JP3336326B2 - Aeration method and device - Google Patents
Aeration method and deviceInfo
- Publication number
- JP3336326B2 JP3336326B2 JP07993695A JP7993695A JP3336326B2 JP 3336326 B2 JP3336326 B2 JP 3336326B2 JP 07993695 A JP07993695 A JP 07993695A JP 7993695 A JP7993695 A JP 7993695A JP 3336326 B2 JP3336326 B2 JP 3336326B2
- Authority
- JP
- Japan
- Prior art keywords
- aeration
- circulating water
- tank
- bubbles
- air
- 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
Links
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)
Description
【0001】[0001]
【産業上の利用分野】本発明は、曝気用の微細気泡を水
面近傍の下向きの循環水流域に噴出させることにより、
槽内全体で均一な曝気を行い、酸素溶解率を向上させる
ようにした曝気方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for spraying fine air bubbles for aeration into a downward circulating water basin near a water surface.
The present invention relates to an aeration method in which uniform aeration is performed in the entire tank to improve the oxygen dissolution rate.
【0002】[0002]
【従来の技術】下水、汚水を好気的に処理する方法とし
て、一般に曝気槽が用いられている。ところで、従来の
曝気槽においては、図3に示すように、曝気槽1の底部
に散気管21を設置し、地上側からブロアー22等にて
高圧空気をダクト23を介して供給し、水中にて散気
し、この放出気泡の浮上力にて槽内に旋回流(循環水
流)を発生させるとともに、気泡による曝気を行うよう
にしていた。2. Description of the Related Art An aeration tank is generally used as a method for aerobically treating sewage and sewage. By the way, in the conventional aeration tank, as shown in FIG. 3, a diffuser tube 21 is installed at the bottom of the aeration tank 1, and high-pressure air is supplied from the ground side by a blower 22 or the like through a duct 23, and is introduced into the water. The buoyancy of the released bubbles generates a swirling flow (circulating water flow) in the tank, and aeration by the bubbles is performed.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、曝気槽
1の底部に設置した散気管21より散気して曝気する方
法においては、散気管21より水中に放出された気泡
が、その浮上力と循環水流の上向流に乗って比較的短時
間に浮上するため、汚水との接触時間が短く、酸素溶解
率が悪いものとなっている。この場合、水中へ放出する
気泡径が小さいほど、酸素溶解率が向上することは周知
である。しかし、曝気量を絞ったり、放出気泡を小径に
すると、供給空気圧が低下して散気装置の散気孔の目詰
まりが生じやすく、また気泡を小径とすると、その浮上
力も弱く、槽内全体に循環水流が起こりにくいなどの不
具合があった。However, in the method of diffusing and aerating from the diffuser tube 21 installed at the bottom of the aeration tank 1, the air bubbles released into the water from the diffuser tube 21 have a floating force and circulation. Since the water floats on the upward flow in a relatively short time, the contact time with the sewage is short, and the oxygen dissolution rate is poor. In this case, it is well known that the smaller the bubble diameter released into water, the higher the oxygen dissolution rate. However, if the aeration amount is reduced or the diameter of the released air bubbles is reduced, the supply air pressure is reduced and clogging of the air diffusion holes of the air diffuser is likely to occur. There were inconveniences such as the difficulty of circulating water flow.
【0004】本発明は、曝気用の微細気泡を水面近傍の
下向きの循環水流域に噴出させることにより、槽内全体
で均一な曝気を行い、酸素溶解率を向上させるようにし
た曝気方法を提供することを目的とする。[0004] The present invention is, by ejecting fine bubbles for aeration in a downward circulating water basin water near performs uniform aeration throughout a tank, provides aeration method to improve the oxygen dissolution rate The purpose is to do.
【0005】[0005]
【課題を解決するための手段】上記目的を達成するた
め、本発明の曝気方法は、曝気槽の底部に配設した粗気
泡発生用散気装置によって、曝気槽内全体に亘って発生
させた循環水流域内にて、水面に対し所定の角度となる
ようにして取り付けたスクリュー式曝気装置によって、
曝気用の微細気泡を水面近傍の下向きの循環水流域に噴
出させて、スクリュー式曝気装置のスクリューによって
発生した水流が粗気泡発生用散気装置によって発生した
循環水流と合流するようにして、微細気泡を下向きの循
環水流に乗せるとともに循環水流中に滞留させることを
特徴とする。In order to achieve the above object, an aeration method according to the present invention uses a rough air provided at the bottom of an aeration tank.
