
【請求項2】 微生物培養剤が、ペレット状の有用微生
物培養剤、遠赤外線セラミック、岩石、鉱物、腐植物を
含む物質、もしくは有用菌以外の微生物に抗菌作用を有
する物質、又はこれら物質の混合物である請求項1に記
載の活性汚泥の製造方法。
2. The microorganism culturing agent is a useful microorganism culturing agent in the form of a pellet, a substance containing far-infrared ceramics, rocks, minerals, humus, a substance having an antibacterial effect on microorganisms other than useful bacteria, or a mixture of these substances. The method for producing activated sludge according to claim 1, wherein
【請求項3】 抽出液用溶媒が水もしくは有機性排水又
はその混合物である請求項1に記載の活性汚泥の製造方
法。
3. The method for producing activated sludge according to claim 1, wherein the solvent for the extract is water or organic wastewater or a mixture thereof.
【請求項4】 被培養液が汚泥である請求項1に記載の
活性汚泥の製造方法。
4. The method for producing activated sludge according to claim 1, wherein the liquid to be cultured is sludge.
【請求項5】 抽出液用溶媒の流入口と抽出液の流出口
とを有し内部に微生物培養剤が収納されている抽出槽
と、前記抽出液流出口に接続される抽出液流入口と被培
養液流入口とを有し内部に散気装置が設けられている培
養槽とからなる活性汚泥の製造装置。
5. An extraction tank having an inlet for an extract solvent and an outlet for an extract and containing a microorganism culture agent therein, and an extract inlet connected to the extract outlet. An activated sludge producing apparatus, comprising: a culture tank having an inlet for a liquid to be cultured and an aeration device provided therein.
【請求項6】 抽出槽に、抽出槽内の液を循環させる装
置を取付けた請求項5に記載の活性汚泥の製造装置。
6. The activated sludge production apparatus according to claim 5, wherein a device for circulating the liquid in the extraction tank is attached to the extraction tank.
【請求項7】 抽出槽内に液の撹拌装置を設けた請求項
5に記載の活性汚泥の製造装置。
7. The activated sludge production apparatus according to claim 5, wherein a liquid stirring device is provided in the extraction tank.
【請求項8】 微生物培養剤が、ペレット状の有用微生
物培養剤、遠赤外線セラミック、岩石、鉱物、腐植物を
含む物質、もしくは有用菌以外の微生物に抗菌作用を有
する物質、又はこれら物質の混合物である請求項5に記
載の活性汚泥の製造装置。
8. The microbial culture medium is a useful microbial culture medium in the form of a pellet, a substance containing far-infrared ceramics, rocks, minerals, humus, a substance having an antibacterial effect on microorganisms other than useful microorganisms, or a mixture of these substances. The activated sludge production apparatus according to claim 5, wherein
【請求項9】 培養槽の内部に液の撹拌装置を設けた請
求項5に記載の活性汚泥の製造装置。
9. The activated sludge production apparatus according to claim 5, wherein a liquid stirring device is provided inside the culture tank.
【請求項10】 培養槽の底部に活性汚泥の取り出し口
を設けた請求項5に記載の活性汚泥の製造装置。
10. The activated sludge producing apparatus according to claim 5, wherein an outlet for taking out activated sludge is provided at the bottom of the culture tank.
【請求項11】 抽出槽と培養槽とをポンプを介して移
送管で接続した請求項5に記載の活性汚泥の製造装置。
11. The activated sludge production apparatus according to claim 5, wherein the extraction tank and the culture tank are connected by a transfer pipe via a pump.
JP15829496A 1996-06-19 1996-06-19 Method and apparatus for producing activated sludge Expired - Fee Related JP3328139B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15829496A JP3328139B2 (en) 1996-06-19 1996-06-19 Method and apparatus for producing activated sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15829496A JP3328139B2 (en) 1996-06-19 1996-06-19 Method and apparatus for producing activated sludge

Publications (2)

Publication Number Publication Date
JPH10488A JPH10488A (en) 1998-01-06
JP3328139B2 true JP3328139B2 (en) 2002-09-24

Family

ID=15668472

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15829496A Expired - Fee Related JP3328139B2 (en) 1996-06-19 1996-06-19 Method and apparatus for producing activated sludge

Country Status (1)

Country Link
JP (1) JP3328139B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101913711A (en) * 2010-05-26 2010-12-15 优泥可环保技术有限公司 Sludge modifying machine and water treatment facility provided with sludge modifying machines in parallel

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6253442B2 (en) * 2014-02-18 2017-12-27 クボタ環境サ−ビス株式会社 Biological treatment reactor, water treatment facility, and biological treatment reactor operating method
JP6285242B2 (en) * 2014-03-28 2018-02-28 クボタ環境サ−ビス株式会社 Waste water treatment facility and waste water treatment method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101913711A (en) * 2010-05-26 2010-12-15 优泥可环保技术有限公司 Sludge modifying machine and water treatment facility provided with sludge modifying machines in parallel

Also Published As

Publication number Publication date
JPH10488A (en) 1998-01-06

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