JPH0681699U - Oxygen supply device for deep aeration tank - Google Patents

Oxygen supply device for deep aeration tank

Info

Publication number
JPH0681699U
JPH0681699U JP2365693U JP2365693U JPH0681699U JP H0681699 U JPH0681699 U JP H0681699U JP 2365693 U JP2365693 U JP 2365693U JP 2365693 U JP2365693 U JP 2365693U JP H0681699 U JPH0681699 U JP H0681699U
Authority
JP
Japan
Prior art keywords
water
treated
intake pipe
oxygen
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
JP2365693U
Other languages
Japanese (ja)
Inventor
亮一 森峰
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP2365693U priority Critical patent/JPH0681699U/en
Publication of JPH0681699U publication Critical patent/JPH0681699U/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

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Activated Sludge Processes (AREA)

Abstract

(57)【要約】 【目的】 酸素供給能力、攪拌能力ともに十分であり、
かつ動力効率の高い大深度曝気槽用酸素供給装置を提供
する。 【構成】 曝気槽内1に上下方向に設けられる引込管5
と、引込管5内の上部に位置して酸素含有ガスを被処理
水中に分散させる機械式散気装置7と、引込管5内の下
部に位置して、被処理水を引込管5内を下向きに流動さ
せる循環ポンプ8とで酸素供給装置を構成する。 【効果】 引込管内上部で分散された酸素含有ガスの被
処理水への溶解量が水深の増大にしたがって増大するた
め、被処理水に十分量の酸素が供給される。
(57) [Summary] [Purpose] Both oxygen supply capacity and stirring capacity are sufficient,
An oxygen supply device for a deep depth aeration tank having high power efficiency is provided. [Structure] Introducing pipe 5 vertically provided in aeration tank 1
And a mechanical air diffuser 7 located in the upper part of the intake pipe 5 for dispersing the oxygen-containing gas in the water to be treated, and a lower part in the intake pipe 5 for introducing the water to be treated into the intake pipe 5. An oxygen supply device is configured with the circulation pump 8 that causes downward flow. [Effect] Since the amount of the oxygen-containing gas dispersed in the upper part of the intake pipe dissolved in the water to be treated increases as the water depth increases, a sufficient amount of oxygen is supplied to the water to be treated.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、下廃水などの汚水の処理に使用される大深度曝気槽用酸素供給装置 に関する。 The present invention relates to an oxygen supply device for a deep depth aeration tank used for treating wastewater such as sewage.

【0002】[0002]

【従来の技術】[Prior art]

従来、下水などの汚水の処理場では、種々の生物学的処理法が行われている。 例えば、活性汚泥法をはじめとする浮遊形の処理では、被処理水を生物反応槽に 供給し、反応槽内で流動させるとともに曝気を行うことにより、被処理水が生物 反応槽内を流動する間に微生物のはたらきによって被処理水中の窒素分などを除 去している。そのための反応槽は通常、最大でも10m程度の水深で設計・運転 されており、このような反応槽に酸素を供給するための散気板、散気管、機械式 曝気装置などの曝気装置は水深4m前後に設置されている。このときのブロワー の吐出圧は5000mmAq程度であり、1つの曝気装置で曝気できる容量は最 大1000m3 程度である。2. Description of the Related Art Conventionally, various biological treatment methods have been carried out in wastewater treatment plants such as sewage. For example, in the floating type treatment such as the activated sludge method, the water to be treated flows in the biological reaction tank by supplying the water to be treated to the biological reaction tank, causing the water to flow in the reaction tank and performing aeration. In the meantime, the nitrogen content in the water to be treated is removed by the action of microorganisms. The reaction tank for that purpose is usually designed and operated at a water depth of about 10 m at the maximum, and aeration devices such as a diffuser plate, a diffuser pipe, and a mechanical aerator for supplying oxygen to such a reaction tank have a depth of water. It is installed around 4m. The discharge pressure of the blower at this time is about 5000 mmAq, and the maximum aeration capacity of one aeration device is about 1000 m 3 .

