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JPH0122835B2 - - Google Patents

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Publication number
JPH0122835B2
JPH0122835B2 JP60237725A JP23772585A JPH0122835B2 JP H0122835 B2 JPH0122835 B2 JP H0122835B2 JP 60237725 A JP60237725 A JP 60237725A JP 23772585 A JP23772585 A JP 23772585A JP H0122835 B2 JPH0122835 B2 JP H0122835B2
Authority
JP
Japan
Prior art keywords
rotating disk
sludge
jet aerator
wastewater
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.)
Expired
Application number
JP60237725A
Other languages
Japanese (ja)
Other versions
JPS6297697A (en
Inventor
Norihiro Yoshikawa
Masatsugu Yamada
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.)
Dengyosha Machine Works Ltd
Original Assignee
Dengyosha Machine Works 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 Dengyosha Machine Works Ltd filed Critical Dengyosha Machine Works Ltd
Priority to JP60237725A priority Critical patent/JPS6297697A/en
Publication of JPS6297697A publication Critical patent/JPS6297697A/en
Publication of JPH0122835B2 publication Critical patent/JPH0122835B2/ja
Granted 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)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、汚水の回転円板を利用する回分式活
性汚泥処理方法および装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a batch activated sludge treatment method and apparatus that utilize a rotating disk for wastewater.

(従来の技術) 回分式活性汚泥法は、曝気、沈澱、処理水の排
出、廃水の注入等の各プロセスを一つの処理槽の
中で行うもので、各プロセスの継続時間や、1サ
イクルの時間を調整することによつて流入量や汚
水負荷の変動に対処することができる上に、処理
槽が一つであるから返送汚泥の必要もないために
装置がコンパクトにでき、建設費や敷地面積も少
なくてすむのが特徴になつている。さらに汚泥の
沈澱が静的状態で行われるので清澄な処理水が得
られ、運転管理も容易なことから最近小規模処理
場向きの処理技術として着目されている。
(Prior art) In the batch activated sludge method, each process such as aeration, sedimentation, discharge of treated water, and injection of waste water is carried out in one treatment tank, and the duration of each process and the length of one cycle are limited. By adjusting the time, it is possible to deal with fluctuations in the inflow volume and sewage load, and since there is only one treatment tank, there is no need to return sludge, making the equipment compact and reducing construction costs and land. One of its characteristics is that it requires less space. Furthermore, since the sludge is settled in a static state, clear treated water can be obtained, and operation management is easy, so it has recently been attracting attention as a treatment technology suitable for small-scale treatment plants.

ただ回分式活性汚泥法は標準活性汚泥法と同様
に、バルキング現象の制御が困難であることが欠
点となつていたが、これに対しては近年、従来の
連続曝気方式とは違つて、廃水の注入時には曝気
を停止しておくことによつて、一時的に嫌気状態
を作り、バルキング現象を抑制できることが実験
的に解明され、回分式活性汚泥法の各種廃水に対
する適用面で大きな光明が見出されている(特公
昭55−24957号公報参照)。
However, the batch activated sludge method, like the standard activated sludge method, had the disadvantage of difficulty in controlling the bulking phenomenon, but in recent years, unlike the conventional continuous aeration method, wastewater It has been experimentally discovered that by stopping aeration when injecting sludge, it is possible to temporarily create an anaerobic state and suppress the bulking phenomenon. (Refer to Special Publication No. 55-24957).

(発明が解決しようとする問題点) しかしながらこの種の汚水処理装置および方法
は、現存のものよりさらにコンパクトで、低エネ
ルギーでしかも浄化効率が良く、保守管理の容易
なものが要望されている。
(Problems to be Solved by the Invention) However, it is desired that this type of sewage treatment apparatus and method be more compact than existing ones, consume less energy, have good purification efficiency, and be easy to maintain.

