JPH054094A - Batch type activated sludge treatment equipment - Google Patents

Batch type activated sludge treatment equipment

Info

Publication number
JPH054094A
JPH054094A JP3183226A JP18322691A JPH054094A JP H054094 A JPH054094 A JP H054094A JP 3183226 A JP3183226 A JP 3183226A JP 18322691 A JP18322691 A JP 18322691A JP H054094 A JPH054094 A JP H054094A
Authority
JP
Japan
Prior art keywords
activated sludge
sewage
valve
batch type
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
JP3183226A
Other languages
Japanese (ja)
Inventor
Tsuneo Suzuki
恒雄 鈴木
Hitoshi Sato
等 佐藤
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.)
Hitachi Ltd
Original Assignee
Hitachi Plant Engineering and Construction 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 Hitachi Plant Engineering and Construction Co Ltd filed Critical Hitachi Plant Engineering and Construction Co Ltd
Priority to JP3183226A priority Critical patent/JPH054094A/en
Publication of JPH054094A publication Critical patent/JPH054094A/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

(57)【要約】 【目的】 空気送風機及び汚水流入ポンプの起動・停止
操作の回数を低減して間欠曝気を行って効率の良い処理
が可能な回分式活性汚泥装置を提供すること。 【構成】 汚水の流入・攪拌工程と曝気・攪拌工程と排
出工程とが単一処理槽内で時間制御によって順次行われ
る回分式活性汚泥処理装置において、処理槽が開口部を
有する仕切壁6によって2個の槽1A及び1Bに区分さ
れ、空気送風機の主配管を分岐させて各槽に接続し、こ
の分岐配管5A及び5Bの上部には開閉弁8A及び8
B、下部には水中攪拌機4A及び4Bを設け、該開閉弁
の下方部分では汚水流入管と接続し、該汚水流入管に逆
止弁9A及び9Bを設けたことを特徴とする汚水の回分
式活性汚泥処理装置である。
(57) [Abstract] [Purpose] To provide a batch type activated sludge device capable of performing efficient treatment by performing intermittent aeration by reducing the number of times of starting and stopping operations of an air blower and a sewage inflow pump. [Structure] In a batch type activated sludge treatment device in which a sewage inflow / agitation process, aeration / agitation process, and discharge process are sequentially performed in a single treatment tank by time control, the treatment tank uses a partition wall 6 having an opening. It is divided into two tanks 1A and 1B, the main pipe of the air blower is branched and connected to each tank, and the opening / closing valves 8A and 8 are provided above the branch pipes 5A and 5B.
B, a submersible batch system characterized in that submersible stirrers 4A and 4B are provided in the lower part, the lower part of the on-off valve is connected to a sewage inflow pipe, and check valves 9A and 9B are provided in the sewage inflow pipe. It is an activated sludge treatment device.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、有機性汚水の活性汚泥
法による回分式処理装置に係り、特に、単一槽内で汚水
を生物学的に処理した後、処理水を排出することを繰り
返す回分式活性汚泥処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a batch type treatment apparatus using an activated sludge method for organic sewage, and more particularly to discharging treated water after biologically treating the sewage in a single tank. It relates to a batch type activated sludge treatment device.

【0002】[0002]

【従来の技術】回分式活性汚泥処理方法は、単一槽内に
汚水を流入しながら攪拌を行う流入・攪拌工程、間欠曝
気を行う曝気工程を予め設定した時間で繰り返した後、
沈殿工程及び上澄水である処理水の排出工程を1サイク
ルとした処理工程で構成されている。また、各工程は、
予め設定した時間で操作され、間欠曝気によって汚水中
のBOD、窒素及び燐を除去する方法である。
2. Description of the Related Art A batch type activated sludge treatment method is a method in which an inflow / agitation step of stirring while inflowing sewage into a single tank and an aeration step of intermittent aeration are repeated at preset times,
It is composed of a treatment step in which a precipitation step and a step of discharging treated water which is supernatant water are one cycle. In addition, each process
It is a method of removing BOD, nitrogen and phosphorus in wastewater by intermittent aeration, which is operated at a preset time.