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかしながら、処理場用地を十分確保できない大都市では、曝気槽容量の増大 が必要となった場合、反応槽の深さを20m〜30m程度まで深くすることで対 処せざるを得ず、そうなると反応槽の容量が最大3000m3 となって従来の曝 気装置では酸素供給能力、攪拌能力とも十分ではない。また、ブロワの吐出圧が 非常に大きくなり、その結果、曝気装置の動力効率(kWh/kg -O2)が低くなる。However, in a large city where the land for the treatment plant cannot be secured sufficiently, if the aeration tank capacity needs to be increased, the reaction tank must be deepened to a depth of about 20 to 30 m. The maximum capacity is 3000 m 3 and the conventional aerator does not have sufficient oxygen supply capacity and stirring capacity. Moreover, the discharge pressure of the blower becomes very high, and as a result, the power efficiency (kWh / kg -O 2 ) of the aeration device becomes low.

【0004】 本考案は上記問題を解決するもので、酸素供給能力、攪拌能力ともに十分であ り、かつ動力効率の高い曝気装置を提供することを目的とするものである。The present invention solves the above problems, and an object of the present invention is to provide an aerator having sufficient oxygen supply ability and stirring ability and high power efficiency.

【0005】[0005]

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

本考案の大深度曝気槽用酸素供給装置は、曝気槽内の被処理水中に浸漬して設 けられる酸素供給装置であって、前記曝気槽に上下方向に設けられ、上端が槽内 上部で開口するとともに下端が槽内底部で開口する引込管と、この引込管内の上 部に位置して槽外の給気手段から供給される酸素含有ガスを被処理水中に分散さ せる機械式散気装置と、引込管内の下部に位置して、前記機械式散気装置により 酸素含有ガスが分散された被処理水を前記引込管内を下向きに流動させる循環ポ ンプとを備えたものである。 The oxygen supply device for a deep depth aeration tank of the present invention is an oxygen supply device that is installed by immersing it in the water to be treated in the aeration tank. An inlet pipe that is open and has a lower end that opens at the bottom of the tank, and a mechanical diffuser that is located above the inlet pipe and that disperses the oxygen-containing gas supplied from the air supply means outside the tank into the water to be treated. An apparatus and a circulation pump, which is located in the lower part of the intake pipe, allows the water to be treated in which the oxygen-containing gas is dispersed by the mechanical diffuser to flow downward in the intake pipe.

【0006】[0006]

【作用】[Action]

上記構成により、被処理水は、引込管内の上部において機械式散気装置により 酸素含有ガスが分散され、引込管内の下部に設けた循環ポンプと引込管のガイド 作用とにより引込管内を下向きに引込管の下端まで流動させられる。このとき、 酸素含有ガスが散気装置により微細気泡として供給されること、酸素含有ガスの 被処理水への溶解量が水深の増大にともなって増大することの両方に起因して、 被処理水への酸素の溶解量が増大する。また、引込管の下端から流出した被処理 水が引込管の外周側を上昇することにより、槽内に循環流が生起される。この結 果、槽内の被処理水は、十分に酸素が供給される状態において活性汚泥と攪拌混 合されることになるので、深い曝気槽を用いても被処理水を処理できる。 With the above configuration, the water to be treated has the oxygen-containing gas dispersed by the mechanical air diffuser in the upper part of the intake pipe, and is drawn downward in the intake pipe by the circulation pump provided in the lower part of the intake pipe and the guide function of the intake pipe. Allow to flow to the bottom of the tube. At this time, the oxygen-containing gas is supplied as fine bubbles by the air diffuser, and the amount of the oxygen-containing gas dissolved in the water to be treated increases as the water depth increases. The amount of oxygen dissolved in the water increases. Further, the water to be treated flowing out from the lower end of the intake pipe rises on the outer peripheral side of the intake pipe, so that a circulating flow is generated in the tank. As a result, the water to be treated in the tank is agitated and mixed with the activated sludge in a state where oxygen is sufficiently supplied, so that the water to be treated can be treated even by using a deep aeration tank.

