JPH10487A - Apparatus for producing activated sludge - Google Patents

Apparatus for producing activated sludge

Info

Publication number
JPH10487A
JPH10487A JP15825596A JP15825596A JPH10487A JP H10487 A JPH10487 A JP H10487A JP 15825596 A JP15825596 A JP 15825596A JP 15825596 A JP15825596 A JP 15825596A JP H10487 A JPH10487 A JP H10487A
Authority
JP
Japan
Prior art keywords
circulating flow
activated sludge
agent
culture tank
main body
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.)
Pending
Application number
JP15825596A
Other languages
Japanese (ja)
Inventor
Takeshi Shudo
健 首藤
Ikuo Yokoyama
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 JP15825596A priority Critical patent/JPH10487A/en
Publication of JPH10487A publication Critical patent/JPH10487A/en
Pending legal-status Critical Current

Links

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

  • Activated Sludge Processes (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable the abrasion of a microorganism cultivating agent to be minimum by connecting a culture tank for contacting a microorganism cultivating agent with liquid to be cultivated under aerobic conditions with a circulating flow generator installed outside the culture tank by a transfer pipe and generating the circulating flow of the liquid in the culture tank forcibly. SOLUTION: A cylinder 4 filled with a microorganism cultivating agent 5 to eliminate the gap of an inner surface is installed in the cylindrical main body 3 of a culture tank 1, the upper and lower parts of the cylinder 4 are opened, a roof 6 consisting of gauze, etc., and a bottom plate 7 are installed in the upper and lower end parts, and the agent 5 is placed in the cylinder 4. Besides, a supply port 8 for liquid to be cultivated and a discharge opening 9 for overflow are formed in the upper part of the main body 3, and a discharge opening for cultivated active sludge and a discharge valve 11 are installed on the lower part side of the main body 3. Moreover, installation openings 14, 15 for connecting a circulating flow generator 2 installed outside the tank 1 are formed on the sides of the main body 3 which are positioned above and below the cylinder 4, and the circulating flow is generated forcibly in the tank 1 by the generator 2.

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、農産加工排水等の有機性排水を処理する際に
用いられる活性汚泥の製造装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for producing activated sludge used in treating organic wastewater such as household wastewater, livestock wastewater, fishery, agricultural processing wastewater and the like.

【0002】[0002]

【従来の技術】従来、前記各種排水の処理法には、活性
汚泥法、接触曝気法、散水ろ床法等が採用されている。
その処理工程は反応工程と沈澱工程とからなり、この反
応工程の方式によりその処理法が大別される。
2. Description of the Related Art Conventionally, activated sludge method, contact aeration method, sprinkling filter method and the like have been adopted as a method for treating the above-mentioned various wastewaters.
The treatment step includes a reaction step and a precipitation step, and the treatment method is roughly classified according to the type of the reaction step.

【0003】この中で、多く採用されている活性汚泥法
においては、反応工程で生成された活性汚泥は沈澱工程
で上澄み部分と汚泥部分に分離され、この上澄み部分は
放流水となり、汚泥部分の一部は活性汚泥濃度を一定に
調整するために反応工程に戻されて再度用いられ、残り
については、濃縮され処理系外へと搬出される。
Among them, in the activated sludge method which is widely used, the activated sludge generated in the reaction step is separated into a supernatant part and a sludge part in a precipitation step, and the supernatant part becomes effluent water, and the sludge part is discharged. Part of the sludge is returned to the reaction step and used again to adjust the concentration of the activated sludge to a constant level, and the rest is concentrated and carried out of the treatment system.

【0004】しかし、この様な排水処理法においては硫
化水素等による悪臭の発生、発生汚泥の増加、その汚泥
からの悪臭の発生などの問題点があった。そこで、これ
らの問題点を解決するために、腐植土壌などを微生物培
養剤として、前記処理工程で発生する汚泥を活性化さ
せ、活性汚泥を作り、これを反応工程中に戻すという方
法が開発され、該活性汚泥の製造装置の一例が特公平5
−10999号公報に開示されている。
[0004] However, such a wastewater treatment method has problems such as generation of offensive odor due to hydrogen sulfide and the like, increase of generated sludge, and generation of offensive odor from the sludge. Therefore, in order to solve these problems, a method has been developed in which humus soil or the like is used as a microbial culture medium to activate sludge generated in the treatment step, to produce activated sludge, and to return the sludge to the reaction step. An example of the activated sludge production apparatus is Japanese Patent Publication 5
No. -10999.

