JPS60206492A - Aeration tank - Google Patents
Aeration tankInfo
- Publication number
- JPS60206492A JPS60206492A JP59063788A JP6378884A JPS60206492A JP S60206492 A JPS60206492 A JP S60206492A JP 59063788 A JP59063788 A JP 59063788A JP 6378884 A JP6378884 A JP 6378884A JP S60206492 A JPS60206492 A JP S60206492A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- aerator
- water
- sludge
- suction port
- 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
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】 (発明の対象、産業上の利用分野) 本発明は曝気槽に関するものである。[Detailed description of the invention] (Subject of invention, field of industrial application) The present invention relates to an aeration tank.
本発明は活性汚泥処理の分野に使用される。The invention is used in the field of activated sludge treatment.
(従来技術とその問題点)
従来の曝気槽のエアレーション装置には、大別して第5
図に示すブロア式(気泡式)と第6図に示すフロート型
の表面撹拌式とがある。これらの方式にはそれぞれ恣の
ような問題点があった。(Prior art and its problems) Conventional aeration equipment for aeration tanks can be roughly divided into five types.
There is a blower type (bubble type) shown in the figure and a float type surface stirring type shown in FIG. Each of these methods had its own problems.
ブロア式曝気槽に於いては、
(&)ニアコンプレッサ等を設置する機械室が必要な為
、設置スペースが大きくなる。Blower-type aeration tanks require a machine room to install near compressors, etc., so the installation space is large.
(b)曝気槽の水深が深いと、水圧によって散気管21
に設けである小孔が目づまりを起こさないようにニアコ
ンプレッサに大動力が必要である。(b) If the water depth of the aeration tank is deep, water pressure will cause the aeration pipe 21 to
A large amount of power is required for the near compressor to prevent the small holes provided in the compressor from clogging.
(c)表面撹拌式に比較して酸素供給効率が比較的小さ
い。(c) Oxygen supply efficiency is relatively low compared to the surface stirring type.
(d)酸素供給効率を上げるためには気泡を小さくする
等の方法があるが、気泡微細化のための新たな装置が必
要となり、また散気管21の目づまりを起こすなどの欠
点もある
(e)一般的なブロア量では、槽内は一応循環はするが
汚泥が槽底に堆積・しやすい。(d) In order to increase the oxygen supply efficiency, there are methods such as making the bubbles smaller, but this requires a new device to make the bubbles finer and also has drawbacks such as clogging of the air diffuser pipe 21 (e ) With a typical blower volume, there is some circulation in the tank, but sludge tends to accumulate on the bottom of the tank.
なお20はエアパイプ、21は散気装置、0は処理汚水
、Dは汚泥堆積、100は槽である。Note that 20 is an air pipe, 21 is an aeration device, 0 is treated sewage, D is a sludge deposit, and 100 is a tank.
表面撹拌式曝気槽に於いては、
(a)酸素供給量のコントロールは、タイマーによる間
欠運転が一般的であるが、この方法の場合は溶存酸素量
の制御とその自動化はむずかしい。In a surface stirring aeration tank, (a) The amount of oxygen supplied is generally controlled by intermittent operation using a timer, but with this method, it is difficult to control the amount of dissolved oxygen and to automate it.
(b)間欠運転の際の運転休止中に汚泥が沈降するため
、再び運転を始めたときの撹拌効率が悪い。(b) Since the sludge settles during the suspension of operation during intermittent operation, the stirring efficiency is poor when the operation is restarted.
(c)表面撹拌式という構造上、槽底に撹拌されにくい
部分(デッドスペース)がある為に汚泥が堆積しやすい
。(c) Due to the structure of the surface stirring type, there is a part (dead space) at the bottom of the tank that is difficult to stir, so sludge tends to accumulate.
(d)デッドスペースを小さくするために、槽の形状や
水面の広さと深さとの割合などが制限される。(d) In order to reduce the dead space, the shape of the tank and the ratio between the width and depth of the water surface are restricted.
(e)外気から酸素が供給される方式である為、特に寒
冷地では水温が下がりすぎて浄化微生物の活動温域から
はずれ、汚水処理能力が著しく低下する。(e) Since oxygen is supplied from the outside air, especially in cold regions, the water temperature drops too much and deviates from the activity temperature range of purifying microorganisms, resulting in a significant drop in sewage treatment capacity.