【0007】[0007]

【実施例】【Example】

以下、本考案の一実施例の大深度曝気槽用酸素供給装置を図1を参照しながら 説明する。1は曝気槽であり、槽1は槽内に水深20〜30mの被処理水を貯留 可能に構成されていて、槽1内の被処理水中には活性汚泥が混合されている。曝 気槽1の上方には、原水を供給する原水供給管2および図示を省略した後段の沈 殿池などで回収した活性汚泥を曝気槽1に返送する汚泥返送管3が開口しており 、槽1の上部には槽1内の被処理水の一部を流出させる流出管4が設けられてい る。槽1内には、被処理水に浸漬して、槽1の水平方向ほぼ中央の位置に上下方 向に長さ14〜24mの引込管5が設けられており、引込管5の上端は槽1内上 部で水面下に開口するとともに下端は槽1の底面から約2mの位置で開口してい る。引込管5内の上部であって水面下2〜4mの位置には、槽1外のブロワー6 などの給気手段に接続して機械式散気装置7が設けられており、この機械式散気 装置7により、ブロワー6から供給される酸素含有ガスを引込管5の上部におい て被処理水に分散させるようになっている。また、引込管5内の下部であって水 深10〜20mの位置には循環ポンプ8が設けられていて、この循環ポンプ8に より、引込管5内の被処理水を1.5m/秒以上の流速で下向きに流動させ、引 込管5の下端から流出させるように構成されている。このとき、引込管5の下端 から流出した被処理水が引込管5の外周側を上昇することにより、曝気槽1内に 槽内循環流が生起されるようになっている。 An oxygen supply device for a deep aeration tank according to an embodiment of the present invention will be described below with reference to FIG. Reference numeral 1 denotes an aeration tank, and the tank 1 is configured to be able to store the water to be treated having a water depth of 20 to 30 m, and the water to be treated in the tank 1 is mixed with activated sludge. Above the aeration tank 1, there are opened a raw water supply pipe 2 for supplying raw water and a sludge return pipe 3 for returning the activated sludge collected in a sedimentation pond at a later stage (not shown) to the aeration tank 1, An outflow pipe 4 for outflowing a part of the water to be treated in the tank 1 is provided above the tank 1. Inside the tank 1, a lead-in pipe 5 having a length of 14 to 24 m is installed in a substantially central position in the horizontal direction of the tank 1 so as to extend upward and downward, and the upper end of the lead-in pipe 5 is a tank. It opens below the water surface in the upper part of 1 and the lower end opens about 2 m from the bottom of tank 1. A mechanical air diffuser 7 is provided in the upper part of the intake pipe 5 and at a position 2 to 4 m below the water surface, connected to an air supply means such as a blower 6 outside the tank 1, and the mechanical air diffuser 7 is provided. The vaporizer 7 is adapted to disperse the oxygen-containing gas supplied from the blower 6 in the water to be treated at the upper part of the intake pipe 5. Further, a circulation pump 8 is provided at a lower portion of the intake pipe 5 and at a water depth of 10 to 20 m, and the treated water in the intake pipe 5 is 1.5 m / sec by the circulation pump 8. It is configured to flow downward at the above flow rate and to flow out from the lower end of the intake pipe 5. At this time, the water to be treated flowing out from the lower end of the intake pipe 5 rises on the outer peripheral side of the intake pipe 5, so that an in-tank circulation flow is generated in the aeration tank 1.

【0008】 以下、上記構成における作用を説明する。槽1では、原水供給管2から原水が 供給され、汚泥返送管3から汚泥が返送される状態において、槽1内の被処理水 が生物学的に処理されるとともに、槽1内の被処理水の一部が流出管4から流出 していく。槽1内の被処理水は、引込管5の上端から引込管5内に流入し、管5 内の上部においてブロワー6より機械式散気装置7を通じて供給された酸素含有 ガスと混合される。次いで被処理水は、循環ポンプ8の作用により引込管5内を 下向きに流動してその下端から流出し、引込管5の外側を上昇する。このとき酸 素含有ガスは、機械式散気装置7より微細気泡として分散され、その気泡の上昇 速度より速い流速で下向きに流動する被処理水中にまき込まれることによってさ らに微細な気泡とされる。そしてこの微細気泡が、水深に応じた溶解度の増大に したがって高効率で被処理水中に溶け込むため、被処理水に十分量の酸素が供給 されることになる。この結果、被処理水は、引込管5内において十分かつ確実に 酸素が供給されるとともに、引込管5の内外で活性汚泥と良好に攪拌混合される ことになるので、水深の深い曝気槽1においても十分活性汚泥法を行うことがで きる。The operation of the above configuration will be described below. In the tank 1, raw water is supplied from the raw water supply pipe 2 and sludge is returned from the sludge return pipe 3, the treated water in the tank 1 is biologically treated, and the treated water in the tank 1 is treated. Part of the water flows out from the outflow pipe 4. The water to be treated in the tank 1 flows into the intake pipe 5 from the upper end of the intake pipe 5, and is mixed with the oxygen-containing gas supplied from the blower 6 through the mechanical diffuser 7 in the upper part of the pipe 5. Then, the water to be treated flows downward in the intake pipe 5 by the action of the circulation pump 8, flows out from the lower end thereof, and rises outside the intake pipe 5. At this time, the oxygen-containing gas is dispersed as fine bubbles by the mechanical air diffusing device 7, and is dispersed into the water to be treated flowing downward at a flow velocity faster than the ascending velocity of the bubbles, thereby forming fine bubbles. To be done. Since the fine bubbles dissolve in the water to be treated with high efficiency due to the increase in solubility according to the water depth, a sufficient amount of oxygen is supplied to the water to be treated. As a result, the water to be treated is sufficiently and surely supplied with oxygen in the intake pipe 5, and is well agitated and mixed with the activated sludge inside and outside the intake pipe 5, so that the aeration tank 1 with a deep water depth is provided. Even in Japan, the activated sludge method can be sufficiently performed.