【0003】しかし、攪拌工程の汚水流入ポンプ操作及
び曝気工程における間欠曝気操作を空気送風機の起動・
停止操作で行う場合、過電流保護回路が頻繁に作動した
り、機械的な摩耗・損傷が起きやすくなる。また、作動
回数を減らすため、電磁弁あるいは空気作動弁を設けた
場合、少なくとも4個の弁を必要とし、複雑となり、管
理上の問題があった。
However, the operation of the sewage inflow pump in the stirring process and the intermittent aeration operation in the aeration process are started and started by the air blower.
When the stop operation is performed, the overcurrent protection circuit is frequently activated and mechanical wear and damage are likely to occur. Also, in order to reduce the number of times of operation, when an electromagnetic valve or an air operated valve is provided, at least four valves are required, which is complicated and there is a problem in management.

【0004】[0004]

【発明が解決しようとする課題】本発明は、間欠曝気の
繰り返し回数が多くても、簡単な構造の開閉弁を用いる
ことによって、空気送風機及び汚水流入ポンプの負担を
少なくし、しかも汚水中のBOD、窒素及び燐を効率よ
く除去できる回分式活性汚泥処理装置を提供することを
目的とする。
The present invention reduces the load on the air blower and the sewage inflow pump by using the open / close valve having a simple structure even when the number of times of intermittent aeration is large, and the waste water can be treated in An object of the present invention is to provide a batch type activated sludge treatment device capable of efficiently removing BOD, nitrogen and phosphorus.

【0005】[0005]

【課題を解決するための手段】本発明は、空気送風機の
主配管を分岐させ、この分岐配管に汚水流入ポンプと水
中攪拌機を接続し、弁によって曝気と汚水流入が交互に
行われ、一方の槽で曝気が行われているとき、他方の槽
では汚水の流入が行われるように構成することによって
上記目的を達成したものである。
According to the present invention, a main pipe of an air blower is branched, and a sewage inflow pump and an underwater agitator are connected to the branch pipe, and aeration and sewage inflow are alternately performed by a valve. When the aeration is performed in the tank, the other tank is configured to allow the inflow of sewage to achieve the above object.

【0006】即ち、本発明は、汚水の流入・攪拌工程と
曝気・攪拌工程と排出工程とが単一処理槽内で時間制御
によって順次行われる回分式活性汚泥処理装置におい
て、処理槽が開口部を有する仕切壁によって2個の槽に
区分され、空気送風機の主配管を分岐させて各槽に接続
し、この各分岐配管の上部には開閉弁、下部には水中攪
拌機を設け、該開閉弁の下方部分では汚水流入管と接続
し、該汚水流入管に逆止弁を設けたことを特徴とする回
分式活性汚泥処理装置を提供するものである。
That is, according to the present invention, in the batch type activated sludge treatment device in which the inflow / agitation step of a wastewater, the aeration / agitation step and the discharge step are sequentially performed in a single treatment tank by time control, the treatment tank has an opening. It is divided into two tanks by a partition wall having an air blower, and the main pipe of the air blower is branched and connected to each tank. An opening / closing valve is provided at the upper part of each branch pipe and an underwater agitator is provided at the lower part of the opening / closing valve. The present invention provides a batch type activated sludge treatment device, characterized in that it is connected to a sewage inflow pipe in the lower part of the above and a check valve is provided in the sewage inflow pipe.

