JP2008114161A - Method and apparatus for treating waste water - Google Patents

Method and apparatus for treating waste water Download PDF

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JP2008114161A
JP2008114161A JP2006300159A JP2006300159A JP2008114161A JP 2008114161 A JP2008114161 A JP 2008114161A JP 2006300159 A JP2006300159 A JP 2006300159A JP 2006300159 A JP2006300159 A JP 2006300159A JP 2008114161 A JP2008114161 A JP 2008114161A
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sludge
tank
storage tank
wastewater treatment
wastewater
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Koji Shimizu
巧治 清水
Takashi Sakakibara
隆司 榊原
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Panasonic Holdings Corp
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Matsushita Electric Industrial Co Ltd
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    • 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
    • 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
    • Y02W10/20Sludge processing

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  • Treatment Of Sludge (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method and an apparatus for treating waste water, by which putrefaction of the sludge in a storage tank for storing the sludge separated at a waste water treatment step can be prevented and production of a bad smell can be prevented by a simple and compact constitution. <P>SOLUTION: In the apparatus for treating the waste water which has the storage tank 7 for storing the sludge separated at the waste water treatment step, an upper underwater pump 11 for discharging the sludge toward the bottom of the storage tank 7 is arranged in the vicinity of the inner peripheral wall of the storage tank 7 to circulate the sludge vertically in the storage tank 7 and uniformize the dissolved oxygen amount in the whole sludge in the storage tank 7 so that the putrefaction of the sludge is prevented and the production of scum and the bad smell is prevented even when the storage tank is the deep one having a small installation area. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

本発明は排水処理方法及び装置に関し、特に貯留槽に汚泥を貯留する工程を有する排水処理方法及び装置に関するものである。   The present invention relates to a wastewater treatment method and apparatus, and more particularly to a wastewater treatment method and apparatus having a step of storing sludge in a storage tank.

従来、図3に示すように、排水を受け入れる調整槽21と、調整槽21から排水を取り出して活性汚泥の存在下で曝気処理する曝気槽22と、曝気槽22で処理された排水を受け入れて汚泥と処理水に分離する沈殿槽23とを備え、沈殿槽23から取り出した汚泥を曝気槽22と汚泥処理装置24に送給し、排水を生物化学的に処理するようにした排水処理装置において、沈殿槽23に取り込む汚泥表面のスカムを掻き寄せて除去し、汚泥処理装置24で処理するようにしたものが知られている(例えば、特許文献1参照)。   Conventionally, as shown in FIG. 3, an adjustment tank 21 that receives wastewater, an aeration tank 22 that takes out the wastewater from the adjustment tank 21 and performs aeration treatment in the presence of activated sludge, and receives wastewater that has been treated in the aeration tank 22. In a wastewater treatment apparatus comprising a sedimentation tank 23 for separating sludge and treated water, the sludge taken out from the sedimentation tank 23 is fed to an aeration tank 22 and a sludge treatment apparatus 24, and wastewater is treated biochemically. The sludge surface scum taken into the sedimentation tank 23 is scraped and removed and treated by the sludge treatment device 24 (for example, see Patent Document 1).

また、汚泥の濃縮槽において、嫌気性になって汚泥が腐敗するのを防止するため、濃縮槽の底から汚泥ポンプにて汚泥を引き抜いてエアレーションを行って濃縮槽への給泥筒内に戻すようにしたものが知られている(例えば、特許文献2参照)。   Also, in order to prevent the sludge from becoming anaerobic and decaying in the sludge concentration tank, the sludge is extracted from the bottom of the concentration tank with a sludge pump and aerated to return it to the supply tank to the concentration tank. What was made is known (for example, refer patent document 2).

また、汚泥を発酵させてコンポストを製造する設備等において、汚泥を貯留する貯留ホッパーの底部にパドルを付設した攪拌軸と散気管を配設することで、貯留ホッパー内が嫌気性になって汚泥が腐敗し、悪臭を発するのを防止するようにしたものも知られている(例えば、特許文献3参照)。
特許第3167270号明細書 特開2006−87970号公報 特許第3582699号明細書
In addition, in facilities that ferment sludge and produce compost, etc., a stirrer shaft and a diffuser pipe with a paddle attached to the bottom of the storage hopper that stores sludge are made anaerobic in the storage hopper. It is also known to prevent rot and odor from occurring (see, for example, Patent Document 3).
Japanese Patent No. 3167270 JP 2006-87970 A Japanese Patent No. 3582699