(f)一般的にエアレータは槽の中央に設置するため、
補修作業性が良いとは云えず、クレーン等を併設しなけ
ればならない場合もある。(f) Since the aerator is generally installed in the center of the tank,
Repair workability cannot be said to be good, and there are cases where it is necessary to install a crane, etc.
(g)フロート式エアレータあ場合、吸込み口が槽底に
近すぎると槽底に吸い付き、エアレータ本体が沈み、散
水できなくなる恐れがあるので吸込み口の位置を槽底に
近くに配設するに際してもある程度制限される。(g) When using a float type aerator, if the suction port is too close to the tank bottom, it will stick to the bottom of the tank, causing the aerator body to sink and water spraying to be impossible. is also limited to some extent.
なお、10はフロートタイプエアレータ本体、11はフ
ロート、12はアーム、Mはモータ、0は処理汚水、D
は汚泥堆積、100は槽、15は吸入口である。In addition, 10 is a float type aerator main body, 11 is a float, 12 is an arm, M is a motor, 0 is treated wastewater, D
1 is a sludge deposit, 100 is a tank, and 15 is a suction port.
また酸素供給効率を上げるために、一槽内にブロア装置
と撹拌機を併設した併用型エアレータも考案されている
が、
(a)撹拌動力とブロア動力の二つの動力が必要 ρな
ため動力費が増大する。In addition, in order to increase the oxygen supply efficiency, a combination type aerator that has a blower device and a stirrer in one tank has been devised, but (a) Two power sources, stirring power and blower power, are required. increases.
(b)広い設置スペースが必要である。(b) A large installation space is required.
(c)水中では撹拌機の回転部分の機械寿命が短く、補
修作業性もよくない。(c) The mechanical life of the rotating part of the stirrer is short in water, and repair workability is also poor.
等の欠点があり、実施率はそれ程高くない。Due to these drawbacks, the implementation rate is not very high.
(本発明の目的)
本発明の目的は、
(a)溶存酸素の制御が連続運転をしながらできるよう
にすること、
(b)汚水を槽底か・も吸い上げて循環効率を良くして
汚泥堆積を防止すること、
(c)撹拌効率を上げて汚泥の堆積を防止すること、
を可能にした曝気槽を提供することである。(Objectives of the present invention) The objects of the present invention are: (a) To enable dissolved oxygen to be controlled during continuous operation; (b) To improve circulation efficiency by sucking up sewage from the bottom of the tank and turning it into sludge. An object of the present invention is to provide an aeration tank that is capable of: (c) preventing sludge accumulation by increasing stirring efficiency;
(発明の構成)
上記目的を達成するために講じた本発明の技術的手段は
次の通りである。(Structure of the Invention) The technical means of the present invention taken to achieve the above object are as follows.
第1の発明については、
吸い込み口を槽底に接して配設するか、あるいは槽底に
近接して設けるとともに散水量を調節する調節装置を備
えたエアレータを有しており、エアレータは槽に固定さ
れていること、
第2の発明については、
吸い込み口を槽底に接して配設するか、あるいは槽底に
近接して設けるとともに散水量を調節する調節装置を備
えたエアレータを有しており、エアレータは槽に固定さ
れ、エアレータの散水口から散水可能な範囲内に水車ま
たはタービンを設け、水車またはタービンは曝気槽底を
撹拌する撹拌部材と伝達手段を介して接続されているこ
と、 である。Regarding the first invention, the aerator is provided with a suction port in contact with or close to the tank bottom and is equipped with an adjustment device for adjusting the amount of water sprayed, and the aerator is installed in the tank. The second invention has an aerator with a suction port disposed in contact with the tank bottom or close to the tank bottom and an adjustment device for adjusting the amount of water sprinkled. The aerator is fixed to the tank, and a water wheel or turbine is provided within a range where water can be sprayed from the water sprinkling port of the aerator, and the water wheel or turbine is connected via a transmission means to a stirring member that stirs the bottom of the aeration tank; It is.
(実施例)
本発明を、図面に示した実施例に基づき更に詳細に説明
する。(Example) The present invention will be explained in more detail based on the example shown in the drawings.
第1図−1は、第1の発明の実施例を示す説明図である
。FIG. 1-1 is an explanatory diagram showing an embodiment of the first invention.