【0007】本発明の処理装置において、処理水排出装
置は、特に制限はなく、様々なものを適用することがで
きるが、フロート付処理水排出装置を用い、そのフロー
トと空気送風機の主配管とを開閉弁を介して接続するこ
とによって、空気送風機からの空気を有効に利用して上
澄水を効率よく排出することができる。
In the treatment apparatus of the present invention, the treated water discharge apparatus is not particularly limited and various kinds can be applied. However, the treated water discharge apparatus with a float is used, and the float and the main pipe of the air blower are used. Is connected via an open / close valve, the air from the air blower can be effectively used to efficiently discharge the supernatant water.

【0008】[0008]

【実施例】次に、本発明の実施例を図面に基づいて説明
する。図1は、本発明の一実施例を示す処理装置の略示
断面図、図2は工程の説明図、図3は図1に示した処理
装置に用いた処理水排出装置の説明図である。
Embodiments of the present invention will now be described with reference to the drawings. FIG. 1 is a schematic cross-sectional view of a treatment apparatus showing an embodiment of the present invention, FIG. 2 is an illustration of steps, and FIG. 3 is an illustration of a treated water discharge apparatus used in the treatment apparatus shown in FIG. .

【0009】図1において、処理装置は、単一槽から成
るが、仕切壁6及び阻流壁7によって第一槽1Aと第二
槽1Bに区分され、汚水流入ポンプ2及び空気送風機3
が分岐配管5A及び5Bによって各槽に接続されてお
り、分岐配管5A及び5Bの下部には水中攪拌機4A及
び4Bが設置されている。仕切壁6及び阻流壁7には、
それぞれ開口部6A及び7Aが設けられ、これらによっ
て両槽は連通している。さらに、第一槽には余剰汚泥引
き抜きポンプ10が接続され、第二槽には処理水排出装
置11が設置されている。汚水流入ポンプから出た汚水
流入管は、第一槽1A及び1Bへのそれぞれ汚水を流入
させるため、分岐させ、それぞれ逆止弁9A及び9Bを
介して分岐配管5A及び5Bと接続され、各分岐配管の
上部には開閉弁8A及び8Bが設けられている。さら
に、処理水排出装置11は、開閉弁8Cを介して空気送
風機3の主配管と接続されている。各機器は、時間制御
で操作される。
In FIG. 1, the treatment apparatus is composed of a single tank, but is divided into a first tank 1A and a second tank 1B by a partition wall 6 and a baffle wall 7, and a sewage inflow pump 2 and an air blower 3 are provided.
Is connected to each tank by branch pipes 5A and 5B, and submersible stirrers 4A and 4B are installed below the branch pipes 5A and 5B. In the partition wall 6 and the baffle wall 7,
Openings 6A and 7A are provided respectively, and these tanks communicate with each other. Further, a surplus sludge extraction pump 10 is connected to the first tank, and a treated water discharge device 11 is installed in the second tank. The sewage inflow pipe discharged from the sewage inflow pump is branched in order to inject the sewage into the first tanks 1A and 1B, respectively, and is connected to the branch pipes 5A and 5B via the check valves 9A and 9B, respectively. On-off valves 8A and 8B are provided above the pipe. Further, the treated water discharger 11 is connected to the main pipe of the air blower 3 via the open / close valve 8C. Each device is operated by time control.

【0010】本発明の装置を用いて汚水処理を行う場合
には、図2に示したように、まず、曝気工程と攪拌工程
と汚水流入工程とを開始し、汚水流入ポンプ2、空気送
風機3並びに水中攪拌機4A及び4Bを駆動させ、開閉
弁8Aを電気的に開き、開閉弁8Bを電気的に閉とする
ことによって、汚水は自動的に風圧の少ない逆止弁9B
を介して、水中攪拌機4Bに流入する。また、空気は、
開閉弁8Aを介して水中攪拌機4Aに流入する。なお、
図2において、鎖線は間欠的操作を示し、実戦は連続操
作を意味する。
When sewage treatment is performed using the apparatus of the present invention, as shown in FIG. 2, first, the aeration step, the stirring step and the sewage inflow step are started, and the sewage inflow pump 2 and the air blower 3 are started. In addition, by driving the submersible stirrers 4A and 4B, electrically opening and closing the on-off valve 8A, and electrically closing the on-off valve 8B, sewage is automatically checked by a check valve 9B having a small wind pressure.
Through the underwater agitator 4B. Also, the air is
It flows into the submersible stirrer 4A via the on-off valve 8A. In addition,
In FIG. 2, the chain line indicates intermittent operation, and actual battle means continuous operation.