ところが、特許文献1に記載されているように、排水処理工程で表面に浮上したスカムを除去して処理するようにした構成では、発生したスカムを処理するものであるため、汚泥を貯留する貯留槽に適用したとしても、貯留槽で汚泥が腐敗してスカムが浮上し、悪臭が発生するのを防止することはできないという問題がある。   However, as described in Patent Document 1, in the configuration in which the scum that floats on the surface in the wastewater treatment process is removed and processed, the generated scum is processed, so that the sludge is stored. Even if it is applied to the tank, there is a problem that it is impossible to prevent the sludge from rotting in the storage tank and the scum rising and generating a bad odor.

また、特許文献2に記載されているように、汚泥の腐敗を防止するため濃縮槽の底部から汚泥ポンプで汚泥を引き抜いてエアシーションして戻すようにした構成では、設備構成が複雑かつ大掛かりとなるため、設備コストが高くなるとともに大きな設置面積が必要になるという問題がある。また、特許文献3に記載された構成においても、貯留ホッパーの底部に複雑な装置構成を配設する必要があるため、設備コストが高くなるという問題がある。   In addition, as described in Patent Document 2, the configuration in which the sludge is pulled out from the bottom of the concentration tank with a sludge pump and air-sealed back to prevent the sludge from decaying is complicated and large. Therefore, there is a problem that the equipment cost increases and a large installation area is required. Further, the configuration described in Patent Document 3 also has a problem that the equipment cost increases because it is necessary to arrange a complicated device configuration at the bottom of the storage hopper.

本発明は、上記従来の問題点に鑑み、排水処理工程から分離された汚泥を貯留する貯留槽での汚泥の腐敗と悪臭の発生を簡単かつコンパクトな構成で防止できる排水処理方法及び装置を提供することを目的とする。   In view of the above-mentioned conventional problems, the present invention provides a wastewater treatment method and apparatus capable of preventing the sludge decay and odor generation in a storage tank for storing sludge separated from a wastewater treatment process with a simple and compact configuration. The purpose is to do.

本発明の排水処理方法は、排水処理工程から分離された汚泥を貯留槽に貯留する工程を有する排水処理方法において、貯留槽の内周壁の近傍に配設した水中ポンプにて貯留槽の底部に向けて汚泥を送出して汚泥を循環させるものである。なお、貯留槽が角型の場合にはその角隅部に水中ポンプを配置するのが好適である。   The wastewater treatment method of the present invention is a wastewater treatment method having a step of storing sludge separated from the wastewater treatment step in a storage tank, and a submersible pump disposed in the vicinity of the inner peripheral wall of the storage tank at the bottom of the storage tank. The sludge is sent out to circulate the sludge. In addition, when a storage tank is a square shape, it is suitable to arrange | position a submersible pump in the corner part.

この構成によれば、排水処理工程から分離された汚泥を貯留槽に貯留した状態で、貯留槽の内周壁の近傍、特に角型の場合にその角隅部に配設した水中ポンプを作動させると、貯留槽内の汚泥の表面近傍の溶存酸素量が比較的多い汚泥が貯留槽の底部に向けて流動されることで、貯留槽の深さが深い場合でもその底部の角隅部の汚泥も効果的に流動され、貯留槽内全体の汚泥が有効に循環されて溶存酸素量が全体に均一化される。かくして、設置平面積が小さくかつ深さの深い貯留槽であっても、貯留槽内全体の汚泥の腐敗を防止して、スカム及び悪臭の発生を防止することができる。しかも、貯留槽内に水中ポンプを配置するだけで良いので、設備コストが安価で済むとともに循環装置の設置スペースを別途に必要としないため、貯留槽での汚泥の腐敗と悪臭の発生を簡単かつコンパクトな構成で防止できる。   According to this configuration, in a state where the sludge separated from the wastewater treatment process is stored in the storage tank, the submersible pump disposed near the inner peripheral wall of the storage tank, particularly in the case of a rectangular shape, is operated. In addition, sludge with a relatively large amount of dissolved oxygen near the surface of the sludge in the storage tank flows toward the bottom of the storage tank, so even if the depth of the storage tank is deep, the sludge at the corner of the bottom The sludge throughout the storage tank is effectively circulated and the dissolved oxygen amount is made uniform throughout. Thus, even in a storage tank having a small installation plane area and a deep depth, the sludge in the entire storage tank can be prevented from being spoiled and the occurrence of scum and malodor can be prevented. Moreover, since it is only necessary to place a submersible pump in the storage tank, the equipment cost is low, and no additional installation space for the circulation device is required. This can be prevented with a compact configuration.

