JPS586290A - Aeration device - Google Patents
Aeration deviceInfo
- Publication number
- JPS586290A JPS586290A JP56103279A JP10327981A JPS586290A JP S586290 A JPS586290 A JP S586290A JP 56103279 A JP56103279 A JP 56103279A JP 10327981 A JP10327981 A JP 10327981A JP S586290 A JPS586290 A JP S586290A
- Authority
- JP
- Japan
- Prior art keywords
- flow
- aeration tank
- air
- aeration
- liquid
- 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.)
- Granted
Links
- 238000005273 aeration Methods 0.000 title claims abstract description 50
- 239000007788 liquid Substances 0.000 abstract description 23
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 abstract description 6
- 239000001301 oxygen Substances 0.000 abstract description 6
- 230000007423 decrease Effects 0.000 abstract description 5
- 238000009792 diffusion process Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 4
- 239000010865 sewage Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000005276 aerator Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は例えば工場排水処理場や都市下水処理場等の汚
水処理場において汚水を浄化するための曝気装置に関す
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an aeration device for purifying wastewater in a sewage treatment plant such as a factory wastewater treatment plant or a city sewage treatment plant.
従来、汚水を処理するには、液表面攪拌式、散気管式、
散気板式、等の技術が知られているが、最近羽根車付き
エアレータなどの機械式曝気装置を用い、曝気槽内に強
制的に気液循環流を生ぜしめ、以って曝気効率を高める
技術が採用されている。Traditionally, sewage treatment methods include liquid surface agitation type, aeration tube type,
Although techniques such as the aeration plate type are known, recently mechanical aeration devices such as aerators with impellers have been used to forcefully generate a gas-liquid circulation flow within the aeration tank, thereby increasing aeration efficiency. technology is being adopted.
かかる従来技術の一例が第1図に示されており、第1図
において、モータ1−で回転される羽根車2′はケーシ
ング3′の中に収容されており、そして液は矢印Aで示
すように下方から上方又は斜め上方に流れるようになっ
ている。そして空気供給管4−がら空気を吸込んで曝気
作用を行っている。An example of such prior art is shown in FIG. 1, in which an impeller 2' rotated by a motor 1- is housed in a casing 3', and the liquid flows as indicated by arrow A. It is designed to flow from the bottom to the top or diagonally upward. Then, air is sucked in through the air supply pipe 4 to effect aeration.
また第2図に示す従来例はフロート5′によって液面に
浮遊している形式のものであり、モータ6′によって回
転される羽根車7′は液をケーシング9′の中に矢印B
で示すように上方から下方に送り、その間空気を供給管
8から吸込んで曝気作用を行っている。Furthermore, the conventional example shown in FIG. 2 is of a type in which the liquid is suspended on the liquid surface by a float 5', and an impeller 7' rotated by a motor 6' moves the liquid into the casing 9' indicated by the arrow B.
As shown, the air is sent from above to below, and during this time air is sucked in from the supply pipe 8 to effect aeration.
このような従来装置はそれ自体効果的なものであるけれ
ども、曝気槽の隅部の方まで気液混相流を循環させて、
曝気性能を高めるためには、ある程度大きな吐出し流速
が必要となり、しかも吐出し後もできるだけ吐出し流が
減速しないようにしなければならない。なんとなれば、
通常気液混相流は曝気槽壁面に到達することなく水面に
上昇してしまい、槽内の混合攪拌が充分に行なわれない
からである。さらに底部の流速が小さいと、活性汚泥が
沈澱してしまい、曝気性能が低下するという問題があっ
た。Although such conventional devices are effective in themselves, they do not circulate the gas-liquid multiphase flow to the corners of the aeration tank.
In order to improve the aeration performance, a relatively high discharge flow rate is required, and it is also necessary to prevent the discharge flow from decelerating as much as possible even after discharge. If anything,
This is because the gas-liquid multiphase flow usually rises to the water surface without reaching the wall surface of the aeration tank, and mixing and agitation within the tank is not performed sufficiently. Furthermore, if the flow velocity at the bottom was low, activated sludge would settle, causing a problem in that the aeration performance would deteriorate.
したがって本発明の目的は、吐出し後の流速を比較的に
減速せず、以って曝気槽全体に気液循環流を生ぜしめる
ことのできる曝気装置を提供するにある。Therefore, it is an object of the present invention to provide an aeration device that does not relatively slow down the flow velocity after discharge and can thereby generate a gas-liquid circulating flow throughout the aeration tank.
