JPH10202281A - Waste water treating device - Google Patents

Waste water treating device

Info

Publication number
JPH10202281A
JPH10202281A JP1401097A JP1401097A JPH10202281A JP H10202281 A JPH10202281 A JP H10202281A JP 1401097 A JP1401097 A JP 1401097A JP 1401097 A JP1401097 A JP 1401097A JP H10202281 A JPH10202281 A JP H10202281A
Authority
JP
Japan
Prior art keywords
fluidized bed
treated water
water
treatment
tank
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
JP1401097A
Other languages
Japanese (ja)
Inventor
Tatsuhiko Suzuki
辰彦 鈴木
Susumu Ishikawa
進 石川
Masanori Yamanaka
正則 山中
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.)
Maezawa Industries Inc
Original Assignee
Maezawa Industries Inc
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 Maezawa Industries Inc filed Critical Maezawa Industries Inc
Priority to JP1401097A priority Critical patent/JPH10202281A/en
Publication of JPH10202281A publication Critical patent/JPH10202281A/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

  • Biological Treatment Of Waste Water (AREA)
  • Physical Water Treatments (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To surely and efficiently execute a solid-liq. separation of a treated water of a fluidized bed and to make the whole device compact by providing a pressure floatation device executing a solid-liq. separation treatment of the treated water at a post stage of the fluidized bed in a treatment of sewerage with the fluidized bed using a biological membrane sticking carrier. SOLUTION: A raw water made to flow into a raw water tank 15 is raised in the fluidized bed 11 and subjected to an aerobic purifying treatment with microorganisms stuck on a biological membrane-sticking carrier, then sent to the pressure floatation device 12. In the pressure floatation device 12, a pressurized air- dissolving water is mixed to the treated water of a fluidized bed, and a suspension component is floated by making its apparent density small by sticking a suspension component in the treated water of the fluidized bed to finely divided bubbles generated from the pressurized air-dissolving water, and the floated sludge is scraped with a scraper and sent to a sludge storage tank 24, and precipitated sludge is sent to a sludge storage tank 24. Then the treated water executed some order solid-liq. separation is subjected to a main finishing treatment at a filter tank 13, and the water subjected to the filtering treatment is discharged to a river, etc., through a treated water tank 31.

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、排水処理装置に関
し、詳しくは、生物膜付着担体を用いた流動床によって
下排水の処理を行う流動床による排水処理装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment apparatus, and more particularly to a fluidized bed wastewater treatment apparatus for treating wastewater by a fluidized bed using a biofilm-adhered carrier.

【0002】[0002]

【従来の技術】流動床による排水処理法は、生物の保持
量が多く、高い撹拌力が得られることから、処理効率が
良好で、コンパクトな装置で十分な排水処理を行うこと
が可能である。このため、従来から多くの研究が成され
ているが、産業排水処理における小規模施設での実用化
例はあるものの、公共の下水処理等の比較的大規模での
実用例はほとんど無い。
2. Description of the Related Art A wastewater treatment method using a fluidized bed has a high treatment efficiency because a large amount of organisms are retained and a high stirring force can be obtained, and it is possible to perform sufficient wastewater treatment with a compact apparatus. . For this reason, many studies have been made so far, but there are practical examples in small-scale facilities in industrial wastewater treatment, but few practical examples in relatively large-scale such as public sewage treatment.

【0003】また、前記流動床自体では、原則として固
液分離は行われないことから、他の固液分離装置を組合
わせる必要があるが、従来は、この固液分離装置とし
て、通常の重力式の沈殿池やろ過装置をそのまま用いて
いたため、流動床の性能を十分に発揮させることができ
なかった。
In addition, since the solid-liquid separation is not performed in principle in the fluidized bed itself, it is necessary to combine another solid-liquid separation device. Since the sedimentation basin and the filtration device of the formula were used as they were, the performance of the fluidized bed could not be sufficiently exhibited.

