JPH0653279B2 - Batch type water treatment device - Google Patents

Batch type water treatment device

Info

Publication number
JPH0653279B2
JPH0653279B2 JP1104259A JP10425989A JPH0653279B2 JP H0653279 B2 JPH0653279 B2 JP H0653279B2 JP 1104259 A JP1104259 A JP 1104259A JP 10425989 A JP10425989 A JP 10425989A JP H0653279 B2 JPH0653279 B2 JP H0653279B2
Authority
JP
Japan
Prior art keywords
tank
sludge
biological treatment
sewage
storage 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 - Fee Related
Application number
JP1104259A
Other languages
Japanese (ja)
Other versions
JPH02280894A (en
Inventor
一 伊藤
栄二 嶋田
耕市 水田
Original Assignee
日立機電工業株式会社
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 日立機電工業株式会社 filed Critical 日立機電工業株式会社
Priority to JP1104259A priority Critical patent/JPH0653279B2/en
Publication of JPH02280894A publication Critical patent/JPH02280894A/en
Publication of JPH0653279B2 publication Critical patent/JPH0653279B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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)
  • 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〕 本発明は設置スペースが小さく、かつ脱窒・脱リンが要
求される小規模排水処理に好適な回分式水処理装置に関
するものである。
TECHNICAL FIELD The present invention relates to a batch-type water treatment device which has a small installation space and is suitable for small-scale wastewater treatment requiring denitrification and dephosphorization.

〔従来の技術〕[Conventional technology]

生活排水等の下水は一般に有機物質が多量に含まれてい
る。このため下水中に空気を供給して所謂曝気を行なっ
て有機物質を好気性処理させる工程と、曝気を停止して
嫌気性処理を行ない、好気性処理で硝化した窒素を窒素
ガスに還元して清浄処理を行ない沈澱工程の後、処理さ
れた水を上澄水として排水する回分式水処理方法が提案
されている。この回分式処理装置としては矩形水槽を用
い、生成処理槽と汚泥濃縮貯留槽とを設置している。
Sewage such as domestic wastewater generally contains a large amount of organic substances. Therefore, a step of supplying air into the sewage to perform so-called aeration to aerobically treat the organic substance, and to stop the aeration to perform anaerobic treatment, reduce the nitrified nitrogen in the aerobic treatment to nitrogen gas. A batch-type water treatment method has been proposed in which the treated water is drained as supernatant water after performing a cleaning treatment and a precipitation step. A rectangular water tank is used as this batch treatment apparatus, and a production treatment tank and a sludge concentration storage tank are installed.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

このように矩形で生物処理槽と汚泥濃縮貯留槽とを別々
に設置すると設置面積が大きくなり、かつ両槽間を接続
するための配管経路が長くなり、かつ各水槽のコーナ部
や中央部に汚泥が堆積し、これが経時的に腐敗して悪臭
等の公害問題となることがある。
If you install the biological treatment tank and sludge concentration storage tank separately in this rectangular shape, the installation area will be large, the piping path for connecting both tanks will be long, and the corners and central parts of each water tank will be Sludge accumulates, and it may spoil over time, causing pollution problems such as foul odors.

小規模な下水処理場ではこのように設置スペースが大き
くなることは不利である。
In such a small sewage treatment plant, such a large installation space is disadvantageous.

本発明ではこの回分式槽の形状を変えることにより上述
の欠点を解消するものである。
In the present invention, the above-mentioned drawbacks are eliminated by changing the shape of this batch type tank.

〔課題を解決するための手段〕[Means for Solving the Problems]

二重円形状にして、かつ外側に生物処理槽を、内側に汚
泥濃縮貯留槽を配置して一体とすると共に、生物処理槽
内に曝気装置を備え、かつ生物処理槽から汚泥濃縮貯留
槽へ汚泥を移送する移送手段を備える。
It has a double circular shape and has a biological treatment tank on the outside and a sludge concentration storage tank on the inside to be integrated, and is equipped with an aeration device inside the biological treatment tank, and from the biological treatment tank to the sludge concentration storage tank. A transfer means for transferring sludge is provided.