また、貯留槽の底部から上方に向けて水中ポンプにて汚泥を送出して汚泥の流れに乱流を生じさせると、貯留槽内で汚泥の流れが乱流状態となることで、槽内の汚泥の溶存酸素量をさらに全体的に均一化でき、スカムの発生をより効果的に防止することができる。なお、槽底部に配設する水中ポンプとしては、吐出量が槽上部の水中ポンプの1.5倍以上のものを採用し、それを槽の中央部に配設することにより、上記作用がより確実に得られて好適である。   In addition, when sludge is sent from the bottom of the storage tank upward by a submersible pump to cause turbulent flow in the sludge flow, the sludge flow becomes turbulent in the storage tank. The amount of dissolved oxygen in the sludge can be made more uniform overall, and the occurrence of scum can be more effectively prevented. As the submersible pump installed at the bottom of the tank, a pump with a discharge rate of 1.5 times or more than the submersible pump at the top of the tank is adopted, and it is arranged at the central part of the tank, so that the above action is more effective. It can be obtained reliably and is suitable.

また、排水処理工程が、生物処理槽で活性汚泥の存在下で曝気処理した排水を沈殿槽にて汚泥と処理水に分離し、分離した汚泥を生物処理槽と貯留槽に送出するものである場合に、上記構成を適用すると分離した汚泥の貯留に効果的である。   In addition, the wastewater treatment process separates the wastewater aerated in the presence of activated sludge in the biological treatment tank into sludge and treated water in the sedimentation tank, and sends the separated sludge to the biological treatment tank and the storage tank. In some cases, application of the above configuration is effective for storing separated sludge.

また、貯留槽に貯留している汚泥を逐次曝気槽に取り出し、曝気槽の汚泥を逐次取り出して再基質化し、再基質化汚泥を曝気槽と排水処理工程に戻し、曝気槽で膜透過させた透過水を排水処理工程に戻す汚泥処理工程を有すると、貯留された汚泥の処理を効果的に行うことができる。   In addition, the sludge stored in the storage tank is sequentially taken out to the aeration tank, the sludge in the aeration tank is taken out sequentially to be re-substrate, the re-substrate sludge is returned to the aeration tank and the wastewater treatment process, and the membrane is permeated in the aeration tank. When it has the sludge treatment process which returns permeate to a wastewater treatment process, the processing of the stored sludge can be performed effectively.

また、本発明の排水処理装置は、排水処理工程から分離された汚泥を貯留する貯留槽を備えた排水処理装置において、貯留槽の内周壁の近傍に、貯留槽の底部に向けて汚泥を送出して汚泥を循環させる水中ポンプを配設したものであり、上記排水処理方法を実施してその効果を奏することができる。   The wastewater treatment apparatus of the present invention is a wastewater treatment apparatus having a storage tank for storing sludge separated from the wastewater treatment process, and sends the sludge to the bottom of the storage tank in the vicinity of the inner peripheral wall of the storage tank. And the submersible pump which circulates sludge is arrange | positioned, The effect | action can be show | played by implementing the said waste_water | drain processing method.

また、貯留槽の底部に、上方に向けて汚泥を送出する水中ポンプを配設すると、貯留槽内での汚泥の流れに乱流を生じさせることができて、槽内の汚泥の溶存酸素量をさらに全体的に均一化でき、スカムの発生をより効果的に防止することができる。   In addition, if a submersible pump that sends sludge upwards is installed at the bottom of the storage tank, turbulent flow can be generated in the sludge flow in the storage tank, and the amount of dissolved oxygen in the sludge in the tank Can be made uniform overall, and the occurrence of scum can be more effectively prevented.

また、排水処理工程が、活性汚泥の存在下で排水を曝気処理する生物処理槽と、生物処理槽で処理された排水を受け入れて汚泥と処理水に分離する沈殿槽とを備え、沈殿槽で分離した汚泥を生物処理槽と貯留槽に送出するように構成されている場合に、上記貯留槽の構成を適用すると汚泥の貯留に効果的である。   In addition, the wastewater treatment process includes a biological treatment tank for aeration treatment of wastewater in the presence of activated sludge and a precipitation tank for receiving wastewater treated in the biological treatment tank and separating it into sludge and treated water. When the separated sludge is configured to be sent to the biological treatment tank and the storage tank, applying the above-described storage tank configuration is effective for storing the sludge.