本発明によれば、曝気装置は曝気槽の底部に設置され、
そして気液混相流の吐出し口は実質的に水平方向に開口
している。したがって気液混相流は曝気槽の底部付近を
水平方向に流れ、そして曝気槽の側壁に沿って上昇し、
液面付近を流れてから再び曝気装置に流入するようにな
り、実質的に曝気槽内の全体を混合攪拌するようになっ
ている。According to the invention, the aeration device is installed at the bottom of the aeration tank,
The discharge port for the gas-liquid multiphase flow opens substantially in the horizontal direction. Therefore, the gas-liquid multiphase flow flows horizontally near the bottom of the aeration tank, and then rises along the side wall of the aeration tank,
After flowing near the liquid level, it flows into the aeration device again, and substantially the entire inside of the aeration tank is mixed and stirred.
以下第3図を参照して本発明の詳細な説明する。全体を
Cで示す本発明を実施した曝気装置は、曝気槽の底部9
上に設置されるもので、底部9上に位置する基台11と
、その基台11上に形成されるケーシング7と、そのケ
ーシング7の上方に設置されてモータ1とよりなるもの
である。ケーシング7はその上端に吸込口10を有し、
その中間部分の内側にはモータ1によって回転する斜根
車2が公知の態様で設けられている。モータ1は例えば
水中ギャードモータが用いられ。ケーシング7からサポ
ート6によって支持されている。The present invention will be described in detail below with reference to FIG. The aeration device implementing the present invention, which is designated as C as a whole, is located at the bottom 9 of the aeration tank.
It is installed on the top and consists of a base 11 located on the bottom 9, a casing 7 formed on the base 11, and a motor 1 installed above the casing 7. The casing 7 has a suction port 10 at its upper end,
Inside the intermediate portion, a slant wheel 2 rotated by a motor 1 is provided in a known manner. For example, an underwater geared motor is used as the motor 1. It is supported by a support 6 from the casing 7.
したがってケーシング7は図示の実施例において羽根車
2より上方の部分は上方が拡がっている筒状に形成され
、その軸線すなわち中心部分にモータおよび羽根車を備
えたポンプユニットが設けられている。ケーシング7の
下部に形成されている吐出し流路12は下方に拡がって
いる外板13とその外板13の半径方向内側に設けられ
、やはり下方に拡がっている内板1′4とで形成され、
この内外両板13.14によって、羽根車2から下方に
流れる吐出し流が水平方向を向くようにゆるやかに曲げ
られ、そしてリング状の吐出し口8から水平に半径方向
外方に吐出されるようになっている。Therefore, in the illustrated embodiment, the casing 7 is formed into a cylindrical shape with an upwardly widening portion above the impeller 2, and a pump unit equipped with a motor and an impeller is provided at the axis or central portion of the casing 7. The discharge passage 12 formed in the lower part of the casing 7 is formed by an outer plate 13 extending downward and an inner plate 1'4 provided on the radially inner side of the outer plate 13 and also extending downward. is,
The discharge flow flowing downward from the impeller 2 is gently bent horizontally by the inner and outer plates 13 and 14, and is then discharged horizontally and radially outward from the ring-shaped discharge port 8. It looks like this.
そして本発明の好ましい実施例によれば、曝気槽の底部
9から吐出し口8の下端8′までの距離をaとし、吐出
し口8の高さすなわち垂直方向の幅をbとすれば、比a
/bが3.0以下になるように形成されている。According to a preferred embodiment of the present invention, if the distance from the bottom 9 of the aeration tank to the lower end 8' of the outlet 8 is a, and the height or vertical width of the outlet 8 is b, then ratio a
/b is formed to be 3.0 or less.
他方、ケーシング7の外周にはリング状の給気管4が設
けられ、この給気管4には給気口5が形成され、図示し
ないパイプを介して外部の酸素又は空気等の供給源に接
続されている。給気管4から吐出し流路12の中に複数
の散気管3が延びており、この散気管3はリング状の給
気管4のステイを構成している。そして散気管3は叶出
し流路12の所で酸素又は空気等を散気するために、複
数の開口3aを有している。図中15は動力用の水中ケ
ーブルであり、16は各種の保護装置用の水中ケーブル
であり、また17は曝気装@Cを吊りおろすためのチェ
ーンである。作動に際して、モータ1を回転させると、
モータ軸1aの端部に取付けられて羽根車2は回転し、
曝気槽内の処理液は矢印りで示すように吸込口10から
吸込まれ、曝気槽の底部9の付近で吐出し口8から水平
方向に吐出される。On the other hand, a ring-shaped air supply pipe 4 is provided on the outer periphery of the casing 7, and an air supply port 5 is formed in this air supply pipe 4, and is connected to an external supply source such as oxygen or air via a pipe (not shown). ing. A plurality of air diffusers 3 extend from the air supply pipe 4 into the discharge flow path 12, and these air diffusers 3 constitute a stay of the ring-shaped air supply pipe 4. The diffuser pipe 3 has a plurality of openings 3a in order to diffuse oxygen, air, etc. at the exposed flow path 12. In the figure, 15 is an underwater cable for power, 16 is an underwater cable for various protection devices, and 17 is a chain for suspending the aeration system @C. During operation, when the motor 1 is rotated,
The impeller 2 is attached to the end of the motor shaft 1a and rotates,
The processing liquid in the aeration tank is sucked in from the suction port 10 as shown by the arrow, and is discharged horizontally from the discharge port 8 near the bottom 9 of the aeration tank.