【0004】[0004]

【発明が解決しようとする課題】流動床の処理水の固液
分離装置として重力式の沈殿池を固液分離処理に用いた
場合は、沈殿池の設置面積が大きいため、設備全体のコ
ンパクト化が十分ではなかった。すなわち、流動床によ
り排水処理を行うと、通水速度を600〜800m/日
と高速化することができるが、重力式の沈殿池の通水速
度は、一般に20〜100m/日であり、流動床の処理
量に対して大きな面積の沈殿池を設置しなければならな
い。
When a gravity sedimentation basin is used for solid-liquid separation treatment as a solid-liquid separation device for treated water in a fluidized bed, the installation area of the sedimentation basin is large, so that the entire equipment is made compact. Was not enough. That is, when the drainage treatment is performed by the fluidized bed, the water passage speed can be increased to 600 to 800 m / day, but the water passage speed of the gravity type sedimentation pond is generally 20 to 100 m / day. A sedimentation basin with a large area for the floor throughput must be installed.

【0005】一方、流動床は、高負荷での運転が可能で
あるが、負荷が高いと流動床から流出する懸濁成分の量
が多くなるため、流動床の処理水の固液分離装置として
ろ過装置を用いた場合は、安定して長時間のろ過運転を
継続することが困難であった。
[0005] On the other hand, the fluidized bed can be operated at a high load, but when the load is high, the amount of suspended components flowing out of the fluidized bed increases. When a filtration device was used, it was difficult to stably continue the filtration operation for a long time.

【0006】そこで本発明は、流動床の処理水の固液分
離を確実にかつ効率よく行うことができ、流動床の長所
を十分に発揮させて設備全体のコンパクト化を図ること
ができる排水処理装置を提供することを目的としてい
る。
Accordingly, the present invention provides a wastewater treatment which can surely and efficiently perform solid-liquid separation of treated water in a fluidized bed, makes full use of the advantages of a fluidized bed, and makes the entire facility compact. It is intended to provide a device.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するた
め、本発明の排水処理装置は、生物膜付着担体を用いた
流動床によって下排水の処理を行う排水処理装置におい
て、前記流動床の後段に、該流動床で処理した処理水の
固液分離処理を行う加圧浮上分離装置を設けたことを特
徴とし、さらに、前記加圧浮上分離装置の後段に、該加
圧浮上分離装置で処理した処理水のろ過処理を行うろ過
槽を設けたことを特徴としている。
In order to achieve the above object, a wastewater treatment apparatus according to the present invention is a wastewater treatment apparatus for treating wastewater by a fluidized bed using a biofilm-adhered carrier. Further comprising a pressurized flotation device for performing a solid-liquid separation treatment of the treated water treated in the fluidized bed. It is characterized by having a filtration tank for filtering the treated water.

【0008】[0008]

【発明の実施の形態】図1は、本発明の排水処理装置を
用いた排水処理設備の一例を示すものであって、流動床
11で処理した処理水の固液分離を、加圧浮上分離装置
12とろ過槽13との組合わせで行うように構成したも
のである。
FIG. 1 shows an example of a wastewater treatment facility using a wastewater treatment apparatus according to the present invention. The solid-liquid separation of treated water treated by a fluidized bed 11 is performed by pressure flotation separation. This is configured to be performed by a combination of the device 12 and the filtration tank 13.

【0009】流入下水(原水)は、スクリーン14を通
って原水槽15に流入した後、ポンプ16により流動床
11の底部に送られ、圧縮機17から供給される空気と
共に流動床11内を上昇し、生物膜付着担体18に付着
している微生物により好気的浄化処理が行われる。
After the inflow sewage (raw water) flows into the raw water tank 15 through the screen 14, it is sent to the bottom of the fluidized bed 11 by the pump 16 and rises in the fluidized bed 11 together with the air supplied from the compressor 17. Then, an aerobic purification treatment is performed by microorganisms adhering to the biofilm-adhering carrier 18.