また、貯留槽と、貯留槽から汚泥を逐次取り出して曝気処理する曝気槽と、曝気槽の汚泥を逐次取り出して再基質化する再基質化装置と、曝気槽から膜透過にて水を分離する膜分離装置にて汚泥処理工程が構成されており、膜分離装置で分離した水は排水処理工程に戻し、再基質化汚泥は曝気槽と排水処理工程に戻すように構成されていると、貯留された汚泥の処理を効果的に行うことができる。   In addition, water is separated from the aeration tank by membrane permeation, a storage tank, an aeration tank that sequentially removes sludge from the storage tank and performs aeration treatment, a re-substrateing device that sequentially extracts sludge from the aeration tank and converts it into a re-substrate. When the sludge treatment process is configured in the membrane separator, the water separated by the membrane separator is returned to the wastewater treatment process, and the re-substrate sludge is stored in the aeration tank and wastewater treatment process. The treated sludge can be effectively processed.

本発明の排水処理方法及び装置によれば、貯留槽の内周壁の近傍に配設した水中ポンプにて溶存酸素量が比較的多い表面近傍の汚泥が貯留槽の底部に向けて流動されることで、貯留槽内全体の汚泥の溶存酸素量が全体に均一化され、設置平面積が小さくかつ深さの深い貯留槽であっても貯留槽内全体の汚泥の腐敗を防止してスカム及び悪臭の発生を防止でき、かつ貯留槽内に水中ポンプを配置するだけなので設備コストの低下と省スペースを図ることができる。   According to the wastewater treatment method and apparatus of the present invention, the sludge near the surface having a relatively large amount of dissolved oxygen flows toward the bottom of the storage tank by a submersible pump disposed in the vicinity of the inner peripheral wall of the storage tank. Therefore, the amount of dissolved oxygen in the sludge in the entire storage tank is made uniform throughout, and even in a storage tank with a small installation flat area and deep depth, the sludge in the entire storage tank is prevented from being spoiled and scum and odor Can be prevented and the submersible pump is simply arranged in the storage tank, so that the equipment cost can be reduced and the space can be saved.

以下、本発明の排水処理方法及び装置の一実施形態について、図1、図2を参照して説明する。   Hereinafter, an embodiment of the wastewater treatment method and apparatus of the present invention will be described with reference to FIGS. 1 and 2.

図1において、1は排水源から排水が流入する調整槽で、その底部に曝気装置2が配設されている。調整槽1内に貯留された排水は、ポンプ(図示せず)にて、 生物処理槽3に供給される。生物処理槽3には、排水を処理する微生物を担持する微生物担持繊維体を揺動可能に支持した揺動微生物担持体(図示せず)が配設され、底部には噴気口が全面に分散配置された曝気装置4が配設されている。   In FIG. 1, reference numeral 1 denotes an adjustment tank into which drainage flows from a drainage source, and an aeration device 2 is disposed at the bottom thereof. The waste water stored in the adjustment tank 1 is supplied to the biological treatment tank 3 by a pump (not shown). The biological treatment tank 3 is provided with an oscillating microorganism carrier (not shown) that supports a microorganism-carrying fiber body that carries microorganisms for treating the waste water so that the microorganisms can be oscillated. The arranged aeration device 4 is arranged.

生物処理槽3で処理された後の排水は、ポンプ(図示せず)にて沈殿槽5に送られ、この沈殿槽5で排水中に浮遊した微生物から成る活性汚泥が沈降分離され、清浄化された処理水が系外に放流される。沈殿槽5で分離された活性汚泥は、一部が生物処理槽3に還流されるとともに、残部の余剰汚泥は汚泥処理部6に送給される。   The wastewater after being treated in the biological treatment tank 3 is sent to a sedimentation tank 5 by a pump (not shown), and activated sludge composed of microorganisms floating in the wastewater is settled and separated in this sedimentation tank 5 and purified. The treated water is discharged out of the system. Part of the activated sludge separated in the sedimentation tank 5 is returned to the biological treatment tank 3, and the remaining surplus sludge is fed to the sludge treatment section 6.