(問題点を解決するための手段) 上述の要望を達成するため本発明方法において
は、処理槽内に回転円板が約40%浸漬する低水位
まで汚水を入れ、この状態で回転円板を高速で順
養運転を行う第1工程と、生物膜の浄化能が安定
したところで回転円板を高速のままジエツトエア
レータを稼動して硝化運転を行う第2工程と、ジ
エツトエアレータを停止するとともに、汚水を回
転円板が100%浸漬する高水位まで入れ、この状
態で脱窒運転を行う第3工程と、高水位のままジ
エツトエアレータを再稼動して槽内に汚水の回流
と曝気を生じさせる曝気運転を行う第4工程と、
ジエツトエアレータを止め回転円板を低速運転し
て沈降作用を行わせる第5工程と、浄化した処理
水の上澄みを抽出する第6工程と、沈降した汚泥
の一部を汚泥排出口から引き抜いて汚泥槽に送る
第7工程とを繰り返し行うようにする。
(Means for Solving the Problems) In order to achieve the above-mentioned requirements, in the method of the present invention, sewage is poured into the treatment tank to a low water level where the rotating disk is immersed by about 40%, and the rotating disk is placed in this state. The first step is acclimatization operation at high speed, the second step is when the biofilm purification ability is stabilized, the jet aerator is operated with the rotating disk at high speed to perform nitrification operation, and the jet aerator is stopped. At the same time, there is a third step in which wastewater is poured to a high water level where the rotating disk is 100% immersed, and denitrification operation is performed in this state, and the jet aerator is restarted while the water level remains high to circulate wastewater and aerate the tank. a fourth step of performing an aeration operation that causes
The fifth step is to stop the jet aerator and operate the rotary disk at low speed to perform sedimentation, the sixth step is to extract the supernatant of the purified treated water, and a part of the settled sludge is pulled out from the sludge discharge port. The seventh step of sending the sludge to the sludge tank is repeated.

また本発明装置としては、回流型の処理槽内に
回転円板装置を設けると共に、ジエツトエアレー
タを設け、この処理槽に対する汚水流入装置と、
上澄水排出装置を設け、処理槽内に沈降した汚泥
を排出する汚泥排出装置と、排出した汚泥を収容
する汚泥槽を設けて回転円板を利用する回分式活
性汚泥処理装置を構成する。
Furthermore, the apparatus of the present invention includes a rotary disk device provided in a recirculation type treatment tank, a jet aerator, and a sewage inflow device for this treatment tank;
A batch type activated sludge treatment apparatus using a rotating disk is constructed by providing a supernatant water discharge device, a sludge discharge device for discharging sludge settled in a treatment tank, and a sludge tank for storing the discharged sludge.

(作用) 上述のように本発明は装置として、回流型の処
理槽内に、回転円板装置とジエツトエアレータを
付加したから、回転円板によつて汚水との接触面
積を増大させると共に、ジエツトエアレータによ
つて曝気効果を高めることができる。このため本
発明装置は設置面積を縮少できると共に、処理効
率を高めることができる。
(Function) As described above, since the present invention has a rotating disk device and a jet aerator added to the recirculation type treatment tank, the rotating disk increases the contact area with wastewater, and The aeration effect can be enhanced by a jet aerator. Therefore, the apparatus of the present invention can reduce the installation area and improve processing efficiency.

また本発明方法は、回転円板の浸漬程度や回転
速度を変えることによつて、好気的状態、嫌気的
状態あるいは静的状態を作り出し、それによつて
汚水流入→脱窒運転→曝気運転→沈降→上澄水放
流→硝化運転からなる処理サイクルを作り出すよ
うにしたから、この各プロセスの継続時間を調節
することによつて、処理廃水に対して最適な処理
法を可能にすると共に、一種の制限曝気方式にす
ることによつてバルキング現象を押えて、処理効
率を向上させることができる。
In addition, the method of the present invention creates an aerobic state, an anaerobic state, or a static state by changing the degree of immersion and rotational speed of the rotating disk, thereby controlling the inflow of wastewater → denitrification operation → aeration operation → By creating a treatment cycle consisting of sedimentation → supernatant water discharge → nitrification operation, by adjusting the duration of each process, it is possible to achieve the optimal treatment method for treated wastewater, and also to By using the limited aeration method, the bulking phenomenon can be suppressed and the treatment efficiency can be improved.

(実施例) 以下、図面について本発明の実施例を説明す
る。
(Example) Hereinafter, an example of the present invention will be described with reference to the drawings.

まず装置として、第1図の平面図に示すよう
に、処理槽1をループ状の回流型に形成し、この
回流路の一部に1個または複数個(本実施例では
3個)の回転円板装置2を設ける。2aはその回
転円板、2bはモータ、2cはチエン等の伝動装
置である。
First, as an apparatus, as shown in the plan view of FIG. A disk device 2 is provided. 2a is its rotating disk, 2b is a motor, and 2c is a transmission device such as a chain.