【0011】このように汚水は、風圧がかかっていない
逆止弁側の槽に流入し、一方空気は、風圧が掛かってい
る逆止弁側の槽に流入する。したがって、予め設定され
た時間で開閉弁の開放動作を交互に行うと、両槽で間欠
的曝気が行われ、空気送風機及び汚水流入ポンプを頻繁
に遮断する必要がない。しかも汚水は、常に、酸素の少
ない槽側に流入するため、汚水のBOD源を利用でき、
脱窒反応が容易に行われる。間欠曝気工程及び汚水流入
工程中に水中攪拌機を常時回転させておけば効率よい接
触・混合ができる。このように、予め設定した時間に開
閉弁8A、8Bの開閉を交互に繰り返すことによって汚
水中のBOD、窒素及び燐は生物学的に除去される。
As described above, the sewage flows into the check valve side tank where the wind pressure is not applied, while the air flows into the check valve side tank where the wind pressure is applied. Therefore, when the opening and closing valves are alternately opened at preset times, intermittent aeration is performed in both tanks, and it is not necessary to frequently shut off the air blower and the dirty water inflow pump. Moreover, since the wastewater always flows into the tank side with less oxygen, the BOD source of the wastewater can be used,
The denitrification reaction is easily performed. Efficient contact and mixing can be performed by constantly rotating the submerged agitator during the intermittent aeration process and the sewage inflow process. In this way, BOD, nitrogen and phosphorus in the wastewater are biologically removed by alternately opening and closing the open / close valves 8A and 8B at preset times.

【0012】一定の時間を経過した後、汚水流入ポンプ
2、空気送風機3及び水中攪拌機4A及び4Bを停止さ
せ、沈殿工程とする。次に、排出工程では、電気的に連
動した開閉弁8Dを開くことによって処理水排出装置1
1より処理水が放流される。処理水排出装置11は、図
3に示したように、開口12部を有する取水部13に蛇
腹部14及びフロート15を結合した構成となってお
り、フロート15は、チューブ16及び開閉弁8Cを介
して空気送風機3の主配管に接続されている。したがっ
て、上記のように開閉弁8C及び8Dを開くと、フロー
ト15内の空気がチューブ16、開閉弁8C及び8Dを
通って排出され、フロート15が沈み、取水部も同時に
沈み、処理水は開口部12から流入し、蛇腹部14へ入
り、配管を通って排出される。
After a certain period of time has passed, the sewage inflow pump 2, the air blower 3, and the submersible stirrers 4A and 4B are stopped to start the precipitation step. Next, in the discharge step, the treated water discharge device 1 is opened by opening the electrically operated on-off valve 8D.
Treated water is discharged from 1. As shown in FIG. 3, the treated water discharger 11 has a structure in which a bellows portion 14 and a float 15 are coupled to a water intake portion 13 having an opening 12 portion, and the float 15 includes a tube 16 and an on-off valve 8C. It is connected to the main pipe of the air blower 3 via. Therefore, when the opening / closing valves 8C and 8D are opened as described above, the air in the float 15 is discharged through the tube 16 and the opening / closing valves 8C and 8D, the float 15 sinks, and the intake part also sinks at the same time, and the treated water opens. It flows in from the portion 12, enters the bellows portion 14, and is discharged through the pipe.