〔作 用〕[Work]

回分式水処理装置に二重円形槽を適用し、かつ外側に生
物処理槽を、その内側で生物処理槽の中央部に汚泥濃縮
貯留槽を配置しているので、設備の一体化が図れて省ス
ペースとなり、しかも配管も最少限度でよく、配管手数
及び使用管長が大幅に低減できる。さらに槽が円形のた
め、槽内の水流は循環流となり、流速を大とすることが
できるので、沈澱工程で槽底部に沈澱した汚泥を効率良
く巻きあげることができる。また円形槽内における水流
は循環水流となるため槽内の均一混合が効率よく行え、
かつ比較的小さな動力で充分混合攪拌でき設備動力,消
費動力とも低減することができる。
Since a double circular tank is applied to the batch-type water treatment system, and the biological treatment tank is placed outside and the sludge concentration storage tank is placed inside the biological treatment tank in the center, the equipment can be integrated. It saves space and requires only a minimum amount of piping, which can significantly reduce the number of pipes and the length of pipe used. Further, since the tank is circular, the water flow in the tank becomes a circulation flow and the flow velocity can be increased, so that the sludge settled to the bottom of the tank in the precipitation step can be efficiently wound up. In addition, since the water flow in the circular tank becomes a circulating water flow, uniform mixing in the tank can be performed efficiently.
Moreover, it is possible to sufficiently mix and stir with a relatively small power, and it is possible to reduce both equipment power consumption and power consumption.

〔実施例〕〔Example〕

以下下本発明を図示の実施例にもとづいて説明する。 The present invention will be described below with reference to the illustrated embodiments.

図において1は所要の径と深さを有する円形をした生物
処理槽で、この生物処理槽1の中央に所要径の汚泥濃縮
貯留槽2を配置する。この時、生物処理槽と汚泥濃縮貯
留槽は同心異径状に配置することが望ましい。そして生
物処理槽1内には未処理の汚水を流入管5を介して供給
するが、この供給量は第2図に示すように通常汚水の生
物処理中予め定めた低水位LWLから高水位HWLの間
に水位を保たれるようになす。また、汚水の流入位置は
上澄水排出管6の反対側が好ましく、汚水を連続流入さ
せる場合には、槽の底部に流入管5を設ける。
In the figure, reference numeral 1 denotes a circular biological treatment tank having a required diameter and depth, and a sludge concentration storage tank 2 having a required diameter is arranged in the center of the biological treatment tank 1. At this time, it is desirable to arrange the biological treatment tank and the sludge concentration storage tank in concentric and different diameters. Then, untreated sewage is supplied into the biological treatment tank 1 through the inflow pipe 5, and the supply amount of the sewage is from a predetermined low water level LWL to a high water level HWL during biological treatment of normal sewage as shown in FIG. Keep the water level between. Further, the inflow position of the sewage is preferably on the opposite side of the supernatant water discharge pipe 6, and when the sewage is continuously introduced, the inflow pipe 5 is provided at the bottom of the tank.

生物処理槽1には供給された汚水を定期的あるいは連続
的に曝気して汚水中の有機物質を好気性発酵処理をする
ための曝気機3が1乃至複数台設置され、この曝気機3
の運転により生物処理槽1槽内汚水の曝気と共に、攪拌
せしめ、かつ水流を発生せしめ、円形状槽内を循環せし
める。この汚水が槽内を循環する時、攪拌曝気がなされ
ると共に、矩形槽に比べ同じ動力の曝気機を用いても速
い流速を得られるので、沈澱工程で槽底部に沈澱した汚
泥を効率良く巻きあげ攪拌混合されるため、汚泥分が槽
底に堆積するのを防止できる。またこの生物処理槽1に
はこの槽底部に吸込口4aを備えた汚泥ポンプ4を設け
ると共に、このポンプ4の吐出口4bを汚泥濃縮貯留槽
2内に配置する。これにより汚泥ポンプ4を駆動すると
沈澱工程の間に生物処理槽の底部に沈澱濃縮した汚泥分
を吸い上げ汚泥濃縮貯留槽へ移送させることができる。
The biological treatment tank 1 is provided with one or a plurality of aerators 3 for aerating the supplied wastewater regularly or continuously to perform aerobic fermentation treatment of organic substances in the wastewater.
By the operation of 1, the biological treatment tank 1 is aerated while agitating sewage in the tank, and causes a water flow to circulate in the circular tank. When this sewage circulates in the tank, aeration and aeration are performed, and a faster flow rate can be obtained even with the aerator with the same power as in the rectangular tank, so the sludge that has settled at the bottom of the tank during the precipitation process can be efficiently wound. Since the mixture is stirred up and mixed, it is possible to prevent sludge from being deposited on the bottom of the tank. Further, the biological treatment tank 1 is provided with a sludge pump 4 having a suction port 4a at the bottom of the biological treatment tank 1, and a discharge port 4b of the pump 4 is arranged in the sludge concentration storage tank 2. As a result, when the sludge pump 4 is driven, the sludge component precipitated and concentrated at the bottom of the biological treatment tank can be sucked up and transferred to the sludge concentration storage tank during the precipitation step.