また3は回転円板装置2の上流側と下流側にそ
れぞれ設けたジエツトエアレータで、3aはその
圧力水送給管、3bはノズルである。第3図はそ
の詳細を示すもので、これは管3aによつて圧送
されてきた処理水または他の水源からの水をノズ
ル3bより噴出させることにより、その噴出部に
生ずる負圧によつて管3cを介して大気を吸い込
んで、噴射水と共に空気を処理槽1内に噴射する
ようにしたものである。ジエツトエアレータ3と
してはこの他、圧縮空気を直接処理槽1内に吹き
込むようにしてもよいが、いずれにしてもこのジ
エツトエアレータ3は、処理槽1内に汚水の回流
を起させると同時に、曝気作用を行うものであ
る。
Further, 3 is a jet aerator provided on the upstream side and the downstream side of the rotating disk device 2, 3a is a pressure water supply pipe thereof, and 3b is a nozzle. Fig. 3 shows the details of this process, which is performed by ejecting treated water or water from another water source through the pipe 3a from the nozzle 3b, and by the negative pressure generated at the ejecting part. The air is sucked in through a pipe 3c, and the air is injected into the processing tank 1 together with the jetted water. Alternatively, the jet aerator 3 may be configured to blow compressed air directly into the treatment tank 1, but in any case, the jet aerator 3 causes wastewater to circulate inside the treatment tank 1 and at the same time , which performs an aeration effect.

また4は回転円板装置2の上流側のジエツトエ
アレータ3と回転円板装置2との間に設けた処理
槽1に対する汚水流入装置で、4aはそのポン
プ、4bは汚水流入管、4cは開閉弁である。ま
た5は回転円板装置2の下流側のジエツトエアレ
ータ3と回転円板装置2との間に設けた処理槽1
内の上澄水排出装置で、5aはその排出管、5b
は開閉弁である。さらに6は回転円板装置2の上
流側に設けたジエツトエアレータ3と下流側に設
けたジエツトエアレータ3との間における処理槽
1内に沈澱した汚泥を処理槽1の外部に排出する
ために設けた汚泥排出装置で、6aはその排出
管、6bは開閉弁である。また7は排出管6aに
接続して処理槽1の外部に設置した汚泥槽であ
る。
Further, 4 is a wastewater inflow device for the treatment tank 1 provided between the jet aerator 3 on the upstream side of the rotating disk device 2 and the rotating disk device 2, 4a is its pump, 4b is a wastewater inflow pipe, and 4c is a wastewater inflow device. It is an on-off valve. Further, 5 is a processing tank 1 provided between the jet aerator 3 on the downstream side of the rotating disk device 2 and the rotating disk device 2.
In the supernatant water discharge device, 5a is its discharge pipe, 5b
is an on-off valve. Furthermore, 6 is for discharging the sludge settled in the treatment tank 1 between the jet aerator 3 installed on the upstream side of the rotating disk device 2 and the jet aerator 3 installed on the downstream side to the outside of the treatment tank 1. 6a is the discharge pipe, and 6b is the on-off valve. Further, 7 is a sludge tank connected to the discharge pipe 6a and installed outside the treatment tank 1.

つぎに上述のように構成した本発明装置を使用
して行う本発明方法を説明する。
Next, the method of the present invention performed using the apparatus of the present invention configured as described above will be explained.

まず第1工程として、処理槽1内に回転円板2
aが約40%浸漬する低水位Lまで汚水を入れ、こ
の状態で回転円板装置2を高速で運転して円板表
面に生物膜を付着させる順養運転を行う。
First, as the first step, a rotating disk 2 is placed inside the processing tank 1.
Sewage is poured to a low water level L where a is immersed by about 40%, and in this state, the rotating disk device 2 is operated at high speed to perform acclimatization operation in which biofilm is deposited on the disk surface.