【0005】該公報に開示されている種汚泥の発生装置
(活性汚泥の発生装置)は、被培養液である汚泥と微生
物培養剤である微生物代謝回路誘導剤とを混合接触さ
せ、種汚泥を製造するものである。すなわち、この装置
は微生物培養剤と被培養液との効率的な接触のため、流
入口、流出口を具備する外筐体と間隔を設けて配置され
た内筒体内部に微生物培養剤を充填し、その下方より散
気管で曝気を行い、上昇流を発生させ、これを前記隙間
より降下させ循環させることを特徴とするものである。
[0005] The seed sludge generator (active sludge generator) disclosed in this publication makes a mixed contact between sludge as a liquid to be cultured and a microbial metabolic circuit inducer as a microbial cultivating agent, thereby converting the seed sludge. It is manufactured. In other words, this device fills the inside of the inner cylinder, which is spaced from the outer housing with an inlet and an outlet, with the microorganism culture agent for efficient contact between the microorganism culture agent and the culture medium. Then, aeration is performed from below by a diffuser tube to generate an upflow, which is lowered from the gap and circulated.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、前記特
公平5−10999号公報に開示された装置において
は、一般的にペレット状の構造を持つ微生物培養剤の下
から直接曝気を行うため、内筒体内において培養剤が曝
気により転倒を繰り返し、培養剤の損耗がひどく、その
補充や交換の作業が多くなり、結果的にランニングコス
トが高くなるという問題点があった。
However, in the apparatus disclosed in Japanese Patent Publication No. Hei 5-10999, since the aeration is generally performed directly from below the microbial culture medium having a pellet-like structure, an inner cylinder is required. There has been a problem that the culture medium repeatedly falls over due to aeration in the body, and the culture medium is severely worn, and the replenishment and replacement work increases, resulting in a high running cost.

【0007】本発明は以上のような従来技術の問題点を
解決するために成されたものであり、その目的は、効果
的に微生物培養剤と被培養液を接触させ、微生物培養剤
の損耗を最小限とすることで、その補充や交換に伴う材
料費や人件費等を最小限とし、結果的にランニングコス
トの低減が可能な活性汚泥の製造装置を提供することで
ある。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems of the prior art, and an object of the present invention is to effectively bring a microorganism culture agent into contact with a culture medium and to reduce the consumption of the microorganism culture agent. It is an object of the present invention to provide an activated sludge manufacturing apparatus capable of minimizing material costs and labor costs associated with replenishment and replacement thereof, thereby reducing 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
課題は、微生物培養剤が収納され、該微生物培養剤と被
培養液とを好気的条件下で接触させる培養槽と、培養槽
の外部に設けられた循環流発生装置とを移送管で接続し
て強制的に培養槽内に被培養液の循環流を発生させるよ
う構成したことを特徴とする活性汚泥の製造装置によっ
て解決される。
According to the present invention, an object of the present invention is to provide a culturing tank containing a microorganism culturing agent and bringing the microorganism culturing agent into contact with the culture solution under aerobic conditions, A solution is provided by an activated sludge manufacturing apparatus characterized in that a circulating flow generating device provided outside the tank is connected by a transfer pipe to forcibly generate a circulating flow of a liquid to be cultured in a culture tank. Is done.

【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濃度の高い汚泥ではなく、微生
物培養剤の作用によって被培養液の微生物濃度を高めた
培養液や有用菌が培養された培養液、および代謝回路の
変換した微生物が培養された培養液等を意味する。ま
た、本発明で使用される被培養液とは有機性排水処理に
よって発生する汚泥のことである。
The activated sludge used in the present invention is not a sludge having a high concentration of microorganisms used in the activated sludge method, but a culture solution or a useful bacterium in which the concentration of microorganisms in the liquid to be cultured is increased by the action of a microorganism culturing agent. Culture medium, and a culture solution in which the microorganism whose metabolic cycle has been converted is cultured. The culture solution used in the present invention is sludge generated by organic wastewater treatment.