生物処理槽1には上澄水排水管6を設けると共に、これ
には弁7を備え、沈澱工程後の上澄水を弁7を開いて排
水するが、汚水の処理中は弁7を閉じておくものであ
る。
The biological treatment tank 1 is provided with a supernatant water drainage pipe 6, which is provided with a valve 7 for draining the supernatant water after the precipitation process by opening the valve 7, but keeps the valve 7 closed during the treatment of wastewater. It is a thing.

汚泥濃縮貯留槽2の底部には汚泥排出ビット8を設け、
このビット8より余剰汚泥を排出する排泥管9を配設
し、この排泥管9に備えた排泥弁10を開閉操作するこ
とにより排泥するものである。
A sludge discharge bit 8 is provided at the bottom of the sludge thickening storage tank 2,
A sludge discharge pipe 9 for discharging excess sludge from the bit 8 is provided, and a sludge discharge valve 10 provided in the sludge discharge pipe 9 is opened / closed to discharge sludge.

流入管5より生物処理槽1内に所要量の汚水を流入し、
曝気機3を運転すると汚水を攪拌すると共に曝気する。
これにより槽内の汚水は循還流となって流れ、汚水は所
望の生物処理を行なわれるものとなる。
A required amount of sewage flows into the biological treatment tank 1 through the inflow pipe 5,
When the aerator 3 is operated, sewage is agitated and aerated.
As a result, the sewage in the tank circulates and flows back, and the sewage is subjected to a desired biological treatment.

この曝気機3の運転を予め定めた時間あるいは汚水の生
物処理が完了したことを検知して停止するようになす。
このようにして汚水の生物処理が終了すると、曝気機3
の運転を停止させる。これにより曝気機運転により生物
処理時においては、汚水中の固形物も水流に乗って槽内
を流下循環しているが、曝気機が停止して水流が発生し
なくなると汚水中に浮遊していた固形物は槽底に沈澱
し、上澄水と固形物とが分離される。上澄水は弁7を開
くことにより排水管6を経て槽外へ排水し、減菌後、河
川,海等へ放流する。
The operation of the aerator 3 is stopped upon detection of a predetermined time or completion of biological treatment of sewage.
When the biological treatment of sewage is completed in this way, the aerator 3
Stop driving. As a result, when biological treatment is performed by operating the aerator, the solids in the wastewater also flow down and circulate in the tank along with the water flow, but when the aerator stops and the water flow stops, it floats in the wastewater. The solid matter settles to the bottom of the tank, and the supernatant water and the solid matter are separated. The supernatant water is drained to the outside of the tank through the drainage pipe 6 by opening the valve 7, sterilized, and then discharged to the river, the sea or the like.

この生物処理によって発生し、生物処理槽1の槽底に沈
澱した汚泥水は汚泥ポンプ4の駆動により汚泥濃縮貯留
槽2へ移送される。この汚泥濃縮貯留槽2内で汚泥は自
重により沈澱し、濃縮されるものとなる。この槽内で濃
縮された汚泥は排泥弁10を開くことにより排泥管9を
経て排泥され、バキューム車等により場外へ搬出して処
理するものである。
The sludge water generated by this biological treatment and settled on the bottom of the biological treatment tank 1 is transferred to the sludge concentration storage tank 2 by driving the sludge pump 4. In the sludge thickening storage tank 2, sludge is settled and concentrated by its own weight. The sludge concentrated in this tank is discharged through the mud discharge pipe 9 by opening the mud discharge valve 10, and is carried out to the outside by a vacuum car or the like for processing.