つぎに第2工程として、生物膜の浄化能が安定
したところで、回転円板装置2を高速のまま、ジ
エツトエアレータ3を稼動して硝化運転を行う。
つぎに第3工程として、ジエツトエアレータ3を
停止するとともに、汚水を汚水流入装置4により
回転円板2aが100%浸漬する高水位Hまで入れ、
この状態で脱窒運転を行う。第4工程は、高水位
のままジエツトエアレータ3を再稼動して処理槽
1内に汚水の回流と曝気を生じさせる曝気運転を
行う。この曝気運転を行つた後第5工程として、
ジエツトエアレータ3を止め、回転円板装置2を
前記高速運転の1/3〜1/5の低速で運転して、処理
槽1内を回流の少ないゆるやかな状態にして沈降
作用を行わせる。つぎに第6工程として、上述の
ようにして浄化した処理水の上澄みを高水位Hか
ら低水位Lになるまで、上澄水排出装置5を介し
て抽出する。そのあと第7工程として、1日に1
回程度沈降した汚泥の一部を汚泥排出装置6を介
して引き抜いて汚泥槽7に送る。本発明方法は前
記した第1〜第7工程を繰り返し行うものであ
る。
Next, in the second step, when the biofilm purification ability is stabilized, nitrification operation is performed by operating the jet aerator 3 while keeping the rotating disk device 2 at high speed.
Next, as a third step, the jet aerator 3 is stopped, and the waste water is introduced by the waste water inflow device 4 to a high water level H where the rotating disk 2a is 100% immersed.
Denitrification operation is performed in this state. In the fourth step, the jet aerator 3 is restarted while the water level remains high, and an aeration operation is performed in which the wastewater is circulated and aerated within the treatment tank 1. After performing this aeration operation, as the fifth step,
The jet aerator 3 is stopped, and the rotary disk device 2 is operated at a low speed of 1/3 to 1/5 of the high speed operation to bring the inside of the treatment tank 1 into a gentle state with little circulation to perform the sedimentation action. Next, as a sixth step, the supernatant of the treated water purified as described above is extracted from the high water level H to the low water level L via the supernatant water discharge device 5. After that, as the seventh step, once a day
A part of the sludge that has settled for several times is extracted through a sludge discharge device 6 and sent to a sludge tank 7. The method of the present invention involves repeating the first to seventh steps described above.

本発明の回転円板を利用する回分式活性汚泥処
理方法は、前述のような処理プロセス、すなわ
ち、汚水流入→脱窒運転→曝気運転→沈降→上澄
水放流→汚泥排出(1日1回程度)→硝化運転の
サイクルを繰り返すものであるから、これによつ
て連続曝気方式とは異なつた一種の制限曝気方式
によりバルキング現象を抑えて処理効率を向上さ
せることが可能となる。
The batch activated sludge treatment method using the rotating disk of the present invention consists of the treatment process as described above, namely, sewage inflow → denitrification operation → aeration operation → sedimentation → supernatant water discharge → sludge discharge (approximately once a day). ) → Since the cycle of nitrification operation is repeated, it is possible to suppress the bulking phenomenon and improve treatment efficiency by using a type of limited aeration method that is different from the continuous aeration method.

このようにして繰り返される処理プロセスにお
いて、脱窒運転では回転円板2aを100%浸漬状
態で運転するため、円板体表面は嫌気的になり、
前の工程で硝化された亜硝酸性窒素や硝酸性窒素
が脱窒菌の働きにより窒素ガスに還元され、脱窒
されることになる。さらにそのあとの曝気運転で
は、回転円板2aを100%浸漬のまま高速運転す
るから、ジエツトエアレータ3の作用とあいまつ
て再曝気によりきれいな処理水を得ることができ
るようDOの増加と前工程で残留するBODの除去
を行い、次いでゆるやかな状態にして沈降を行わ
せるようにしているので、効果的な汚水浄化がで
きる。
In the treatment process that is repeated in this way, the rotating disk 2a is operated in a 100% immersed state during the denitrification operation, so the surface of the disk becomes anaerobic.
The nitrite nitrogen and nitrate nitrogen that were nitrified in the previous process are reduced to nitrogen gas by the action of denitrifying bacteria, resulting in denitrification. Furthermore, in the subsequent aeration operation, the rotary disk 2a is operated at high speed with 100% immersion, so combined with the action of the jet aerator 3, the DO increases and the pre-processing is performed so that clean treated water can be obtained by re-aeration. The remaining BOD is removed by the process, and then the water is allowed to settle in a gentle state, allowing for effective wastewater purification.

