JPH05185085A - Water treating method by batch type activated sludge and apparatus for treating water - Google Patents

Water treating method by batch type activated sludge and apparatus for treating water

Info

Publication number
JPH05185085A
JPH05185085A JP4026007A JP2600792A JPH05185085A JP H05185085 A JPH05185085 A JP H05185085A JP 4026007 A JP4026007 A JP 4026007A JP 2600792 A JP2600792 A JP 2600792A JP H05185085 A JPH05185085 A JP H05185085A
Authority
JP
Japan
Prior art keywords
sludge
fluidized bed
activated sludge
water
reaction 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
JP4026007A
Other languages
Japanese (ja)
Inventor
Motomu Suekata
求 末方
Shinji Naito
信二 内藤
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.)
Inax Corp
Original Assignee
Inax Corp
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 Inax Corp filed Critical Inax Corp
Priority to JP4026007A priority Critical patent/JPH05185085A/en
Publication of JPH05185085A publication Critical patent/JPH05185085A/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)

Abstract

PURPOSE:To improve treating efficiency by increasing sludge holding volume in a tank of small size. CONSTITUTION:In a water-treating method for purifying water using an activated sludge in which processes of inflow, aeration, precipitation and discharge are carried out in order in a reaction tank 1, a carrier for fluidized bed 4, 4 and 4 consisting of a sponge, a plastic or a ceramic, etc., is provided in the reaction tank 1 and the activated sludge is allowed to attach to the surface of the carrier to increase a sludge holding volume.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は、回分式活性汚泥によ
る水処理方法の改良及びその方法を実行する装置に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improved water treatment method using batch activated sludge and an apparatus for carrying out the method.

【0002】[0002]

【従来の技術及びその課題】従来、1個の反応槽内で流
入,曝気,沈澱,排出の工程を順次行い、汚水等を浄化
処理する回分式活性汚泥による水処理方法では、汚水中
に汚泥を分散させ、汚泥細菌により生物的浄化処理が行
なわれているが、浄化処理効率を高めるためには反応槽
内の汚泥の保持量を高める必要があり、汚泥保持量を高
めるためには反応槽全体を大型のものにせねばならない
という問題点があった。
2. Description of the Related Art Conventionally, a batch type activated sludge water treatment method for purifying sewage and the like by sequentially performing steps of inflow, aeration, precipitation, and discharge in one reaction tank has been known as a sludge in wastewater. The sludge is dispersed and biologically purified by sludge bacteria, but in order to increase the purification efficiency, it is necessary to increase the amount of sludge retained in the reaction tank. There was a problem that the whole thing had to be large.

【0003】[0003]

【課題を解決するための手段】本発明は上記従来の問題
点に鑑み案出したものであって、小型の装置で汚泥保持
量を高め、処理効率を向上できる水処理方法及び装置を
提供せんことを目的とし、その第1の要旨は、1個の反
応槽内で、流入,曝気,沈澱,排出の工程を順次行い活
性汚泥による浄化処理を行なう水処理方法において、前
記反応槽内に、スポンジ,プラスチック,セラミック等
の流動床担体を入れ、該流動床担体に前記活性汚泥を付
着させて処理することである。又、第2の要旨は、流
入,曝気,沈澱,排出の各工程を順次行い活性汚泥によ
る浄化処理を行なう反応槽内に、前記活性汚泥の付着す
るスポンジ,プラスチック,セラミック等の流動床担体
を入れるとともに、該流動床担体の流出を防ぐ回収手段
を付設したことである。
The present invention has been devised in view of the above-mentioned problems of the prior art, and does not provide a water treatment method and device which can increase the sludge holding amount and the treatment efficiency with a small-sized device. The first gist of the invention is to provide a water treatment method in which the steps of inflow, aeration, precipitation, and discharge are sequentially performed in one reaction tank to perform purification treatment with activated sludge, This is to put a fluidized bed carrier such as sponge, plastic, ceramic, etc., and make the activated sludge adhere to the fluidized bed carrier for treatment. The second gist is that a fluidized bed carrier such as sponge, plastic, or ceramic to which the activated sludge adheres is placed in a reaction tank in which the steps of inflow, aeration, precipitation, and discharge are sequentially performed to perform purification treatment with activated sludge. In addition to the above, a recovery means for preventing the fluidized bed carrier from flowing out is additionally provided.

【0004】[0004]

【作用】反応槽内にはスポンジ,プラスチック,セラミ
ック等の流動床担体が入れられているため、槽内の汚泥
はこの流動床担体に付着し、汚泥細菌が良好に増殖され
ることとなり、槽内の汚泥保持量が高まり、その分、処
理効率が向上される。又、流動床担体の回収手段を装置
に付設することにより、余剰汚泥の引抜きが行なわれて
も流動床担体が外部に排出されることがない。
[Function] Since a fluidized bed carrier such as sponge, plastic or ceramic is put in the reaction tank, the sludge in the tank adheres to the fluidized bed carrier and sludge bacteria are satisfactorily grown. The amount of sludge retained inside is increased, and the treatment efficiency is improved accordingly. Further, by attaching the fluidized bed carrier recovery means to the device, the fluidized bed carrier is not discharged to the outside even if the excess sludge is drawn out.