【0010】前記生物膜付着担体18としては、従来か
ら用いられているアンスラサイトや粒状活性炭等の担体
を用いることもできるが、ポリプロピレンやポリエチレ
ン等に、比重調整用のシリカやカルシウム等の無機物,
金属粉を添加したプラスチック製担体を用いることが好
ましい。このようなプラスチック製担体は、前記シリカ
等の添加量を調節することによって比重を任意に調整す
ることが可能であり、生物膜付着担体18の比重や大き
さを、流動床11の形状,構成や処理条件に応じて最適
な範囲に設定することができる。
As the biofilm-adhering carrier 18, conventionally used carriers such as anthracite and granular activated carbon can be used. However, inorganic materials such as silica and calcium for adjusting the specific gravity, and polypropylene and polyethylene can be used.
It is preferable to use a plastic carrier to which metal powder is added. The specific gravity of such a plastic carrier can be arbitrarily adjusted by adjusting the amount of the silica or the like added thereto. And the optimum range can be set according to the processing conditions.

【0011】さらに、比重や表面積等に応じて生物膜付
着担体18の大きさを比較的大きく、例えば2〜20m
m程度にすることにより、処理水との分離性や洗浄性を
向上させることができる。したがって、流動床11の流
入原水量に対応した比重及び大きさの生物膜付着担体1
8を用いることが可能となるため、生物の保持量や撹拌
力を最適な状態に設定することができ、処理効率を大幅
に向上させることができる。なお、生物膜付着担体18
の形状は、球形,パイプ状等、成形可能な形状ならば任
意であるが、その表面は、生物膜が付着し易い微細な凹
凸を有するものが好ましい。さらに、微生物の生息に適
した50〜300μm程度の空孔を有するものが特に好
ましい。
Further, the size of the biofilm-adhering carrier 18 is relatively large, for example, 2 to 20 m, depending on the specific gravity and the surface area.
By setting it to about m, the separation property from the treated water and the cleaning property can be improved. Therefore, the biofilm-adhered carrier 1 having a specific gravity and a size corresponding to the amount of inflowing raw water into the fluidized bed 11
Since it is possible to use No. 8, it is possible to set the holding amount of the living organisms and the stirring power in an optimum state, and it is possible to greatly improve the processing efficiency. The biofilm-adhering carrier 18
Any shape can be used as long as it can be molded, such as a sphere or a pipe, but it is preferable that its surface has fine irregularities to which a biofilm can easily adhere. Further, those having pores of about 50 to 300 μm suitable for the inhabitation of microorganisms are particularly preferable.

【0012】前記流動床11で処理された処理水(流動
床処理水)は、床上部に設けられたウェッジワイヤース
クリーン19で上記生物膜付着担体18と分離して配管
20から加圧浮上分離装置12に送られる。前記ウェッ
ジワイヤースクリーン19は、例えば、リング状に形成
した多数のウェッジ形ワイヤーを、複数本のサポートロ
ッドにより所定間隔で保持するとともに、両端を閉塞し
てドラム状に形成し、その一端に前記処理水流出用の前
記配管20を接続したものであって、前記ウェッジ形ワ
イヤーの間隔を適当に設定することにより、目詰まりを
抑えながら処理水及び汚泥を効率よく排出できるととも
に、生物膜付着担体18の流出を確実に防止することが
できる。したがって、生物膜付着担体18の分離にウェ
ッジワイヤースクリーン19を用いることにより、従来
の流動床のように、上部の水面積を大きくしたり、散気
に伴うガスの分離手段を設ける必要がなくなり、流動床
11の簡略化やコンパクト化を図ることができる。
The treated water (fluidized bed treated water) treated in the fluidized bed 11 is separated from the biofilm-attached carrier 18 by a wedge wire screen 19 provided at the upper part of the bed, and is separated from the pipe 20 by a pressure flotation device. 12 is sent. The wedge wire screen 19 is formed, for example, by holding a large number of wedge-shaped wires formed in a ring shape at predetermined intervals by a plurality of support rods, closing both ends to form a drum shape, and forming the processing By connecting the pipe 20 for water outflow, by appropriately setting the interval between the wedge-shaped wires, it is possible to efficiently discharge treated water and sludge while suppressing clogging, Outflow can be reliably prevented. Therefore, by using the wedge wire screen 19 for separating the biofilm-adhered carrier 18, it is not necessary to increase the water area on the upper part or to provide a gas separating means accompanying aeration as in a conventional fluidized bed. The fluidized bed 11 can be simplified and made compact.