汚泥処理部6は、沈殿槽5から送給された活性汚泥を貯留する貯留槽7と、貯留槽7から堰(図示せず)を越流した活性汚泥が供給される曝気槽8と、曝気槽8中の水を分離して抽出する膜分離装置9と、曝気槽8から活性汚泥を取り出して再基質化し、曝気槽8に還流させる再基質化手段としての超音波汚泥削減装置10とを備えている。   The sludge treatment unit 6 includes a storage tank 7 that stores the activated sludge fed from the settling tank 5, an aeration tank 8 that is supplied with activated sludge that has overflowed a weir (not shown) from the storage tank 7, and an aeration A membrane separation device 9 that separates and extracts the water in the tank 8 and an ultrasonic sludge reduction device 10 as a re-substrate forming means for taking activated sludge from the aeration tank 8 to re-substrate and recirculating it to the aeration tank 8. I have.

貯留槽7は、小さな設置面積で十分な容積を確保するため、平面積が小さく深さの深い直方体状の槽にて構成されており、図2に示すように、沈殿槽5から送給された汚泥は貯留槽7の1つの角隅部に流入される。貯留槽7の他の3つの角隅部の上部には、貯留槽7の液面近くの汚泥を吸入して底部に向けて送出し、貯留槽7内で汚泥を上下に循環させる上部水中ポンプ11が配設されている。また、貯留槽7の底部の中央部には、底部の汚泥を吸入して上方に向けて送出する底部水中ポンプ12が配設されている。底部水中ポンプ12には、吐出量が上部水中ポンプ11の1.5倍以上のものが適用されている。また、上部水中ポンプ11はその吸い込み口が液面下2〜5cmに位置し、底部水中ポンプ12はその吸い込み口が槽底面から2cm程度に位置するように配置されている。   In order to secure a sufficient volume with a small installation area, the storage tank 7 is configured by a rectangular parallelepiped tank having a small flat area and a deep depth, and is fed from the sedimentation tank 5 as shown in FIG. The sludge flows into one corner of the storage tank 7. An upper submersible pump that sucks sludge near the liquid surface of the storage tank 7 and sends it toward the bottom at the top of the other three corners of the storage tank 7 and circulates the sludge up and down in the storage tank 7. 11 is disposed. In addition, a bottom submersible pump 12 that sucks sludge at the bottom and sends it upward is disposed at the center of the bottom of the storage tank 7. The bottom submersible pump 12 has a discharge amount 1.5 times or more that of the upper submersible pump 11. The upper submersible pump 11 has a suction port located 2 to 5 cm below the liquid level, and the bottom submersible pump 12 is arranged so that the suction port is located about 2 cm from the bottom of the tank.

曝気槽8には、その底部に曝気装置12が配設され、再基質化汚泥が活性汚泥による好気性消化によって窒素と水に分解される。その水は膜分離装置9で分離抽出されて沈殿槽5に還流され、沈殿槽5を介して系外に放流される。また、超音波汚泥削減装置10から還流される再基質化汚泥の一部は生物処理槽3に還流され、この生物処理槽3で分解される。   The aeration tank 8 is provided with an aeration device 12 at the bottom thereof, and the re-substrate sludge is decomposed into nitrogen and water by aerobic digestion with activated sludge. The water is separated and extracted by the membrane separation device 9, refluxed to the precipitation tank 5, and discharged outside the system through the precipitation tank 5. In addition, a part of the resubstrate sludge that is recirculated from the ultrasonic sludge reduction device 10 is recirculated to the biological treatment tank 3 and decomposed in the biological treatment tank 3.

以上の構成の排水処理装置において、排水源から排出された排水は調整槽1に受け入れられ、曝気装置2にて曝気処理される。次いで、調整槽1から生物処理槽3に排水が取り出され、生物処理槽3で活性汚泥の存在下で曝気装置4にて曝気されて、排水中の有機物が活性汚泥にて分解処理される。その後、処理排水と活性汚泥は沈殿槽5に取り出され、沈殿槽5で汚泥と処理水に分離され、分離された処理水は系外に放流され、分離された汚泥の一部は生物処理槽3に還流され、残部の余剰汚泥が汚泥処理部6の貯留槽7に送出される。   In the wastewater treatment apparatus having the above configuration, the wastewater discharged from the wastewater source is received by the adjustment tank 1 and aerated by the aeration apparatus 2. Next, the waste water is taken out from the adjustment tank 1 to the biological treatment tank 3 and aerated by the aeration apparatus 4 in the presence of activated sludge in the biological treatment tank 3, and the organic matter in the waste water is decomposed by the activated sludge. Thereafter, the treated wastewater and activated sludge are taken out into the sedimentation tank 5, separated into sludge and treated water in the sedimentation tank 5, the separated treated water is discharged out of the system, and a part of the separated sludge is biological treatment tank. The remaining excess sludge is sent to the storage tank 7 of the sludge treatment unit 6.