この際、散気管3の開口3aから酸素又は空気を供給す
るので、処理液は酸素又は空気と混合攪拌され、気液混
相流となる。At this time, since oxygen or air is supplied from the opening 3a of the aeration tube 3, the processing liquid is mixed and stirred with the oxygen or air, resulting in a gas-liquid multiphase flow.
この気液混相流は曝気槽の底部9の付近から水平にすな
わち底部9と平行に流出する。第1図および第2図に示
す従来例では吐出し流はその上下両側の静止水を同伴流
として動かし流速が急激に低下するが本例では少なくと
も吐出し流の下側の静止水がないか、あるいは少ないた
め、これを同伴流として動かすことによる反作用として
流速が急激に低下することがなく、全体として、流速低
下がすくなくてすむ。This gas-liquid multiphase flow flows out from near the bottom 9 of the aeration tank horizontally, that is, parallel to the bottom 9. In the conventional example shown in Figs. 1 and 2, the discharge flow moves the still water on both sides above and below it as an accompanying flow, and the flow velocity decreases rapidly, but in this example, at least there is no still water on the lower side of the discharge flow. , or because it is small, the flow velocity does not suddenly decrease as a reaction to moving this as an entrained flow, and overall the flow velocity does not need to decrease as much.
第4図は本発明の効果を示す図であって曝気槽Eの底部
付近に設置した曝気装置Cがらの吐出し流は矢印Fで示
すように、まず底部9に沿って半径方向外方に流れ、次
いで側壁18に沿って上方に流れ、液面Sの付近で再び
水平に半径方向内方に流れ、そして曝気装置Cの上方で
下方に流れる。FIG. 4 is a diagram showing the effect of the present invention, in which the discharge flow from the aeration device C installed near the bottom of the aeration tank E first flows outward in the radial direction along the bottom 9, as shown by the arrow F. The flow then flows upwardly along the side wall 18, horizontally radially inwardly again near the liquid level S, and downwardly above the aerator C.
したがって本発明によれば吐出される気液混相流はl気
槽E全体の隅々まで流れるので、曝気性能が向上する。Therefore, according to the present invention, the discharged gas-liquid multiphase flow flows to every corner of the entire l-air tank E, so that the aeration performance is improved.
さらに底部9の流速が大きく保てるので、活性汚泥の沈
澱がなく、さらに効率が向上する。Furthermore, since the flow velocity at the bottom 9 can be kept high, there is no sedimentation of activated sludge, further improving efficiency.
本発明の実施に際して、曝気槽の底部が一部高くなって
いたり、低くなっている場合があるが、そのときは曝気
槽の平面の面積が最大の部分を底部とする。第5図は曝
気槽の底部9の一部9aが低くなっている場合を示して
おり、この場合は脚部20を設けてその上に曝気装置C
を設置し、吐出し口8の位置を第3図で説明した通りa
/bが3゜0以下になるようにすればよい。また一部が
高くなっている場合は底部9に設置すればよい。When carrying out the present invention, the bottom of the aeration tank may be partially raised or lowered, and in that case, the portion of the aeration tank with the largest plane area is defined as the bottom. FIG. 5 shows a case where a part 9a of the bottom part 9 of the aeration tank is lowered, and in this case, a leg part 20 is provided and the aeration device C is mounted on the leg part 20.
, and the position of the discharge port 8 is a as explained in Fig. 3.
/b should be 3°0 or less. In addition, if a part is elevated, it may be installed at the bottom 9.