【0013】所定時間後、空気送風機3を作動させると
共に開閉弁8Cを開、開閉弁8Dを閉とすることによっ
てフロート15内に空気を入れると、フロート15及び
取水部13は、液面より上にくるように浮上し、開口部
12からの処理水の流入は停止する。次いで、開閉弁8
Cを閉とすれば、1サイクルが終了し、最初の工程に戻
る。余剰汚泥は、定期的に余剰汚泥ポンプ10によって
引き抜かれる。
After a predetermined time, when air is introduced into the float 15 by operating the air blower 3 and opening the open / close valve 8C and closing the open / close valve 8D, the float 15 and the water intake part 13 are above the liquid level. And the inflow of treated water from the opening 12 is stopped. Next, the on-off valve 8
When C is closed, one cycle ends and the process returns to the first step. The surplus sludge is regularly withdrawn by the surplus sludge pump 10.

【0014】上記実施例には、分岐配管に開閉弁8A及
び8B、汚水流入管に逆止弁9A及び9Bを設けた場合
を示したが、これらの代わりに汚水流入管と分岐配管と
の接続部に三方向開閉弁を設けた構造とすることもでき
る。
In the above embodiment, the branch pipes are provided with the on-off valves 8A and 8B and the waste water inflow pipes are provided with the check valves 9A and 9B. Instead of these, the connection between the waste water inflow pipe and the branch pipes is shown. It is also possible to adopt a structure in which a three-way on-off valve is provided in the section.

【0015】実施例1 図1に示した装置を用い汚水として表1に示す水質の下
水を表1に示す運転条件で処理し、得られた処理水の水
質を表1に示す。なお、曝気は、従来法では連続曝気を
行い、本発明方法では開閉弁8Aと開閉弁8Bを10分
間隔で電気的に交互に開閉した。
Example 1 Using the apparatus shown in FIG. 1, sewage having the water quality shown in Table 1 was treated as sewage under the operating conditions shown in Table 1, and the water quality of the obtained treated water is shown in Table 1. Aeration was performed by continuous aeration in the conventional method, and in the method of the present invention, the on-off valve 8A and the on-off valve 8B were electrically opened and closed alternately at intervals of 10 minutes.

【0016】[0016]

【表1】 [Table 1]

【0017】[0017]

【発明の効果】本発明の装置を用いれば、一方の槽で曝
気を行うとき、他方の槽は曝気を行わず攪拌と汚水の流
入を行うので、嫌気的処理と好気的処理との組合せを繰
り返して行うことができ、BOD除去ばかりでなく、硝
化及び脱窒、さらには脱りんも効率よく行うことがで
き、また、バルキング防止及びスカム発生防止も期待す
ることができる。さらに、汚水流入ポンプ及び空気送風
機の起動・停止の回数が少なく、開閉弁の開閉とともに
すべての作業を電気的に時間制御で行うことができるた
め、装置の管理も容易である。そのため、特に、過疎地
域や小規模下水道において管理の容易な装置として有効
に利用することができる。
When the apparatus of the present invention is used for aeration in one tank, stirring and inflow of sewage are performed in the other tank without performing aeration, so a combination of anaerobic treatment and aerobic treatment is performed. It is possible to perform not only BOD removal but also nitrification and denitrification, and further dephosphorization efficiently, and it is possible to expect bulking prevention and scum generation prevention. Furthermore, since the number of times the sewage inflow pump and the air blower are started and stopped is small and all the work can be performed electrically with time control together with opening and closing of the on-off valve, the management of the device is easy. Therefore, it can be effectively used as a device that can be easily managed especially in a depopulated area or a small-scale sewer.

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

【図1】本発明の一実施例を示す汚水の活性汚泥処理装
置の断面図である。
FIG. 1 is a sectional view of an activated sludge treatment device for wastewater showing an embodiment of the present invention.

【図2】本発明の装置を用いた汚水の活性汚泥処理工程
の説明図である。
FIG. 2 is an explanatory diagram of an activated sludge treatment process of wastewater using the device of the present invention.