【0013】前記加圧浮上分離装置12は、配管20か
ら供給される流動床処理水に配管21から供給される加
圧空気溶解水を混合し、この加圧空気溶解水から発生す
る微細気泡に前記流動床処理水中の懸濁成分を付着させ
て見掛けの比重を小さくすることにより浮上させるもの
で、浮上した浮上汚泥(フロス)は、掻取機22により
掻取られて経路23から汚泥貯留槽24に送られ、底部
に沈殿した汚泥は、経路25から汚泥貯留槽24に送ら
れる。このときの汚泥濃度は3〜5%であり、従来の汚
泥濃縮槽における重力濃縮に比較して高濃度である。
The pressurized flotation device 12 mixes the fluidized bed treated water supplied from the pipe 20 with the pressurized air dissolved water supplied from the pipe 21, and converts the fine bubbles generated from the pressurized air dissolved water into fine bubbles. The floating components are floated by adhering suspended components in the fluidized-bed treated water to reduce the apparent specific gravity, and the raised floating sludge (floss) is scraped by the scraper 22 and passed through the path 23 to the sludge storage tank. The sludge which has been sent to the bottom 24 and settled at the bottom is sent from the passage 25 to the sludge storage tank 24. The sludge concentration at this time is 3 to 5%, which is higher than gravity concentration in a conventional sludge concentration tank.

【0014】上記加圧浮上分離装置12で処理された水
の一部は、出口側で配管26に抜取られてポンプ27で
加圧され、コンプレッサー28から供給される圧縮空気
と混合槽29で混合した後、加圧空気溶解水として前記
配管21から流動床処理水に供給混合される。
A part of the water treated by the pressurized flotation device 12 is withdrawn from a pipe 26 at an outlet side, pressurized by a pump 27, and mixed with compressed air supplied from a compressor 28 in a mixing tank 29. After that, it is supplied to the fluidized-bed treated water from the pipe 21 and mixed as pressurized air-dissolved water.

【0015】上記加圧浮上分離装置12で、ある程度の
固液分離処理が行われた処理水(加圧浮上処理水)は、
配管30から前記ろ過槽13の底部に流入し、主にSS
成分の除去による仕上げ処理が行われ、ろ過処理された
水は、処理水槽31を経て河川等に放流される。なお、
ろ過槽13には、ろ材を洗浄するための洗浄手段とし
て、槽下部に、引抜き配管32,空洗配管33,水洗配
管34が設けられており、洗浄排水は、配管35により
前記原水槽15に戻される。このように、ろ過槽13の
洗浄排水を原水槽15に戻して原水と混合し、再度処理
することにより、汚泥の発生箇所を加圧浮上分離装置1
2に一本化することができるだけでなく、発生汚泥の高
濃度化を図ることができるので、汚泥発生量がランニン
グコストに大きく影響する比較的小規模な下排水処理施
設では、そのランニングコストを大幅に低減させること
ができる。
The treated water (pressurized levitation treated water) that has been subjected to a certain degree of solid-liquid separation processing by the pressure flotation / separation apparatus 12 is
It flows into the bottom of the filtration tank 13 from the pipe 30 and mainly
Finishing treatment is performed by removing components, and the filtered water is discharged to a river or the like via a treated water tank 31. In addition,
In the filtration tank 13, a drawing pipe 32, an empty washing pipe 33, and a washing pipe 34 are provided in the lower part of the tank as washing means for washing the filter medium. Will be returned. In this way, the washing wastewater from the filtration tank 13 is returned to the raw water tank 15, mixed with the raw water, and treated again, so that the sludge generation site can be located in the pressure flotation device 1
In addition to being able to unify the wastewater into a single wastewater treatment facility, it is possible to increase the concentration of the generated sludge. It can be greatly reduced.