なお曝気機3として図示の実施例では自吸式のものを使
用したが、横軸回転式,縦軸回転式,水中式等各種の機
種が採用できる。又、嫌気工程で攪拌を行なうため、水
中攪拌や水中ポンプ等を併用することもできる。上澄水
の排水装置としてフロート式排水,テレスコープ式排水
装置等も採用できる。
Although the self-priming type is used as the aerator 3 in the illustrated embodiment, various types such as a horizontal axis rotating type, a vertical axis rotating type, and an underwater type can be adopted. Further, since stirring is performed in the anaerobic process, it is possible to use underwater stirring, a submersible pump or the like together. As a drainage device for clear water, a float type drainage device, a telescope type drainage device, etc. can also be adopted.

〔発明の効果〕〔The invention's effect〕

本発明による時は、生物処理槽と汚泥濃縮貯留槽が一体
化されているため、設置スペースが小さくてすみ、生物
処理槽内に汚泥濃縮貯留槽を同心的に配置しているた
め、スワール現象が防止でき、生物処理中に汚泥が底部
に堆積することが防止できる。また汚泥を生物処理槽か
ら汚泥濃縮貯留槽へ移送するための配管長が短くで済
み、さらに曝気機の運転により汚水の混合攪拌と曝気が
行なえ、かつ循環水流も発生するので少ない動力で充分
な生物処理が行なえ、沈澱工程において慣性力により循
環水流が停止するまでの間に槽底部から水面の間にせん
断力が働くため、汚泥の沈澱,濃縮効果を高めることが
でき、省エネルギー化を図れる等の利点を有する。
According to the present invention, since the biological treatment tank and the sludge enrichment storage tank are integrated, the installation space is small, and the sludge enrichment storage tank is concentrically arranged in the biological treatment tank, which results in the swirl phenomenon. Can be prevented, and sludge can be prevented from accumulating on the bottom during biological treatment. Also, the length of the pipe for transferring the sludge from the biological treatment tank to the sludge thickening storage tank is short, and the aeration machine can be operated to mix and stir the aged water and generate a circulating water flow. Biological treatment can be performed, and shearing force acts between the bottom of the tank and the water surface until inertial force stops the circulating water flow in the sedimentation process, which can enhance sludge sedimentation and concentration effects and save energy. Have the advantage of.

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

第1図は平面図、第2図は断面図である。 1は生物処理槽、2は汚泥濃縮貯留槽、3は曝気機、4
は汚泥ポンプ、5は流入管、6は排水管、9は排泥管。
FIG. 1 is a plan view and FIG. 2 is a sectional view. 1 is a biological treatment tank, 2 is a sludge concentration storage tank, 3 is an aerator, 4
Is a sludge pump, 5 is an inflow pipe, 6 is a drain pipe, and 9 is a sludge pipe.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】二重円形状にして、かつ外側に生物処理槽
を、内側に汚泥濃縮貯留槽を配置して一体とすると共
に、生物処理槽内に曝気装置を備え、かつ生物処理槽か
ら汚泥濃縮貯留槽へ汚泥を移送する移送手段を備えたこ
とを特徴とする回分式水処理装置。
1. A double circular shape, a biological treatment tank is arranged on the outside and a sludge concentration storage tank is arranged on the inside to be integrated, and an aeration device is provided in the biological treatment tank. A batch-type water treatment device comprising a transfer means for transferring sludge to a sludge thickening storage tank.
JP1104259A 1989-04-24 1989-04-24 Batch type water treatment device Expired - Fee Related JPH0653279B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1104259A JPH0653279B2 (en) 1989-04-24 1989-04-24 Batch type water treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1104259A JPH0653279B2 (en) 1989-04-24 1989-04-24 Batch type water treatment device

Publications (2)

Publication Number Publication Date
JPH02280894A JPH02280894A (en) 1990-11-16
JPH0653279B2 true JPH0653279B2 (en) 1994-07-20

Family

ID=14375936

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1104259A Expired - Fee Related JPH0653279B2 (en) 1989-04-24 1989-04-24 Batch type water treatment device

Country Status (1)

Country Link
JP (1) JPH0653279B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20020088568A (en) * 2001-05-18 2002-11-29 한샘이앤지(주) Wastewater disposal plant for oxidation ditch using oxidation ditch and method for constructing the same
KR20020088565A (en) * 2001-05-18 2002-11-29 한샘이앤지(주) Wastewater disposal plant using oxidation ditch

Also Published As

Publication number Publication date
JPH02280894A (en) 1990-11-16

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