また上澄水の放流、汚泥排出工程の後に、回転
円板2aを約40%浸漬状態で高速運転させて、回
流と曝気を行いながら硝化運転を行つて、十分な
硝化菌の活動を行わせ、その後の新たな汚水の流
入および脱窒運転に備えるようなプロセスにして
いるのも本発明方法の特徴になつている。
Further, after the supernatant water discharge and sludge discharge process, the rotating disk 2a is operated at high speed in a state of approximately 40% immersion, and nitrification operation is performed while circulating and aerating, to ensure sufficient activity of nitrifying bacteria. Another feature of the method of the present invention is that the process prepares for the subsequent inflow of new wastewater and denitrification operation.

以上のように本発明は、回分式活性汚泥法にお
いて、回転円板を装置の重要な部分として活用す
ることにより、汚水との接触面積を拡大して浄化
効率の向上と装置のコンパクト化を図つたもので
あつて、ことに処理プロセスの間で回転円板装置
の浸漬程度や回転速度を変えることによつて好気
的状態、嫌気的状態又はゆるやかな状態を作り、
種々の処理プロセスを現出させるものである。さ
らにこれにジエツトエアレータの噴流を加味する
ことによつて曝気効果をさらに高めて処理効率を
上げることができるものである。
As described above, the present invention utilizes the rotating disk as an important part of the apparatus in the batch activated sludge process, thereby increasing the contact area with wastewater, improving purification efficiency, and making the apparatus more compact. aerobic, anaerobic or gentle conditions are created by varying the degree of immersion and rotational speed of the rotating disk device, especially during the treatment process;
It allows various processing processes to emerge. Furthermore, by adding a jet stream from a jet aerator to this, the aeration effect can be further enhanced and the treatment efficiency can be increased.

しかも前記処理サイクルの中で、各プロセスの
継続時間を調節することによつて種々の廃水に対
して最適な処理が可能となり、また処理の自動化
も可能となるから、本発明によれば保守管理の容
易な省力化した回分式活性汚泥処理装置を得るこ
とができる。
Moreover, by adjusting the duration of each process in the treatment cycle, it is possible to perform optimal treatment for various types of wastewater, and it is also possible to automate the treatment, so according to the present invention, maintenance management is possible. It is possible to obtain a batch type activated sludge treatment device that is easy and labor-saving.

(発明の効果) 上述のように本発明は装置として、回流型の処
理槽内に、回転円板装置とジエツトエアレータを
付加したから、回転円板によつて汚水との接触面
積を増大させると共に、ジエツトエアレータによ
つて曝気効果を高めることができる。このため本
発明装置は従来のこの種装置と比較して設置面積
を縮少できると共に、処理効率を高めることがで
きるというすぐれた効果が得られる。
(Effects of the Invention) As described above, the present invention has a rotating disk device and a jet aerator added to the circulation type treatment tank, so the rotating disk increases the contact area with wastewater. At the same time, the jet aerator can enhance the aeration effect. Therefore, compared to conventional devices of this type, the device of the present invention has excellent effects in that the installation area can be reduced and processing efficiency can be increased.

また本発明方法は、回転円板の浸漬程度や回転
速度を変えることによつて、好気的状態、嫌気的
状態あるいは静的状態を作り出し、それによつて
汚水流入→脱窒運転→曝気運転→沈降→上澄水放
流→硝化運転からなる処理サイクルを作り出すよ
うにしたから、この各プロセスの継続時間を調節
することによつて、処理廃水に対して最適な処理
法を可能にすると共に、一種の制限曝気方式にす
ることによつてバルキング現象を押えることがで
きるから、本発明によれば、処理効率を著しく向
上させることができるというすぐれた効果が得ら
れる。
In addition, the method of the present invention creates an aerobic state, an anaerobic state, or a static state by changing the degree of immersion and rotational speed of the rotating disk, thereby controlling the inflow of wastewater → denitrification operation → aeration operation → By creating a treatment cycle consisting of sedimentation → supernatant water discharge → nitrification operation, by adjusting the duration of each process, it is possible to achieve the optimal treatment method for treated wastewater, and also to Since the bulking phenomenon can be suppressed by using the limited aeration method, the present invention has the excellent effect of significantly improving treatment efficiency.

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

第1図は本発明に係る回転円板を利用する回分
式活性汚泥処理装置の平面図、第2図はそのA−
A断面図、第3図はジエツトエアレータの一例を
示す部分断面図である。 1……処理槽、2……回転円板装置、3……ジ
エツトエアレータ、4……汚水流入装置、5……
上澄水排出装置、6……汚泥排出装置、7……汚
泥槽。
Fig. 1 is a plan view of a batch type activated sludge treatment equipment using a rotating disk according to the present invention, and Fig. 2 is its A-
A sectional view and FIG. 3 are partial sectional views showing an example of a jet aerator. 1... Treatment tank, 2... Rotating disk device, 3... Jet aerator, 4... Sewage inflow device, 5...
Supernatant water discharge device, 6...Sludge discharge device, 7...Sludge tank.