【0016】さらに、加圧浮上分離装置12は、高速処
理が行えるだけでなく、通常の重力沈殿処理に比べて懸
濁成分の除去率が高いため、要求される処理水質によっ
ては後段のろ過槽13を設置しなくてもよく、加圧浮上
分離装置12のみで十分な固液分離処理を行うことが可
能である。また、加圧浮上分離装置12の後段にろ過槽
13を設けた場合は、ろ過槽13への流入負荷を小さく
できるので、ろ過槽13の容量を小さくすることが可能
になり、しかも、浮上分離処理では、髪の毛、油分、ス
カム等の浮上し易い成分を、略完全に除去することがで
きるため、ろ過槽13での閉塞やスカムの発生が少なく
なり、安定した状態で長時間の連続運転が可能となる。
Further, the pressure flotation device 12 can not only perform high-speed processing, but also has a higher removal rate of suspended components than ordinary gravity sedimentation processing. It is not necessary to install 13, and it is possible to perform a sufficient solid-liquid separation process only by the pressure flotation device 12. Further, when the filtration tank 13 is provided at the subsequent stage of the pressure flotation device 12, the load on the filtration tank 13 can be reduced, so that the capacity of the filtration tank 13 can be reduced. In the treatment, components that easily float, such as hair, oil, and scum, can be almost completely removed, so that clogging and scum in the filtration tank 13 are reduced, and continuous operation for a long time in a stable state is achieved. It becomes possible.

【0017】したがって、流動床11と加圧浮上分離装
置12とを組合わせることにより、排水処理設備の処理
効率を大幅に向上させることができ、設備の小形化を図
ることができる。さらに、ろ過槽13を加えることによ
り、処理水質を大幅に向上させることができる。
Therefore, by combining the fluidized bed 11 and the pressure flotation device 12, the treatment efficiency of the wastewater treatment equipment can be greatly improved, and the equipment can be downsized. Further, by adding the filtration tank 13, the quality of the treated water can be greatly improved.

【0018】なお、上記形態例では、流動床を好気性流
動床としているが、嫌気性の流動床であってもよく、ま
た、加圧浮上分離装置として無薬注加圧浮上を用いてい
るが、凝集剤を添加した凝集加圧浮上としてもよい。さ
らに、ろ過槽を上向流としているが、下向流にしてもよ
い。ろ過槽のろ材構成を多層式とすることも可能であ
り、ろ材の種類もアンスラサイト、ケイ砂、その他のプ
ラスチック製ろ材等を使用することができ、特に限定さ
れるものではない。
In the above embodiment, the fluidized bed is an aerobic fluidized bed. However, it may be an anaerobic fluidized bed, and a non-chemical injection pressurized floater is used as a pressurized floater. However, it is also possible to adopt a coagulation pressure levitation to which a coagulant is added. Further, although the filtration tank has an upward flow, it may have a downward flow. The filter medium composition of the filtration tank may be a multilayer type, and the type of the filter medium may be anthracite, silica sand, another plastic filter medium, or the like, and is not particularly limited.

【0019】[0019]

【発明の効果】以上説明したように、本発明の排水処理
装置は、処理効率に優れた流動床と懸濁成分の除去率が
高い加圧浮上分離装置とを組合わせたので、処理能力を
損なうことなく設備の小形化を図ることができる。
As described above, the wastewater treatment apparatus of the present invention combines a fluidized bed with excellent treatment efficiency and a pressurized flotation apparatus with a high removal rate of suspended components, thereby increasing the treatment capacity. The size of the equipment can be reduced without any loss.

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

【図1】 本発明の排水処理装置を用いた排水処理設備
の一例を示す系統図である。
FIG. 1 is a system diagram showing an example of a wastewater treatment facility using a wastewater treatment device of the present invention.