【0010】[0010]

【発明の実施の形態】以下、本発明の好ましい実施態様
について図面にもとづいて説明するが、本発明が本実施
態様のみに限定されないことは言うまでもない。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below with reference to the drawings, but it is needless to say that the present invention is not limited to only the embodiments.

【0011】図1は本発明装置の一実施態様を示す縦断
面図であり、培養槽1と循環流発生装置2とで構成され
ている。
FIG. 1 is a longitudinal sectional view showing an embodiment of the apparatus of the present invention, which comprises a culture tank 1 and a circulating flow generator 2.

【0012】3は培養槽1の円筒状本体(以下本体と称
す)であり、4は本体3内部に、その内面と隙間が無い
ように配設され、微生物培養剤5が充填される円筒体で
ある。円筒体4の上下は開口しており、その上下端部分
には金網またはパンチングメタル等から成る天板6およ
び底板7が取り付けてあり、微生物培養剤5を円筒体4
内に収納する働きをしている。天板6は脱着自在に取付
けられており、微生物培養剤5の充填または交換が可能
な構造となっている。
Reference numeral 3 denotes a cylindrical main body (hereinafter referred to as a main body) of the culture tank 1. Reference numeral 4 denotes a cylindrical body which is disposed inside the main body 3 so as to have no gap with the inner surface thereof and is filled with the microorganism culture agent 5. It is. The upper and lower ends of the cylindrical body 4 are open, and a top plate 6 and a bottom plate 7 made of wire mesh or punched metal are attached to the upper and lower ends thereof.
It works to store it inside. The top plate 6 is detachably attached, and has a structure in which the microorganism culture agent 5 can be charged or replaced.

【0013】円筒体4内に充填される微生物培養剤5
は、活性汚泥を製造するために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ス、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が好適なものとして挙げられ
る。また、本体3上部には、被培養液をポンプなどによ
り汲み上げて、流入させるための供給口8、被培養液の
オーバーフロー用排出口9が設けられ、本体3の下部側
面には培養後の活性汚泥の取り出し口10および取出し
バルブ11が設けられている。
Microorganism culture agent 5 filled in cylindrical body 4
Is a substance containing an effective component for producing activated sludge, specifically, a useful microorganism culture agent in the form of pellets,
Suitable substances include far-infrared ceramics, rocks, minerals, humus-containing substances, substances having an antibacterial effect on microorganisms other than useful bacteria, or mixtures of these substances. In addition, a supply port 8 for pumping and inflowing the liquid to be cultured by a pump or the like and an outlet 9 for overflowing the liquid to be cultured are provided in the upper part of the main body 3. A sludge discharge port 10 and a discharge valve 11 are provided.

【0014】また本体3の底部には、被培養液中に含ま
れるゴミ等を本体3内から除去するための排出口12、
排出バルブ13が設けられている。また、円筒体4の上
下に位置する本体3の側面には培養槽1の外部に設けら
れた後記循環流発生装置2を接続するための取り付け口
14および15が設けられている。
An outlet 12 for removing dust and the like contained in the culture solution from the inside of the main body 3 is provided at the bottom of the main body 3.
A discharge valve 13 is provided. In addition, attachment ports 14 and 15 are provided on the side surfaces of the main body 3 located above and below the cylindrical body 4 for connecting a circulating flow generator 2 described later provided outside the culture tank 1.

【0015】16は被培養液の流入量、活性汚泥の取り
出し量を規定できる水位センサーであり、あらかじめ設
定した水位を検知して、その制御回路により、ポンプ、
バルブ等の制御を行うものである。17はガイド管であ
り、供給口8より流入された被培養液を円筒体4の下側
に直接導入させている。
Reference numeral 16 denotes a water level sensor capable of regulating the inflow amount of the liquid to be cultured and the removal amount of the activated sludge. The water level sensor detects a predetermined water level and controls the pump,
It controls valves and the like. Reference numeral 17 denotes a guide tube which directly introduces the culture solution flowing from the supply port 8 into the lower side of the cylindrical body 4.