排水処理工程から送出された汚泥は貯留槽7に貯留される。この貯留状態で、貯留槽7の上部の角隅部に配設された上部水中ポンプ11が作動することで、貯留槽7の表面近傍の溶存酸素量が比較的多い汚泥が、図1に白抜き矢印で示すように、貯留槽7の底部に向けて流動され、貯留槽7内の汚泥が上下に循環される。また、貯留槽7の底部中央部に配設された底部水中ポンプ12が作動することで、貯留槽7の底部中央部の汚泥が上方に向けて流動され、上記貯留槽7内での汚泥の上下循環が強化されるとともに、底部に向けて流動する汚泥流の一部と衝突して乱流を発生させることになる。これによって、貯留槽7の深さが深い場合でもその底部の角隅部の汚泥も効果的に流動されるとともに全体的に均一化されるため、貯留槽7内全体の汚泥が有効に循環・混合され、汚泥中の溶存酸素量が、微生物が死滅しない最低限の溶存酸素量に全体に均一化される。かくして、設置面積が小さくかつ深さの深い貯留槽7であっても、貯留槽7内の全体の汚泥の腐敗を防止して、スカム及び悪臭の発生を防止することができる。   The sludge sent from the waste water treatment process is stored in the storage tank 7. In this storage state, when the upper submersible pump 11 disposed at the upper corner of the storage tank 7 is operated, sludge having a relatively large amount of dissolved oxygen near the surface of the storage tank 7 is shown in FIG. As indicated by the extraction arrow, the fluid flows toward the bottom of the storage tank 7 and the sludge in the storage tank 7 is circulated up and down. In addition, when the bottom submersible pump 12 disposed in the center of the bottom of the storage tank 7 is activated, the sludge in the center of the bottom of the storage tank 7 flows upward, and the sludge in the storage tank 7 is The vertical circulation is strengthened, and a turbulent flow is generated by colliding with a part of the sludge flow flowing toward the bottom. As a result, even when the depth of the storage tank 7 is deep, the sludge at the corners of the bottom is also effectively flowed and uniformly made uniform, so that the entire sludge in the storage tank 7 is effectively circulated and When mixed, the amount of dissolved oxygen in the sludge is uniformized to the minimum amount of dissolved oxygen that does not kill the microorganisms. Thus, even if the storage tank 7 has a small installation area and a deep depth, the entire sludge in the storage tank 7 can be prevented from decaying and the occurrence of scum and odors can be prevented.

貯留槽7の汚泥は曝気槽8に逐次取り出される。曝気槽8の汚泥は超音波汚泥削減装置10に逐次取り出されて再基質化され、再基質化汚泥は一部が排水処理工程の生物処理槽3に還流されて処理が行われるとともに、残部が曝気槽8に還流されて曝気処理によって窒素と水に分解される。分解された水は膜分離装置9にて分離され、排水処理工程の沈澱槽5に還流され、沈澱槽5から処理水として系外に放流される。以上のようにして汚泥処理部6にて貯留槽7に貯留された汚泥が逐次処理される。   The sludge in the storage tank 7 is sequentially taken out to the aeration tank 8. The sludge in the aeration tank 8 is sequentially taken out by the ultrasonic sludge reduction device 10 and converted into a re-substrate, and a part of the re-substrate converted sludge is returned to the biological treatment tank 3 in the waste water treatment process and the remainder is processed. It is returned to the aeration tank 8 and decomposed into nitrogen and water by aeration treatment. The decomposed water is separated by the membrane separation device 9, is refluxed to the precipitation tank 5 in the waste water treatment process, and is discharged out of the system as treated water from the precipitation tank 5. As described above, the sludge stored in the storage tank 7 is sequentially processed in the sludge treatment unit 6.