【符号の説明】[Explanation of symbols]

11…流動床、12…加圧浮上分離装置、13…ろ過
槽、15…原水槽、18…生物膜付着担体、19…ウェ
ッジワイヤースクリーン、22…掻取機、24…汚泥貯
留槽、29…混合槽、31…処理水槽
11: Fluidized bed, 12: Pressure flotation separator, 13: Filtration tank, 15: Raw water tank, 18: Biofilm adhered carrier, 19: Wedge wire screen, 22: Scraper, 24: Sludge storage tank, 29 ... Mixing tank, 31 ... treated water tank

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 生物膜付着担体を用いた流動床によって
下排水の処理を行う排水処理装置において、前記流動床
の後段に、該流動床で処理した処理水の固液分離処理を
行う加圧浮上分離装置を設けたことを特徴とする排水処
理装置。
1. A wastewater treatment apparatus for treating sewage wastewater by a fluidized bed using a biofilm-adhered carrier, wherein a pressurization for performing a solid-liquid separation treatment of the treated water treated by the fluidized bed is provided at a subsequent stage of the fluidized bed. A wastewater treatment device comprising a flotation device.
【請求項2】 前記加圧浮上分離装置の後段に、該加圧
浮上分離装置で処理した処理水のろ過処理を行うろ過槽
を設けたことを特徴とする請求項1記載の排水処理装
置。
2. The wastewater treatment apparatus according to claim 1, wherein a filtration tank for filtering the treated water treated by the pressure flotation apparatus is provided downstream of the pressure flotation apparatus.
JP1401097A 1997-01-28 1997-01-28 Waste water treating device Pending JPH10202281A (en)

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Application Number Priority Date Filing Date Title
JP1401097A JPH10202281A (en) 1997-01-28 1997-01-28 Waste water treating device

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JPH10202281A true JPH10202281A (en) 1998-08-04

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006167551A (en) * 2004-12-14 2006-06-29 Kurita Water Ind Ltd Biological treatment apparatus
CN1311445C (en) * 2002-02-08 2007-04-18 索尼株式会社 Optical head
JP2008246386A (en) * 2007-03-30 2008-10-16 Kurita Water Ind Ltd Organic wastewater treatment apparatus
FR2919601A1 (en) * 2007-07-30 2009-02-06 Degremont Sa Purifying wastewater by biological treatment that eliminates sludge such as carbon, nitrogen or phosphorus in the wastewater, comprises fixing a portion of microorganisms on movable solid supports, and treating the activated sludge
CN110468033A (en) * 2019-08-26 2019-11-19 同济大学 Strengthen the anaerobic digestion device for producing biogas using self-holding air bearing

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1311445C (en) * 2002-02-08 2007-04-18 索尼株式会社 Optical head
JP2006167551A (en) * 2004-12-14 2006-06-29 Kurita Water Ind Ltd Biological treatment apparatus
JP4591678B2 (en) * 2004-12-14 2010-12-01 栗田工業株式会社 Biological treatment equipment
JP2008246386A (en) * 2007-03-30 2008-10-16 Kurita Water Ind Ltd Organic wastewater treatment apparatus
FR2919601A1 (en) * 2007-07-30 2009-02-06 Degremont Sa Purifying wastewater by biological treatment that eliminates sludge such as carbon, nitrogen or phosphorus in the wastewater, comprises fixing a portion of microorganisms on movable solid supports, and treating the activated sludge
WO2009047406A2 (en) * 2007-07-30 2009-04-16 Degremont Method and installation for biologically treating waste water
WO2009047406A3 (en) * 2007-07-30 2009-06-18 Degremont Method and installation for biologically treating waste water
US8382984B2 (en) 2007-07-30 2013-02-26 Degremont Method and installation for biologically treating waste water
CN110468033A (en) * 2019-08-26 2019-11-19 同济大学 Strengthen the anaerobic digestion device for producing biogas using self-holding air bearing
CN110468033B (en) * 2019-08-26 2020-12-08 同济大学 Anaerobic digestion device for strengthening methane production by utilizing self-sustaining air flotation
US11618872B2 (en) 2019-08-26 2023-04-04 Tongji University Anaerobic digestion device based on self-sustained air flotation

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