【0016】一方、循環流発生装置2は強制的に培養槽
1内に循環流を起こすための装置であり、エアリフトポ
ンプ18とその移送管として作用する接続管19から成
る。エアリフトポンプ18は前記本体3の二ヵ所の接続
口14,15に接続管19を介して接続されており、エ
アリフトポンプ18を稼動させることにより、図1の矢
印の様な循環流を発生させる。循環流の方向は矢印とは
逆方向にしても良く、装置の構造により適宜選択でき
る。この場合、エアリフトポンプ18により曝気も同時
に行なわれるため別に曝気装置を設ける必要はない。
On the other hand, the circulating flow generator 2 is a device for forcibly generating a circulating flow in the culture tank 1, and includes an air lift pump 18 and a connecting pipe 19 serving as a transfer pipe thereof. The air lift pump 18 is connected to two connection ports 14 and 15 of the main body 3 via connection pipes 19, and generates a circulating flow as indicated by an arrow in FIG. 1 by operating the air lift pump 18. The direction of the circulating flow may be opposite to the direction of the arrow, and can be appropriately selected depending on the structure of the device. In this case, since aeration is performed simultaneously by the air lift pump 18, there is no need to provide a separate aeration device.

【0017】以下、本実施態様の作用について説明す
る。ポンプ等を用いて供給口8より導入された被培養液
は導入口17により本体3内の円筒体4の下方部分から
満たされ、その冠水量は水位センサー16の制御回路に
よって調整される。被培養液中にごみ等が多く含まれる
場合には、これを沈澱させ、排出バルブ13を開くこと
により、排出口12より排出させ、ごみ等を除去する。
次に、循環流発生装置2のエアリフトポンプ18を起動
させ、循環流を発生させる。これにより、培養槽1と循
環流発生装置2との間で図1の矢印のごとく一定方向の
水流が発生し、被培養液が内筒体4内に充填された微生
物培養剤5と接触しながら循環される。
The operation of this embodiment will be described below. The liquid to be cultured introduced from the supply port 8 using a pump or the like is filled from the lower portion of the cylindrical body 4 in the main body 3 by the introduction port 17, and the flooding amount is adjusted by the control circuit of the water level sensor 16. When a large amount of dust or the like is contained in the culture solution, the waste is settled and discharged through the discharge port 12 by opening the discharge valve 13 to remove the dust and the like.
Next, the air lift pump 18 of the circulating flow generator 2 is started to generate a circulating flow. As a result, a water flow in a certain direction is generated between the culture tank 1 and the circulating flow generator 2 as shown by an arrow in FIG. 1, and the liquid to be cultured comes into contact with the microorganism culture agent 5 filled in the inner cylinder 4. It is circulated while.

【0018】この際、微生物培養剤5が本体2の内面と
隙間なく配設されているため、被培養液が必ず微生物培
養剤5と接触するようになっている。循環する時間すな
わち培養する時間については24時間以上を目安とし、
特に限定されない。培養後、製造された活性汚泥は、取
り出しバルブ11を開くことにより、取出し口10を経
て、後記反応工程へ返送される。
At this time, since the microorganism culturing agent 5 is arranged without a gap with the inner surface of the main body 2, the liquid to be cultured always comes into contact with the microorganism culturing agent 5. The time for circulating, that is, the time for culturing, should be 24 hours or more,
There is no particular limitation. After the cultivation, the produced activated sludge is returned to the later-described reaction step via the discharge port 10 by opening the discharge valve 11.

【0019】あらかじめ設定した水位まで活性汚泥が排
出返送されると、水位センサー16の制御回路によって
取り出しバルブ11は閉塞される。この際、返送する被
培養液の量は全体容量の半量を目安とするが、特に限定
されない。この状態において培養槽1には残り半量の活
性汚泥が残り、新たに供給口8より、被培養液が本体3
内に導入され、上記の操作を繰り返す。活性汚泥を半量
程度残すのは、活性汚泥の製造効率を向上させるためで
ある。
When the activated sludge is discharged and returned to a predetermined water level, the control circuit of the water level sensor 16 closes the take-out valve 11. At this time, the amount of the culture solution to be returned is approximately half of the total volume, but is not particularly limited. In this state, the remaining half of the activated sludge remains in the culture tank 1, and the culture liquid is newly supplied from the supply port 8 to the main body 3.
And the above operation is repeated. The reason for leaving about half of the activated sludge is to improve the production efficiency of the activated sludge.