【図3】図1に示した処理水排出装置の説明図である。FIG. 3 is an explanatory view of the treated water discharge device shown in FIG. 1.

【符号の説明】[Explanation of symbols]

1A 第一槽 1B 第二槽 2 汚水流入ポンプ 3 空気送風機 4A及び4B 水中攪拌機 5A及び5B 分岐配管 6 仕切壁 7 阻流壁 8A、8B、8C及び8D 開閉弁 9A及び9B 逆止弁 11 処理水排出装置 1A first tank 1B second tank 2 Sewage inflow pump 3 air blower 4A and 4B underwater stirrer 5A and 5B branch piping 6 partition walls 7 Barrier wall 8A, 8B, 8C and 8D open / close valve 9A and 9B check valve 11 Treated water discharge device

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 汚水の流入・攪拌工程と曝気・攪拌工程
と排出工程とが単一処理槽内で時間制御によって順次行
われる回分式活性汚泥処理装置において、処理槽が開口
部を有する仕切壁によって2個の槽に区分され、空気送
風機の主配管を分岐させて各槽に接続し、この各分岐配
管の上部には開閉弁、下部には水中攪拌機を設け、該開
閉弁の下方部分では汚水流入管と接続し、該汚水流入管
に逆止弁を設けたことを特徴とする汚水の回分式活性汚
泥処理装置。
1. A partition wall in which a treatment tank has an opening in a batch type activated sludge treatment device in which the inflow / agitation step of a wastewater, the aeration / agitation step and the discharge step are sequentially performed in a single treatment tank by time control. It is divided into two tanks, and the main pipe of the air blower is branched and connected to each tank. An on-off valve is provided at the upper part of each branch pipe and an underwater stirrer is provided at the lower part of the branch pipe. A batch type activated sludge treatment device for sewage, which is connected to a sewage inflow pipe and is provided with a check valve in the sewage inflow pipe.
【請求項2】 汚水流入管の逆止弁及び分岐配管の上部
の開閉弁の代わりに、汚水流入管と分岐配管の接続部に
三方向開閉弁を設けた請求項1記載の汚水の回分式活性
汚泥処理装置。
2. The batch type of sewage according to claim 1, wherein a three-way on-off valve is provided at the connection between the sewage inflow pipe and the branch pipe, instead of the check valve of the sewage inflow pipe and the opening / closing valve on the upper part of the branch pipe. Activated sludge treatment equipment.
【請求項3】 空気送風機の主配管とフロート付処理水
排出装置のフロートとを開閉弁を介して接続した請求項
1又は2記載の汚水の回分式活性汚泥処理装置。
3. The batch type activated sludge treatment device of sewage according to claim 1 or 2, wherein the main pipe of the air blower and the float of the treated water discharge device with float are connected via an on-off valve.
JP3183226A 1991-06-27 1991-06-27 Batch type activated sludge treatment equipment Pending JPH054094A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3183226A JPH054094A (en) 1991-06-27 1991-06-27 Batch type activated sludge treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3183226A JPH054094A (en) 1991-06-27 1991-06-27 Batch type activated sludge treatment equipment

Publications (1)

Publication Number Publication Date
JPH054094A true JPH054094A (en) 1993-01-14

Family

ID=16132001

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3183226A Pending JPH054094A (en) 1991-06-27 1991-06-27 Batch type activated sludge treatment equipment

Country Status (1)

Country Link
JP (1) JPH054094A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100404690B1 (en) * 2001-01-03 2003-11-07 김용성 Apparatus for advanced treatment of water polluted by organic substances
JP2020018966A (en) * 2018-07-31 2020-02-06 オルガノ株式会社 Water treatment method and water treatment device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100404690B1 (en) * 2001-01-03 2003-11-07 김용성 Apparatus for advanced treatment of water polluted by organic substances
JP2020018966A (en) * 2018-07-31 2020-02-06 オルガノ株式会社 Water treatment method and water treatment device

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