A predetermined angle with respect to the water surface in the circulating water basin generated over the entire aeration tank by the bubble generation diffuser
By screw-type aerator installed as
The fine bubbles for aeration are jetted into the downward circulating water basin near the water surface, and are screwed by the screw of the screw type aerator.
The generated water flow was generated by a diffuser for generating coarse bubbles
The method is characterized in that the microbubbles are placed on the downward circulating water flow so as to merge with the circulating water flow and stay in the circulating water flow .
【0006】[0006]
【作 用】曝気槽内全体に亘って発生させた循環水流域
内にて、曝気用の微細気泡を水面近傍の下向きの循環水
流域に噴出させて、微細気泡を下向きの循環水流に乗せ
るとともに該循環水流中に滞留させることにより、槽内
全体で均一な曝気を行うとともに、微細気泡と水との接
触時間を長く保持でき、酸素溶解率を向上することがで
きる。[Operation] In the circulating water basin generated over the entire aeration tank, fine bubbles for aeration are jetted into a downward circulating water basin near the water surface, and the fine bubbles are put on the downward circulating water flow. By staying in the circulating water flow, uniform aeration can be performed throughout the tank, and the contact time between the fine bubbles and water can be maintained for a long time, and the oxygen dissolution rate can be improved.
【0007】[0007]
【実施例】以下、本発明の曝気方法を図面に示す実施例
に基づいて説明する。まず、図1に参考例を示す。図に
おいて1は所要の容積を有する曝気槽で、図示のように
並列配設されるか、または単独に配設されるとともに、
この曝気槽1の槽内片側壁で、槽底部に旋回流発生用の
散気装置2を設置する。この散気装置2は槽底部に設置
する散気管21と、水面上方に設置したブロアー等の圧
力空気源22と、このブロアーと散気管とを接続するダ
クト23とより構成される。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The aeration method of the present invention will be described below based on an embodiment shown in the drawings. First, a reference example is shown in FIG. In the figure, reference numeral 1 denotes an aeration tank having a required volume, which is arranged in parallel as shown in the figure or independently.
A diffuser 2 for generating a swirling flow is installed on one side wall of the aeration tank 1 at the bottom of the tank. The air diffuser 2 includes an air diffuser 21 installed at the bottom of the tank, a pressure air source 22 such as a blower installed above the water surface, and a duct 23 connecting the blower and the air diffuser.
【0008】この散気管21は水中に放出される気泡に
よる浮力にて槽内全体にわたって旋回流(循環水流)が
生じる位置に設置されるとともに、旋回流が発生するに
十分な空気がブロアーから供給され、散気管21の散気
孔に目詰まりが生じることなく空気が噴出されるように
して散気孔径が定められ、この散気孔径は一般に粗目で
ある。またブロアー22の空気供給量も多量となるよう
な能力と圧力とを有し、ダクト23を経て散気管21へ
供給される。The air diffuser 21 is installed at a position where a swirling flow (circulating water flow) is generated throughout the tank by the buoyancy of bubbles released into the water, and sufficient air is supplied from the blower to generate the swirling flow. The diameter of the diffuser hole is determined so that air is blown out without clogging of the diffuser holes of the diffuser tube 21, and the diffuser hole diameter is generally coarse. Further, the air supply amount of the blower 22 has a capacity and a pressure so as to be large, and is supplied to the air diffuser tube 21 through the duct 23.
【0009】この散気装置2の散気により、槽内全体に
発生する循環水流の水流域、例えば散気管21を有する
側と対向する反対側内壁面に沿い、かつ水面近傍の位置
に微細気泡発生装置3を配設する。この微細気泡発生装
置3にて循環水流中に供給される微細気泡は、この循環
水流に乗って望ましくは水面近傍の水域により槽底部に
まで運ばれ、さらに槽内を循環させ、水との接触時間を
長く保ち、その途中にて空気中の酸素を溶解するように
する。Due to the air diffuser 2, fine air bubbles are generated in the water flow area of the circulating water flow generated in the entire tank, for example, along the inner wall surface opposite to the air diffusion tube 21 side and near the water surface. The generator 3 is provided. The microbubbles supplied into the circulating water stream by the microbubble generator 3 are carried to the bottom of the tank by the water area, preferably near the water surface, riding on the circulating water stream, and further circulated in the tank to make contact with water. Keep the time long and try to dissolve the oxygen in the air along the way.