【0005】[0005]

【実施例】以下、本発明の実施例を図面に基づいて説明
する。図1は回分式活性汚泥法による各工程を図示した
ものであり、先ず、流入工程では、反応槽1の内部に外
部より汚水3が流入される。汚水3が所定時間流入され
た後に曝気工程に移り、この曝気工程では、反応槽1内
に設置されている散気管等より気泡を放出して汚水3内
に汚泥2を分散させるために内部で対流を起こさせる。
この曝気工程が所定時間行なわれた後に曝気が停止され
て沈澱工程に移り、この沈澱工程では汚水3中に分散し
た汚泥2が時間の経過とともに除々に反応槽1の底面側
に沈積する。所定時間後には汚泥2の上部に浄化された
上澄水の層が形成されるため、この上澄水を外部に引き
抜いて排出する排出工程が行なわれる。この排出工程の
終了後に再び反応層1内に新たな汚水3が流入されて流
入工程が再開される。このように回分式活性汚泥法で
は、1個の反応層内で流入,曝気,沈澱,排出の各工程
が順次行なわれて汚水の浄化処理が行なわれる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 illustrates each step by the batch activated sludge method. First, in the inflow step, the wastewater 3 is flown into the reaction tank 1 from the outside. After the sewage 3 has flowed into the sewage 3 for a predetermined time, the process proceeds to an aeration step. In this aeration step, air bubbles are released from an air diffuser pipe or the like installed in the reaction tank 1 to disperse the sludge 2 in the sewage 3 internally. Cause convection.
After this aeration process has been performed for a predetermined time, the aeration is stopped and the process proceeds to a precipitation process. In this precipitation process, sludge 2 dispersed in sewage 3 gradually accumulates on the bottom surface side of reaction tank 1 over time. After a predetermined time, a layer of purified supernatant water is formed on the upper part of the sludge 2, so that a discharge step of extracting and discharging the supernatant water is performed. After the completion of this discharge step, new wastewater 3 is again introduced into the reaction layer 1 and the inflow step is restarted. As described above, in the batch activated sludge method, the steps of inflow, aeration, precipitation, and discharge are sequentially performed in one reaction layer to purify the wastewater.

【0006】本例においては、反応層1内に流動床担体
4,4,4が投入されており、この流動床担体4,4,
4はスポンジ,プラスチック,セラミック等の素材から
なり、多数の粒状,砂状等に形成されたものである。こ
のように反応層1内に予め流動床担体4,4,4を入れ
ておくと、汚泥2がこの流動床担体4,4,4の表面に
付着し、細菌が良好に増殖することができ、曝気工程に
おいて、汚泥2が付着した状態の流動床担体4,4,4
が汚水3中に良好に分散されることとなり、各流動床担
体4,4,4に付着している汚泥中の細菌が良好に汚水
3中の有機物を分解して浄化処理し、さらに増殖するこ
とができ、各流動床担体4,4,4を介し細菌の増殖に
よる汚泥2の保持量が高まり、全体として反応槽1内に
存在する汚泥2の保持量が高くなり、その分、反応槽1
が小型のものであっても処理効率が従来のものよりも向
上することとなる。
In this example, the fluidized bed carriers 4, 4, 4 are put in the reaction bed 1.
Reference numeral 4 is made of a material such as sponge, plastic, or ceramic, and is formed into a large number of grains, sands, or the like. When the fluidized bed carriers 4, 4 and 4 are previously placed in the reaction layer 1 as described above, the sludge 2 adheres to the surfaces of the fluidized bed carriers 4, 4 and 4 and bacteria can proliferate well. In the aeration process, fluidized bed carriers 4, 4, 4 with sludge 2 attached
Will be well dispersed in the sewage 3, and the bacteria in the sludge adhering to the fluidized bed carriers 4, 4, 4 will satisfactorily decompose and purify the organic matter in the sewage 3 and further proliferate. It is possible to increase the retention amount of sludge 2 due to the growth of bacteria through each fluidized bed carrier 4, 4, 4 and the retention amount of sludge 2 existing in the reaction tank 1 as a whole becomes higher. 1
The processing efficiency is improved as compared with the conventional one, even if it is small.