【0009】 上記において、酸素含有ガスの気泡は、槽1の上部から下部へ、下部から上部 へと水深を2回利用することになるので、酸素溶解効率が従来の最大20%から 50%へと高くなり、動力効率も従来の最大2.0kwh/kg -O2へから3.5kwh/ kg -O2へと高くなる。In the above, since the bubbles of the oxygen-containing gas use the water depth twice from the upper part to the lower part of the tank 1 and from the lower part to the upper part, the oxygen dissolution efficiency is increased from the conventional maximum of 20% to 50%. and it increases the power efficiency increases to conventional maximum 2.0kwh / kg -O 2 Hekara 3.5kwh / kg -O 2.

【0010】[0010]

【考案の効果】[Effect of device]

以上述べたように、本考案によれば、引込管の上部で機械式散気装置より微細 気泡としての酸素を被処理水に供給し、この被処理水を循環ポンプにより引込管 内を下降させて、被処理水への酸素の溶解量を増大させる構成としたことにより 、槽内の被処理水に十分な酸素を供給できる。また引込管内の下降流により槽内 に循環流が生起されて、被処理水と活性汚泥とが良好に攪拌混合される。この結 果、深度の大きい曝気槽において、被処理水に十分かつ確実に酸素を供給し、被 処理水と活性汚泥とを良好に攪拌混合する状態で活性汚泥処理を行うことができ る。このとき、動力効率も高くなる。 As described above, according to the present invention, oxygen as fine bubbles is supplied to the water to be treated at the upper part of the intake pipe by the mechanical air diffuser, and the water to be treated is lowered in the intake pipe by the circulation pump. With the configuration in which the amount of oxygen dissolved in the water to be treated is increased, sufficient oxygen can be supplied to the water to be treated in the tank. Further, a downward flow in the intake pipe causes a circulating flow in the tank, and the water to be treated and the activated sludge are well mixed with stirring. As a result, in an aeration tank with a large depth, activated sludge treatment can be performed in a state where oxygen is sufficiently and reliably supplied to the treated water and the treated water and the activated sludge are well stirred and mixed. At this time, power efficiency is also high.

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

【図1】本考案の一実施例の大深度曝気槽用酸素供給装
置を示した説明図である。
FIG. 1 is an explanatory view showing an oxygen supply device for a deep depth aeration tank according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 曝気槽 5 引込管 6 ブロワー(給気手段) 7 機械式散気装置 8 循環ポンプ 1 Aeration tank 5 Intake pipe 6 Blower (air supply means) 7 Mechanical air diffuser 8 Circulation pump