【0020】図2は他の実施態様を示す縦断面図であ
る。図1と異なるところは、循環流発生装置2のエアリ
フトポンプ18の代わりに水流ポンプ20が用いられて
おり、曝気を行うために空気供給管21が接続管19に
接続されて設けられている点である。空気供給管21の
設置位置は内筒体4の上方または接続管19の適宜位置
等いづれでもよい。
FIG. 2 is a longitudinal sectional view showing another embodiment. The difference from FIG. 1 is that a water flow pump 20 is used in place of the air lift pump 18 of the circulating flow generator 2, and an air supply pipe 21 is connected to a connection pipe 19 for aeration. It is. The installation position of the air supply pipe 21 may be any position above the inner cylinder 4 or an appropriate position of the connection pipe 19.

【0021】また図3は本発明装置を排水処理施設にお
いて活用した場合の模式図である。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、沈澱池によるご
み等の除去、および微生物による浄化処理を行う反応工
程を経て、最終的に沈澱工程で上澄み分と汚泥分とに分
離され、上澄み分は処理水として河川等に放流される。
一方、汚泥分は濃縮工程において濃縮され、その一部は
本発明装置内へと取り出され、微生物培養剤により活性
化され、製造された活性汚泥は反応工程中の各処理槽へ
と戻される。結果的に、処理槽内に含まれる本装置で製
造された活性汚泥の濃度が高まり、処理効率を高めるも
のである。
FIG. 3 is a schematic diagram when the present invention is used in a wastewater treatment facility. The organic wastewater that has flowed into the wastewater treatment facility undergoes a reaction process that removes refuse and the like using screens and sedimentation basins, and a purification process that uses microorganisms.These processes are finally separated into supernatant and sludge in the precipitation process. The supernatant is discharged to rivers and the like as treated water.
On the other hand, the sludge is concentrated in the concentration step, and a part of the sludge is taken out into the apparatus of the present invention, activated by the microorganism culture agent, and the produced activated sludge is returned to each treatment tank in the reaction step. As a result, the concentration of the activated sludge produced by the present apparatus contained in the treatment tank is increased, and the treatment efficiency is enhanced.

【0022】[0022]

【発明の効果】以上説明したごとく、本発明の活性汚泥
発生装置を用いると、被培養液と微生物培養剤との確実
な接触が行なわれると同時に、微生物培養剤の損耗を最
小限とすることができる。従って、その補充や交換に伴
う材料費や人件費等を最小限とすることができ、結果的
にランニングコストの低減が可能となることから、本発
明は極めて実用的なものである。
As described above, when the activated sludge generator of the present invention is used, reliable contact between the liquid to be cultured and the microorganism culturing agent is performed, and at the same time, the wear of the microorganism culturing agent is minimized. Can be. Therefore, the present invention is extremely practical because the material cost and labor cost associated with the replenishment and replacement can be minimized, and the running cost can be reduced as a result.

【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】本発明装置の他の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. 2 is a longitudinal sectional view of an apparatus for producing activated sludge showing another embodiment of the apparatus of the present invention.

【図3】本発明装置を排水処理施設に活用した場合の模
式図である。
FIG. 3 is a schematic diagram when the device of the present invention is used in a wastewater treatment facility.

【符号の説明】[Explanation of symbols]

1…培養槽 2…循環流発生装置 3…円筒状本体 4…円筒体 5…微生物培養剤 6…天板 7…底板 8…供給口 9…オーバーフロー排出口 10…取り出し口 11…取り出しバルブ 12…排出口 13…排出バルブ 14…取り付け口 15…取り付け口 16…水位センサー 17…ガイド管 18…エアリフトポンプ 19…接続管 20…水流ポンプ 21…空気供給管 DESCRIPTION OF SYMBOLS 1 ... Culture tank 2 ... Circulation flow generator 3 ... Cylindrical body 4 ... Cylindrical body 5 ... Microorganism culture agent 6 ... Top plate 7 ... Bottom plate 8 ... Supply port 9 ... Overflow discharge port 10 ... Removal port 11 ... Removal valve 12 ... Discharge port 13 ... Discharge valve 14 ... Mounting port 15 ... Mounting port 16 ... Water level sensor 17 ... Guide pipe 18 ... Air lift pump 19 ... Connection pipe 20 ... Water flow pump 21 ... Air supply pipe