【0010】したがって、この微細気泡発生装置3にて
水中に噴出される微細気泡は、循環水流の下向流に乗り
やすいようにして、その噴出方向が定められる。Therefore, the direction of the fine bubbles ejected into the water by the fine bubble generating device 3 is determined so that the fine bubbles can easily get on the downward flow of the circulating water flow.
【0011】微細気泡発生装置3としては、図1に示す
ように水面上方に設けたブロアー32に吸気管33を介
して微細気泡散気管31を接続して構成するもの、ある
いは図2に示す本発明の一実施例のように、スクリュー
の回動にてスクリュー先端水域にて発生する負圧にて大
気を自吸し、スクリューの渦流にて破砕されて水中へ噴
出されるスクリュー式曝気装置4等が採用される。The microbubble generator 3 is constructed by connecting a microbubble diffuser 31 via a suction pipe 33 to a blower 32 provided above the water surface as shown in FIG. 1 or a book shown in FIG. As in the embodiment of the invention, the screw type aeration device 4 which self-absorbs the atmosphere by the negative pressure generated in the water area of the screw tip by the rotation of the screw, is crushed by the vortex of the screw, and is jetted into the water. Etc. are adopted.
【0012】ブロアー・散気管式の場合は、散気管31
の散気孔径は曝気に適した微細孔とし、かつ目詰まりが
生じたときこれを清掃あるいは点検不能なように散気管
33の一部に回動可能な継手34を設け、これにより図
1の右方に示す如く、散気管31を水面上方へ移動でき
るようにする。なお、この散気管31により水中へ噴出
される気泡量は汚水に適した曝気が行えるようにしてブ
ロアー31の能力等が定められ、かつ空気供給量は調整
できるものである。In the case of a blower / diffuser tube type,
1 is provided with a rotatable joint 34 at a part of the diffuser pipe 33 so that it cannot be cleaned or inspected when clogging occurs. As shown on the right, the air diffuser 31 can be moved above the water surface. The amount of air bubbles blown out into the water by the air diffuser 31 determines the capacity and the like of the blower 31 so that aeration suitable for sewage can be performed, and the air supply amount can be adjusted.
【0013】また、図2に示すようにスクリュー式曝気
機4の場合は、曝気槽1の上方に架台5を設け、この架
台5にスクリュー式曝気機4を水面に対し所定の角度と
なるようにして取り付けると、スクリュー41の回動に
より発生する水流が散気装置2にて発生する循環水流と
合流するようにし、旋回流速を向上するようにする。In the case of the screw type aerator 4 as shown in FIG. 2, a pedestal 5 is provided above the aeration tank 1, and the screw type aerator 4 is mounted on the pedestal 5 at a predetermined angle with respect to the water surface. When installed, the rotation of the screw 41
The generated water flow merges with the circulating water flow generated in the air diffuser 2 to improve the swirling flow velocity.
【0014】このように構成した曝気装置においては、
散気装置2より槽底水域内に散気すると、その気泡は浮
力にて上昇する。この散気が連続的に行われることによ
り上向流が槽内全体において循環水流となるとともに、
散気が大きな気泡であってもある程度の曝気が行われ
る。そして、循環水流域にあって微細気泡が噴出される
ので、微細気泡は循環水流に乗って槽内全域に拡散さ
れ、気泡の水中内での滞留時間が長くなり、これにより
水との接触時間がまして酸素の溶解率が向上するものと
なる。In the aeration apparatus configured as described above,
When the air diffuser 2 diffuses air into the tank bottom water, the bubbles rise by buoyancy. By performing this aeration continuously, the upward flow becomes a circulating water flow throughout the tank,
Aeration is performed to some extent even if the air bubbles are large. Since fine bubbles are ejected in the circulating water flow area, the fine bubbles are diffused throughout the tank on the circulating water flow, and the residence time of the bubbles in the water becomes longer, thereby increasing the contact time with the water. Thus, the dissolution rate of oxygen is improved.