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 曝気槽内の被処理水中に浸漬して設けら
れる酸素供給装置であって、前記曝気槽に上下方向に設
けられ、上端が槽内上部で開口するとともに下端が槽内
底部で開口する引込管と、この引込管内の上部に位置し
て槽外の給気手段から供給される酸素含有ガスを被処理
水中に分散させる機械式散気装置と、引込管内の下部に
位置して、前記機械式散気装置により酸素含有ガスが分
散された被処理水を前記引込管内を下向きに流動させる
循環ポンプとを備えたことを特徴とする大深度曝気槽用
酸素供給装置。
1. An oxygen supply device provided by being immersed in water to be treated in an aeration tank, the oxygen supply device being provided in the aeration tank in a vertical direction, with an upper end opening at an upper part of the tank and a lower end being a bottom part of the tank. An opening intake pipe, a mechanical air diffuser located in the upper part of this intake pipe to disperse the oxygen-containing gas supplied from the air supply means outside the tank into the water to be treated, and a lower part inside the intake pipe An oxygen supply apparatus for a deep depth aeration tank, comprising: a circulation pump that causes the water to be treated in which the oxygen-containing gas is dispersed by the mechanical air diffuser to flow downward in the intake pipe.
JP2365693U 1993-05-10 1993-05-10 Oxygen supply device for deep aeration tank Pending JPH0681699U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2365693U JPH0681699U (en) 1993-05-10 1993-05-10 Oxygen supply device for deep aeration tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2365693U JPH0681699U (en) 1993-05-10 1993-05-10 Oxygen supply device for deep aeration tank

Publications (1)

Publication Number Publication Date
JPH0681699U true JPH0681699U (en) 1994-11-22

Family

ID=12116565

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2365693U Pending JPH0681699U (en) 1993-05-10 1993-05-10 Oxygen supply device for deep aeration tank

Country Status (1)

Country Link
JP (1) JPH0681699U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11319882A (en) * 1998-05-11 1999-11-24 Oppenheimer Technology Japan:Kk Treatment of oil-containing waste water and treating device
KR20040042081A (en) * 2002-11-13 2004-05-20 주식회사한국연수 Sewage and wastewater treatment process and facilities
JP2006102682A (en) * 2004-10-07 2006-04-20 Veritas Corp Forced-circulation of water of lakes and marshes type light shield method, and apparatus therefor
JP2010535627A (en) * 2007-08-15 2010-11-25 ユナイテッド・ユーティリティーズ・ピーエルシー Method and apparatus for aeration

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11319882A (en) * 1998-05-11 1999-11-24 Oppenheimer Technology Japan:Kk Treatment of oil-containing waste water and treating device
KR20040042081A (en) * 2002-11-13 2004-05-20 주식회사한국연수 Sewage and wastewater treatment process and facilities
JP2006102682A (en) * 2004-10-07 2006-04-20 Veritas Corp Forced-circulation of water of lakes and marshes type light shield method, and apparatus therefor
JP4546211B2 (en) * 2004-10-07 2010-09-15 株式会社ベリタス Method and apparatus for controlling algae in lakes and marshes
JP2010535627A (en) * 2007-08-15 2010-11-25 ユナイテッド・ユーティリティーズ・ピーエルシー Method and apparatus for aeration

Similar Documents

Publication Publication Date Title
JP6072254B2 (en) Water treatment equipment
US20110096618A1 (en) Method and apparatus for aeration
JPS6012636Y2 (en) Reactor device for treating liquids consisting of biologically degradable waste products
KR100762885B1 (en) High speed aerator of slim type having multiple mixing stages
JP2008119609A (en) Gas diffusion system and gas diffusion method
JPH0681699U (en) Oxygen supply device for deep aeration tank
KR100882818B1 (en) An aeration apparatus
US10683221B2 (en) Gas injection and recycling apparatus and methods
JP3150530B2 (en) Biological nitrogen removal equipment
KR20180126209A (en) Areation tank capable of effective aeration for optimal operation
GB2072027A (en) Transfer of oxygen into waste water
JP4313934B2 (en) Underwater stirring type diffuser
KR200355479Y1 (en) Depth Layer Sequential Bath Reacting Waste Water Disposal System
KR101767402B1 (en) Oxygen supplying system for water body
KR200221815Y1 (en) Fluidized bed system for sewage treatment
JP6604676B1 (en) Waterway device
JP6280273B1 (en) Sewage purification equipment
JP4651201B2 (en) Air diffuser and air diffuser
JP4002459B2 (en) Sewage treatment reactor
JP3209874B2 (en) Aeration device
JPS6246477Y2 (en)
JP3545671B2 (en) Sewage treatment equipment
JPS60118292A (en) Waste water treating apparatus
JP3005939B2 (en) Garbage extinction device by fluid system
JPH039835Y2 (en)