本実施形態によれば、上記のように設置面積が小さくかつ深さの深い貯留槽7であっても汚泥の腐敗を防止してスカム及び悪臭の発生を防止することができ、しかも貯留槽7内に底部水中ポンプ11と底部水中ポンプ12を配置するだけで良いので、設備コストが安価で済むとともに循環装置の設置スペースを別途に必要とせず、貯留槽7での汚泥の腐敗と悪臭の発生を簡単かつコンパクトな構成で防止することができる。   According to this embodiment, even if it is the storage tank 7 with a small installation area and a deep depth as described above, it is possible to prevent the decay of sludge and prevent the occurrence of scum and odor, and the storage tank 7. Since only the bottom submersible pump 11 and the bottom submersible pump 12 need to be arranged in the inside, the equipment cost can be reduced and no additional installation space for the circulation device is required. Can be prevented with a simple and compact configuration.

本発明の排水処理方法及び装置は、貯留槽の内周壁の近傍に配設した水中ポンプにて溶存酸素量が比較的多い表面近傍の汚泥が貯留槽の底部に向けて流動されることで、貯留槽内全体の汚泥の溶存酸素量が全体に均一化され、設置面積が小さくかつ深さの深い貯留槽であっても貯留槽内全体の汚泥の腐敗を防止してスカム及び悪臭の発生を防止でき、かつ貯留槽内に水中ポンプを配置するだけなので設備コストの低下と省スペースを図ることができるので、各種排水処理設備に好適に適用することができる。   The wastewater treatment method and apparatus of the present invention is such that the sludge near the surface with a relatively large amount of dissolved oxygen flows toward the bottom of the storage tank by a submersible pump arranged in the vicinity of the inner peripheral wall of the storage tank. The amount of dissolved oxygen in the entire sludge tank is made uniform throughout, and even if the storage space is small and deep, the sludge in the whole reservoir is prevented from decaying and scum and odors are generated. This can be prevented, and since only the submersible pump is arranged in the storage tank, the equipment cost can be reduced and the space can be saved. Therefore, it can be suitably applied to various wastewater treatment facilities.

本発明の一実施形態の排水処理装置の構成図。The block diagram of the waste water treatment equipment of one embodiment of the present invention. 同実施形態の貯留槽の模式平面図。The schematic plan view of the storage tank of the embodiment. 従来例の排水処理装置の構成図。The block diagram of the waste water treatment apparatus of a prior art example.

符号の説明Explanation of symbols

3 生物処理槽
5 沈澱槽
7 貯留槽
8 曝気槽
9 膜分離装置
10 超音波汚泥削減装置(再基質化装置)
11 上部水中ポンプ
12 底部水中ポンプ
3 Biotreatment tank 5 Precipitation tank 7 Storage tank 8 Aeration tank 9 Membrane separation device 10 Ultrasonic sludge reduction device (re-substrateing device)
11 Upper submersible pump 12 Bottom submersible pump

Claims (8)