第1図は従来の曝気装置の一例を一部断面で示す側面図
、第2図は従来の曝気装置の他の例を示す概要断面側面
図、第3図は本発明の一実施例を一部断面で示す側面図
、第4図は本発明の効果を示す側面図、第5図は本聚明
を実施した曝気装置を曝気槽に設置する一例を示す側面
図である。
1・・・・・・モータ 2・・・・・・羽根車 3
・・・・・・散気管 4・・・・・・給気管 7・
・・・・・ケーシング 8・・・・・・吐出し口
9・・・・・・底部 10・・・・・・吸込口12・
・・・・・吐出し流路
特許出願人 株式会社荏原製作所
荏原インフィルコ株式会社FIG. 1 is a side view showing a partial cross section of an example of a conventional aeration device, FIG. 2 is a schematic cross-sectional side view showing another example of a conventional aeration device, and FIG. 3 is a side view showing an example of an embodiment of the present invention. FIG. 4 is a side view showing the effects of the present invention, and FIG. 5 is a side view showing an example of installing an aeration device implementing the present invention in an aeration tank. 1... Motor 2... Impeller 3
... Air diffuser pipe 4 ... Air supply pipe 7.
...Casing 8...Discharge port
9... Bottom 10... Suction port 12.
...Discharge channel patent applicant Ebara Corporation Ebara Infilco Corporation
Claims (2)
そのケーシングは上部に吸込口、中間に羽根車を、そし
て下部には吐出し流路を有し、その吐出し流路の吐出し
口は略水平で、かつ半径方向外方に向っており、かつ曝
気槽の底部付近に位置していることを特徴とする曝気装
置。(1) Equipped with a casing installed at the bottom of the aeration tank,
The casing has an inlet in the upper part, an impeller in the middle, and a discharge passage in the lower part, and the outlet of the discharge passage is substantially horizontal and faces radially outward; An aeration device characterized in that the aeration device is located near the bottom of the aeration tank.
、吐出し口の上下方向の幅をbとし、比a/bが3.0
以下である特許請求の範囲第1項記載の曝気装置。(2) The distance between the lower end of the discharge port and the bottom of the aeration tank is a, the vertical width of the discharge port is b, and the ratio a/b is 3.0.
An aeration device according to claim 1, which is as follows.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56103279A JPS586290A (en) | 1981-07-03 | 1981-07-03 | Aeration device |
US06/393,723 US4512936A (en) | 1981-07-03 | 1982-06-30 | Aeration apparatus |
KR8202973A KR850001349B1 (en) | 1981-07-03 | 1982-07-03 | Aerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP56103279A JPS586290A (en) | 1981-07-03 | 1981-07-03 | Aeration device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS586290A true JPS586290A (en) | 1983-01-13 |
JPS6136475B2 JPS6136475B2 (en) | 1986-08-19 |
Family
ID=14349905
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP56103279A Granted JPS586290A (en) | 1981-07-03 | 1981-07-03 | Aeration device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS586290A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60148025U (en) * | 1984-03-10 | 1985-10-01 | 株式会社 関水社 | Solid-containing liquid stirring device for nuclear equipment |
JP2002035784A (en) * | 2000-07-21 | 2002-02-05 | Mitsui Mining Co Ltd | Agitation and aeration apparatus |
JP2002248489A (en) * | 2001-02-26 | 2002-09-03 | Mitsui Miike Mach Co Ltd | Air blowoff device of axial flow stirrer |
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 |
JP2010017655A (en) * | 2008-07-10 | 2010-01-28 | Hitachi Plant Technologies Ltd | Aeration agitator |
JP2010167329A (en) * | 2009-01-20 | 2010-08-05 | Hitachi Plant Technologies Ltd | Aeration agitator |
-
1981
- 1981-07-03 JP JP56103279A patent/JPS586290A/en active Granted
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60148025U (en) * | 1984-03-10 | 1985-10-01 | 株式会社 関水社 | Solid-containing liquid stirring device for nuclear equipment |
JPS6349298Y2 (en) * | 1984-03-10 | 1988-12-19 | ||
JP2002035784A (en) * | 2000-07-21 | 2002-02-05 | Mitsui Mining Co Ltd | Agitation and aeration apparatus |
JP2002248489A (en) * | 2001-02-26 | 2002-09-03 | Mitsui Miike Mach Co Ltd | Air blowoff device of axial flow stirrer |
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 |
JP2010017655A (en) * | 2008-07-10 | 2010-01-28 | Hitachi Plant Technologies Ltd | Aeration agitator |
JP2010167329A (en) * | 2009-01-20 | 2010-08-05 | Hitachi Plant Technologies Ltd | Aeration agitator |
Also Published As
Publication number | Publication date |
---|---|
JPS6136475B2 (en) | 1986-08-19 |
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