Claims (1)

【特許請求の範囲】 1 一つの処理槽内に回転円板が約40%浸漬する
低水位まで汚水を入れ、この状態で回転円板を高
速で順養運転を行う第1工程と、生物膜の浄化能
が安定したところで回転円板を高速のままジエツ
トエアレータを稼動して硝化運転を行う第2工程
と、ジエツトエアレータを停止するとともに、汚
水を回転円板が100%浸漬する高水位まで入れ、
この状態で脱窒運転を行う第3工程と、高水位の
ままジエツトエアレータを再稼動して槽内に汚水
の回流と曝気を生じさせる曝気運転を行う第4工
程と、ジエツトエアレータを止め回転円板を低速
運転して沈降作用を行わせる第5工程と、浄化し
た処理水の上澄みを抽出する第6工程と、沈降し
た汚泥の一部を汚泥排出口から引き抜いて汚泥槽
に送る第7工程とを繰り返し行うようにしたこと
を特徴とする回転円板を利用する回分式活性汚泥
処理方法。 2 回流型の一つの処理槽内に回転円板装置を設
けると共に、ジエツトエアレータを設け、この処
理槽に対する汚水流入装置と、上澄水排出装置を
設け、処理槽内に沈降した汚泥を排出する汚泥排
出装置と、排出した汚泥を収容する汚泥槽を設け
てなる回転円板を利用する回分式活性汚泥処理装
置。
[Claims] 1. A first step in which wastewater is poured into one treatment tank to a low water level at which the rotating disk is immersed by about 40%, and the rotating disk is acclimatized at high speed in this state; The second step is to operate the jet aerator while keeping the rotating disk at high speed to perform nitrification operation once the purification ability of the wastewater has stabilized, and the second step is to stop the jet aerator and increase the water level so that the rotating disk is 100% immersed in the wastewater. Fill it up to
The third step is to carry out denitrification operation in this state, the fourth step is to restart the jet aerator while the water level is still high and perform an aeration operation to generate wastewater circulation and aeration in the tank, and the fourth step is to stop the jet aerator. A fifth step in which the rotating disk is operated at low speed to perform sedimentation, a sixth step in which the supernatant of the purified treated water is extracted, and a portion of the settled sludge is pulled out from the sludge discharge port and sent to the sludge tank. A batch activated sludge treatment method using a rotating disk, characterized in that seven steps are repeated. 2 A rotating disk device is installed in one treatment tank of the circulation type, and a jet aerator is installed, and a sewage inflow device and a supernatant water discharge device are installed for this treatment tank to discharge the sludge that has settled in the treatment tank. A batch-type activated sludge treatment device that utilizes a rotating disk that includes a sludge discharge device and a sludge tank that stores the discharged sludge.
JP60237725A 1985-10-25 1985-10-25 Method and apparatus for batchwise activated sludge treatment utilizing rotary disc Granted JPS6297697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60237725A JPS6297697A (en) 1985-10-25 1985-10-25 Method and apparatus for batchwise activated sludge treatment utilizing rotary disc

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60237725A JPS6297697A (en) 1985-10-25 1985-10-25 Method and apparatus for batchwise activated sludge treatment utilizing rotary disc

Publications (2)

Publication Number Publication Date
JPS6297697A JPS6297697A (en) 1987-05-07
JPH0122835B2 true JPH0122835B2 (en) 1989-04-27

Family

ID=17019564

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60237725A Granted JPS6297697A (en) 1985-10-25 1985-10-25 Method and apparatus for batchwise activated sludge treatment utilizing rotary disc

Country Status (1)

Country Link
JP (1) JPS6297697A (en)

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5832633B2 (en) * 1978-09-06 1983-07-14 株式会社クボタ Wastewater treatment method
JPS5539264A (en) * 1978-09-13 1980-03-19 Niigata Eng Co Ltd Rotary disk type nitrogen removing apparatus

Also Published As

Publication number Publication date
JPS6297697A (en) 1987-05-07

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