排水処理工程から分離された汚泥を貯留槽に貯留する工程を有する排水処理方法において、貯留槽の内周壁の近傍に配設した水中ポンプにて貯留槽の底部に向けて汚泥を送出して汚泥を循環させることを特徴とする排水処理方法。   In the wastewater treatment method having a step of storing the sludge separated from the wastewater treatment step in the storage tank, the sludge is sent to the bottom of the storage tank by a submersible pump disposed in the vicinity of the inner peripheral wall of the storage tank. A wastewater treatment method characterized by circulating water. 貯留槽の底部から上方に向けて水中ポンプにて汚泥を送出して汚泥の流れに乱流を生じさせることを特徴とする請求項1記載の排水処理方法。   The wastewater treatment method according to claim 1, wherein sludge is sent out by a submersible pump from the bottom of the storage tank upward to generate turbulent flow in the sludge flow. 排水処理工程は、生物処理槽で活性汚泥の存在下で曝気処理した排水を沈殿槽にて汚泥と処理水に分離し、分離した汚泥を生物処理槽と貯留槽に送出することを特徴とする請求項1又は2記載の排水処理方法。   The wastewater treatment step is characterized in that wastewater aerated in the presence of activated sludge in a biological treatment tank is separated into sludge and treated water in a sedimentation tank, and the separated sludge is sent to the biological treatment tank and the storage tank. The wastewater treatment method according to claim 1 or 2. 貯留槽に貯留している汚泥を逐次曝気槽に取り出し、曝気槽の汚泥を逐次取り出して再基質化し、再基質化汚泥を曝気槽と排水処理工程に戻し、曝気槽で膜透過させた透過水を排水処理工程に戻す汚泥処理工程を有することを特徴とする請求項1〜3の何れかに又は2記載の排水処理方法。   The sludge stored in the storage tank is sequentially taken out to the aeration tank, the sludge from the aeration tank is taken out sequentially to be re-substrate, the re-substrate sludge is returned to the aeration tank and the wastewater treatment process, and the permeated water is permeated through the aeration tank. A wastewater treatment method according to any one of claims 1 to 2, further comprising a sludge treatment step for returning the wastewater to the wastewater treatment step. 排水処理工程から分離された汚泥を貯留する貯留槽を備えた排水処理装置において、貯留槽の内周壁の近傍に、貯留槽の底部に向けて汚泥を送出して汚泥を循環させる水中ポンプを配設したことを特徴とする排水処理装置。   In a wastewater treatment device equipped with a storage tank that stores sludge separated from the wastewater treatment process, an underwater pump that distributes sludge toward the bottom of the storage tank and circulates the sludge is arranged near the inner peripheral wall of the storage tank. Wastewater treatment equipment characterized by having been installed. 貯留槽の底部に、上方に向けて汚泥を送出する水中ポンプを配設したことを特徴とする請求項5記載の排水処理装置。   6. The waste water treatment apparatus according to claim 5, wherein a submersible pump for sending sludge upward is disposed at the bottom of the storage tank. 排水処理工程は、活性汚泥の存在下で排水を曝気処理する生物処理槽と、生物処理槽で処理された排水を受け入れて汚泥と処理水に分離する沈殿槽とを備え、沈殿槽で分離した汚泥を生物処理槽と貯留槽に送出するように構成されていることを特徴とする請求項5又は6記載の排水処理装置。   The wastewater treatment process is equipped with a biological treatment tank for aeration treatment of wastewater in the presence of activated sludge and a precipitation tank for receiving wastewater treated in the biological treatment tank and separating it into sludge and treated water. The wastewater treatment apparatus according to claim 5 or 6, wherein the sludge is configured to be sent to a biological treatment tank and a storage tank. 貯留槽と、貯留槽から汚泥を逐次取り出して曝気処理する曝気槽と、曝気槽の汚泥を逐次取り出して再基質化する再基質化装置と、曝気槽から膜透過にて水を分離する膜分離装置にて汚泥処理工程が構成されており、膜分離装置で分離した水は排水処理工程に戻し、再基質化汚泥は曝気槽と排水処理工程に戻すように構成されていることを特徴とする請求項5〜7の何れかに記載の排水処理装置。   A storage tank, an aeration tank that sequentially removes sludge from the storage tank and performs aeration treatment, a re-substrateing device that sequentially extracts sludge from the aeration tank and converts it into a re-substrate, and membrane separation that separates water from the aeration tank by membrane permeation The apparatus has a sludge treatment process, wherein the water separated by the membrane separation device is returned to the wastewater treatment process, and the re-substrate sludge is returned to the aeration tank and the wastewater treatment process. The waste water treatment apparatus in any one of Claims 5-7.
JP2006300159A 2006-11-06 2006-11-06 Method and apparatus for treating waste water Pending JP2008114161A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011066736A1 (en) * 2009-12-01 2011-06-09 Li Jinmin Sludge treatment method and apparatus thereof and application to wastewater bio-treatment

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011066736A1 (en) * 2009-12-01 2011-06-09 Li Jinmin Sludge treatment method and apparatus thereof and application to wastewater bio-treatment
CN102149645A (en) * 2009-12-01 2011-08-10 李进民 Sludge treatment method and apparatus thereof and application to wastewater bio-treatment
CN102149645B (en) * 2009-12-01 2011-11-16 李进民 Sludge treatment method and apparatus thereof and application to wastewater bio-treatment
JP2013512096A (en) * 2009-12-01 2013-04-11 リ、ジンミン Sludge treatment method using sludge biological treatment method, and sludge treatment apparatus and apparatus
US8932466B2 (en) 2009-12-01 2015-01-13 Jinmin Li Method and apparatus for sluge treatment and use thereof in sewage biotreatment
EA024049B1 (en) * 2009-12-01 2016-08-31 Цзиньминь Ли Sludge treatment method and apparatus and application of said method and apparatus for wastewater bio-treatment

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