【0007】尚、図2に示すように、反応槽1内の汚泥
2の余剰分を外部に引抜き、これを濃縮するために反応
槽1には汚泥濃縮槽7が隣設されており、反応槽1内の
底面側に設置されたポンプP1から汚泥引抜菅5を介し
余剰汚泥2がこの汚泥濃縮槽7内に引き抜かれるが、こ
の時に汚泥2とともに前記流動床担体4,4,4も引き
抜かれてしまうため、図2では汚泥引抜菅5の下流端に
網籠6を設けて、この網籠6により流動床担体4,4,
4を回収するように構成されている。尚、この網籠6は
スクリーン,パンチングメタル等で形成したものであっ
ても良い。この網籠6内に回収された流動床担体4,
4,4は、例えば毎週の管理,点検時等に反応槽1内に
戻される。
As shown in FIG. 2, a sludge thickening tank 7 is provided adjacent to the reaction tank 1 in order to extract the excess sludge 2 in the reaction tank 1 to the outside and concentrate it. Excess sludge 2 is drawn into the sludge thickening tank 7 from a pump P1 installed on the bottom side of the tank 1 through a sludge drawing tube 5, and at this time, the fluidized bed carriers 4, 4, 4 are drawn together with the sludge 2. As shown in FIG. 2, a net basket 6 is provided at the downstream end of the sludge drawing pipe 5 so that the fluid bed carriers 4, 4,
4 is configured to be collected. The net basket 6 may be formed of a screen, punching metal or the like. The fluidized bed carrier 4, which is collected in the net basket 6,
Items 4 and 4 are returned to the reaction tank 1 during weekly management and inspection, for example.

【0008】尚、さらに流動床担体4,4,4の外部へ
の流出を防ぐために、例えば図3に示すように、前記汚
泥引抜用ポンプP1の吸込口周辺に網8を配設し、この
網8により流動床担体4,4,4の流出を防ぐことがで
きる。又、上澄水を引き抜くためのポンプP2には処理
水引抜管9が接続され、ポンプP2の下部には汚泥の巻
き上がりを防ぐためにラッパ状の阻流板10が配設され
ており、この阻流板10とポンプP2の吸込口周辺に網
11を設けて、この網11により流動床担体4,4,4
の外部への流出を防ぐことができる。
In order to prevent the fluidized bed carriers 4, 4, 4 from flowing out to the outside, a net 8 is provided around the suction port of the sludge drawing pump P1 as shown in FIG. 3, for example. The net 8 can prevent the outflow of the fluidized bed carriers 4, 4, 4. Further, a treated water withdrawing pipe 9 is connected to a pump P2 for withdrawing supernatant water, and a trumpet-like baffle plate 10 is disposed below the pump P2 for preventing the sludge from rolling up. A net 11 is provided around the plate 10 and the suction port of the pump P2, and the fluidized bed carriers 4, 4, 4 are provided by the net 11.
Can be prevented from leaking to the outside.

【0009】尚、さらに図4に示すように、バルブを介
し開閉可能な処理水引抜管9と汚泥引抜管5がそれぞれ
設けられた反応槽1においても、各引抜管の吸込口付近
に網12,13を設けて、この網12,13により流動
床担体4,4,4の外部への流出を防ぐことができる。
Further, as shown in FIG. 4, also in the reaction tank 1 provided with the treated water withdrawal pipe 9 and the sludge withdrawal pipe 5 which can be opened and closed via a valve, respectively, a net 12, near the suction port of each withdrawal pipe, By providing 13, the nets 12, 13 can prevent the fluidized bed carriers 4, 4, 4 from flowing out.

【0010】[0010]

【発明の効果】本発明は、1個の反応槽内で、流入,曝
気,沈澱,排出の工程を順次行い活性汚泥による浄化処
理を行なう水処理方法において、前記反応槽内に、スポ
ンジ,プラスチック,セラミック等の流動床担体を入
れ、該流動床担体に前記活性汚泥を付着させて処理する
こととしたため、流動床担体に汚泥が付着して汚泥中の
細菌が良好に増殖することができ、反応槽内の汚泥保持
量が高まり、汚水処理効率が向上し、反応槽を小型のも
のとすることができる。又、流入,曝気,沈澱,排出の
各工程を順次行い活性汚泥による浄化処理を行なう反応
槽内に、前記活性汚泥の付着するスポンジ,プラスチッ
ク,セラミック等の流動床担体を入れるとともに、該流
動床担体の流出を防ぐ回収手段を付設したことにより、
回収手段により外部への流動床担体の流出を防ぎ処理効
率を高めることができる。
INDUSTRIAL APPLICABILITY The present invention is a water treatment method in which the steps of inflow, aeration, precipitation, and discharge are sequentially carried out in one reaction tank to carry out purification treatment with activated sludge. Since a fluidized bed carrier such as ceramics is placed and the activated sludge is adhered to the fluidized bed carrier for treatment, sludge adheres to the fluidized bed carrier and bacteria in the sludge can proliferate well, The amount of sludge retained in the reaction tank is increased, the efficiency of sewage treatment is improved, and the reaction tank can be made smaller. In addition, a fluidized bed carrier such as sponge, plastic, or ceramic to which the activated sludge adheres is put in a reaction tank in which the steps of inflow, aeration, precipitation, and discharge are sequentially performed to perform purification treatment with activated sludge, and the fluidized bed is By attaching a recovery means to prevent the carrier from flowing out,
The recovery means can prevent the outflow of the fluidized bed carrier to the outside and enhance the processing efficiency.