【0015】[0015]
【発明の効果】本発明によれば、曝気槽内全体に亘って
発生させた循環水流域内にて、曝気用の微細気泡を水面
近傍の下向きの循環水流域に噴出させ、特に、スクリュ
ーの回動により発生する水流が散気装置にて発生する循
環水流と合流するようにし、旋回流速を向上するように
して、微細気泡を下向きの循環水流に乗せるとともに循
環水流中に滞留させることにより、槽内全体で均一な曝
気を行うとともに、微細気泡と水との接触時間を長く保
持でき、酸素溶解率を向上することができる。According to the present invention, at was generated throughout aeration tank circulating water in the basin, is ejected fine bubbles for aeration in a downward circulating water basin water near particular, screw
The water flow generated by the rotation of the
So that it merges with the circulating water flow to improve the swirl velocity
The fine bubbles into the downward circulating water flow and circulate
By staying in the ring water flow , uniform aeration can be performed throughout the tank, the contact time between the fine bubbles and water can be maintained for a long time, and the oxygen dissolution rate can be improved.
【図1】曝気装置の参考例の説明図である。 FIG. 1 is an explanatory diagram of a reference example of an aeration apparatus.
【図2】本発明の曝気方法を実施する曝気装置の一例を
示す説明図である。 FIG. 2 shows an example of an aeration apparatus for implementing the aeration method of the present invention .
FIG.
【図3】従来の曝気装置の説明図である。FIG. 3 is an explanatory diagram of a conventional aeration apparatus.
1 曝気槽 2 散気装置 21 散気管 22 ブロアー 3 微細気泡発生装置 31 散気管 32 ブロアー 4 スクリュー式曝気装置 DESCRIPTION OF SYMBOLS 1 Aeration tank 2 Air diffuser 21 Air diffuser 22 Blower 3 Fine bubble generator 31 Air diffuser 32 Blower 4 Screw type aerator
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−91298(JP,A) (58)調査した分野(Int.Cl.7,DB名) C02F 3/14 - 3/26 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-6-91298 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) C02F 3/14-3/26
Claims (1)
気装置によって、曝気槽内全体に亘って発生させた循環
水流域内にて、水面に対し所定の角度となるようにして
取り付けたスクリュー式曝気装置によって、曝気用の微
細気泡を水面近傍の下向きの循環水流域に噴出させて、
スクリュー式曝気装置のスクリューによって発生した水
流が粗気泡発生用散気装置によって発生した循環水流と
合流するようにして、微細気泡を下向きの循環水流に乗
せるとともに循環水流中に滞留させることを特徴とする
曝気方法。1. A dispersion for generating coarse air bubbles disposed at the bottom of an aeration tank.
In the circulating water basin generated over the entire aeration tank by the aeration device , at a predetermined angle with respect to the water surface
By the attached screw type aeration device, fine bubbles for aeration are jetted into the downward circulating water basin near the water surface,
Water generated by screw of screw type aerator
The circulating water flow generated by the diffuser for generating coarse bubbles
An aeration method characterized in that fine air bubbles are placed in a downward circulating water flow and retained in the circulating water flow so as to be merged .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP07993695A JP3336326B2 (en) | 1995-03-10 | 1995-03-10 | Aeration method and device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP07993695A JP3336326B2 (en) | 1995-03-10 | 1995-03-10 | Aeration method and device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08243582A JPH08243582A (en) | 1996-09-24 |
JP3336326B2 true JP3336326B2 (en) | 2002-10-21 |
Family
ID=13704212
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP07993695A Expired - Fee Related JP3336326B2 (en) | 1995-03-10 | 1995-03-10 | Aeration method and device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3336326B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100437923B1 (en) * | 2001-05-10 | 2004-06-30 | 한상배 | Sequencing Batch Reactor System for treating waste water |
JP5190242B2 (en) * | 2007-10-02 | 2013-04-24 | 株式会社神鋼環境ソリューション | Biological treatment method and biological treatment apparatus |
JP6313945B2 (en) * | 2013-09-30 | 2018-04-18 | 三菱日立パワーシステムズ株式会社 | Air diffuser for seawater desulfurization, seawater desulfurizer equipped with the same, and water quality improvement method |
-
1995
- 1995-03-10 JP JP07993695A patent/JP3336326B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH08243582A (en) | 1996-09-24 |
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