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 微生物培養剤が収納され、該微生物培養
剤と被培養液とを好気的条件下で接触させる培養槽と、
培養槽の外部に設けられた循環流発生装置とを移送管で
接続して強制的に培養槽内に被培養液の循環流を発生さ
せるよう構成したことを特徴とした活性汚泥の製造装
置。
1. A culture tank containing a microorganism culturing agent, and bringing the microorganism culturing agent into contact with a culture solution under aerobic conditions;
An activated sludge manufacturing apparatus, wherein a circulating flow generator provided outside a culture tank is connected by a transfer pipe to forcibly generate a circulating flow of a liquid to be cultured in the culture tank.
【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ス、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装置。
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. Claim 1.
4. The activated sludge production apparatus according to claim 1.
【請求項3】 循環流発生装置がエアリフトポンプであ
る請求項1に記載の活性汚泥の製造装置。
3. The activated sludge production apparatus according to claim 1, wherein the circulating flow generator is an air lift pump.
【請求項4】 循環流発生装置が水流ポンプと空気供給
管とからなっている請求項1に記載の活性汚泥の製造装
置。
4. The activated sludge producing apparatus according to claim 1, wherein the circulating flow generator comprises a water pump and an air supply pipe.
JP15825596A 1996-06-19 1996-06-19 Apparatus for producing activated sludge Pending JPH10487A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15825596A JPH10487A (en) 1996-06-19 1996-06-19 Apparatus for producing activated sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15825596A JPH10487A (en) 1996-06-19 1996-06-19 Apparatus for producing activated sludge

Publications (1)

Publication Number Publication Date
JPH10487A true JPH10487A (en) 1998-01-06

Family

ID=15667638

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15825596A Pending JPH10487A (en) 1996-06-19 1996-06-19 Apparatus for producing activated sludge

Country Status (1)

Country Link
JP (1) JPH10487A (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

Cited By (2)

* 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
JP2011245476A (en) * 2010-05-26 2011-12-08 Universal Engineering Co Ltd Sludge modifying machine and water treatment facility provided with sludge modifying machines in parallel

Similar Documents

Publication Publication Date Title
KR100303811B1 (en) Biological aerated filter system
CN1994935B (en) Odor-free energy-saving micro aerobiont combined processing system for cabaret sewage processing and reusing
CN110183052A (en) A kind of waste waste water treatment system and method
KR100661815B1 (en) The sewage treatment system
KR970006499B1 (en) Apparatus and method for organic wastewater treatment
CN209890451U (en) Nitrification and denitrification circulating water treatment system
JPH10487A (en) Apparatus for producing activated sludge
JP3328139B2 (en) Method and apparatus for producing activated sludge
JPH04367788A (en) Purification tank
KR200237437Y1 (en) A sewage and wastewater disposal system
CN208292824U (en) A kind of starch gourmet powder waste water biochemistry intensive treatment system
KR200165565Y1 (en) Hanging microbe contact aeration purifier
JPH08168792A (en) Method of deodorizing-modifying organic waste water treating flow
JP3243061B2 (en) Water treatment device and water treatment method
JPH02157094A (en) Batchwise biomembrane filtering method and apparatus
JPH10486A (en) Apparatus for producing activated sludge
KR100474106B1 (en) Method for wastewater and night soil treatment utilizing microbial actuator and its apparatus
CN213708058U (en) Rural micro-polluted water purification device
CN215799023U (en) Combined domestic sewage treatment equipment
CN220078792U (en) Aquaculture tail water purification system with flexible switching of recycling and standard discharge
KR19980078896A (en) Sewage Treatment Method and Device Using Soil Activated Humus
KR910004079B1 (en) Waste water purifier using coal
KR20010064953A (en) Method and device of waste water treatment using bio mineral water reactor
JPH01157328A (en) Culture of water circulating type and cultivating device
JPH07265891A (en) Water treating device