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

【図1】回分式活性汚泥法による各工程を示す工程説明
図である。
FIG. 1 is a process explanatory view showing each process by a batch activated sludge method.

【図2】汚泥引抜装置に流動床担体の回収手段を設けた
概略構成図である。
FIG. 2 is a schematic configuration diagram in which a fluidized bed carrier recovery means is provided in a sludge drawing device.

【図3】引抜用ポンプの周辺に流動床担体の流出防止用
の網を設置した状態の概略構成図である。
FIG. 3 is a schematic configuration diagram showing a state in which a net for preventing outflow of a fluidized bed carrier is installed around a drawing pump.

【図4】引抜管の吸込口に網を配置した状態の概略構成
図である。
FIG. 4 is a schematic configuration diagram showing a state in which a net is arranged at a suction port of a drawn tube.

【符号の説明】[Explanation of symbols]

1 反応槽 2 汚泥 3 汚水 4 流動床担体 5 引抜管 6 網籠 7 汚泥濃縮槽 8,11,12,13 網 P1,P2 ポンプ 1 Reaction Tank 2 Sludge 3 Sewage 4 Fluidized Bed Carrier 5 Extraction Tube 6 Net Basket 7 Sludge Concentration Tank 8, 11, 12, 13 Net P1, P2 Pump

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 1個の反応槽内で、流入,曝気,沈澱,
排出の工程を順次行い活性汚泥による浄化処理を行なう
水処理方法において、前記反応槽内に、スポンジ,プラ
スチック,セラミック等の流動床担体を入れ、該流動床
担体に前記活性汚泥を付着させて処理することを特徴と
する回分式活性汚泥による水処理方法。
1. Inflow, aeration, precipitation,
In a water treatment method in which the steps of discharging are sequentially performed to perform purification treatment with activated sludge, a fluidized bed carrier such as sponge, plastic, or ceramic is put in the reaction tank, and the activated sludge is attached to the fluidized bed carrier for treatment. A method for treating water with batch activated sludge, which is characterized by:
【請求項2】 流入,曝気,沈澱,排出の各工程を順次
行い活性汚泥による浄化処理を行なう反応槽内に、前記
活性汚泥の付着するスポンジ,プラスチック,セラミッ
ク等の流動床担体を入れるとともに、該流動床担体の流
出を防ぐ回収手段を付設したことを特徴とする回分式活
性汚泥による水処理装置。
2. A fluidized bed carrier such as sponge, plastic or ceramic to which the activated sludge adheres is placed in a reaction tank in which the steps of inflow, aeration, precipitation and discharge are sequentially carried out for purification treatment with activated sludge, A water treatment apparatus using batch type activated sludge, which is provided with a recovery means for preventing the outflow of the fluidized bed carrier.
JP4026007A 1992-01-16 1992-01-16 Water treating method by batch type activated sludge and apparatus for treating water Pending JPH05185085A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4026007A JPH05185085A (en) 1992-01-16 1992-01-16 Water treating method by batch type activated sludge and apparatus for treating water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4026007A JPH05185085A (en) 1992-01-16 1992-01-16 Water treating method by batch type activated sludge and apparatus for treating water

Publications (1)

Publication Number Publication Date
JPH05185085A true JPH05185085A (en) 1993-07-27

Family

ID=12181644

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4026007A Pending JPH05185085A (en) 1992-01-16 1992-01-16 Water treating method by batch type activated sludge and apparatus for treating water

Country Status (1)

Country Link
JP (1) JPH05185085A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006122876A (en) * 2004-11-01 2006-05-18 Nishihara Environment Technology Inc Water treatment equipment
CN110980948A (en) * 2019-12-14 2020-04-10 浙江永续环境工程有限公司 Facultative oxygen type flowing biological bed reactor

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS636100B2 (en) * 1981-12-28 1988-02-08 Tonen Sekyu Kagaku Kk

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS636100B2 (en) * 1981-12-28 1988-02-08 Tonen Sekyu Kagaku Kk

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006122876A (en) * 2004-11-01 2006-05-18 Nishihara Environment Technology Inc Water treatment equipment
CN110980948A (en) * 2019-12-14 2020-04-10 浙江永续环境工程有限公司 Facultative oxygen type flowing biological bed reactor

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