1はエアレターで、曝気槽に固定してあり汚泥を吸い込
むさいに槽底に吸い着かないようにしている。エアレー
タ1の吸い込み口5は槽底に近接して配設し、槽底10
1の汚泥を吸い上げるようにしている。吸い込み口5は
i1図−2に示すように槽底101に接して設けること
もできるがこの場合は 、吸い込み口5は横方向に設け
て槽底101に吸い込み口5が接しないようにしている
。1 is an air letter, which is fixed to the aeration tank and prevents the sludge from sticking to the bottom of the tank when it is sucked in. The suction port 5 of the aerator 1 is arranged close to the tank bottom, and
I am trying to suck up the sludge from 1. The suction port 5 can be provided in contact with the tank bottom 101 as shown in Figure I1-2, but in this case, the suction port 5 is provided in the horizontal direction so that the suction port 5 does not contact the tank bottom 101. .
エアレータ1の排出口には散水量を調節するバルブ2を
備えている。なお排出口にはノズル4を形成して遠くの
方へ汚泥が散水できるようにしている。The outlet of the aerator 1 is equipped with a valve 2 for adjusting the amount of water sprayed. A nozzle 4 is formed at the discharge port so that the sludge can be sprayed far away.
エアレータ1の上部にはモータMが設けてあり、モータ
M はエアレータ1の内部に設けられているイン1vラ
ー3と連結されている。A motor M is provided at the top of the aerator 1, and the motor M is connected to an inlet roller 3 provided inside the aerator 1.
したがってエアレータl体1の上部に設けられたlモー
タMにより回転するインペラー3で、処理汚水Oを槽底
に近設された吸い込み口5から吸い上げ、ノズル4を通
して槽の液面に向けて散水する。散水量の調整はバルブ
2の開閉で容易にできる0寥也・七−fMのロ軟板庖袈
Σシ;乙にようでLz”6L本実施例は酸素供給効率が
高く、同一処理能力では必要動力もフロートタイプエア
レータとほぼ同じである。Therefore, an impeller 3 rotated by a motor M installed at the top of the aerator body 1 sucks up treated wastewater O from a suction port 5 located near the bottom of the tank, and sprays water through a nozzle 4 toward the liquid surface of the tank. . The amount of water sprinkled can be easily adjusted by opening and closing the valve 2. The required power is also almost the same as a float type aerator.
エアレータ1はフロートタイプとは違い槽壁に固定して
おり、吸い込み口5を槽底に近く設けても、吸い付けら
れて散水部が沈むようなことはない。Unlike the float type, the aerator 1 is fixed to the tank wall, and even if the suction port 5 is provided close to the bottom of the tank, the water spraying part will not sink due to suction.
エアレータ1の設置場所は実施例のように槽内でも良い
し、吸い込み口5さえ槽内に設置すればエアレータ1は
槽外部に設けても支障はない。これにより条件に合わせ
た選択ができ、補修作業性等も良くなり、増設用として
も適している。The aerator 1 may be installed inside the tank as in the embodiment, or the aerator 1 may be installed outside the tank without any problem as long as the suction port 5 is installed inside the tank. This allows selection according to conditions, improves repair workability, and is suitable for expansion.
更にエアレータ1への蒸気配管等により水温の管理調整
ができるようにしても良い。Furthermore, the water temperature may be controlled and adjusted by steam piping to the aerator 1.
第3図、第4図はノズル部の他の実施例を示す断面図で
、ノズル4の排出口には回動自在のカイト弁9が設けで
ある。3 and 4 are cross-sectional views showing other embodiments of the nozzle section, in which a rotatable kite valve 9 is provided at the discharge port of the nozzle 4.
そこで酸素供給量を減らすときは、第3図のより
うにガイド弁9を下方に向は水流が下へ向くように調整
して空気との接触時間を短くする。Therefore, when reducing the amount of oxygen supplied, the guide valve 9 is adjusted downward so that the water flow is directed downward, as shown in FIG. 3, to shorten the contact time with air.
酸素供給量を増やすときには第4図に示すようにガイド
弁9を上方に向け、水流と空気との接触時間を長くする
。When increasing the amount of oxygen supplied, the guide valve 9 is directed upward as shown in FIG. 4 to lengthen the contact time between the water flow and the air.
この実施例によれば、水流と空気との接触時間をある一
定の範囲内で無段階に調整できる。According to this embodiment, the contact time between the water flow and the air can be adjusted steplessly within a certain range.
第2図は、第二の発明の実施例を示す説明図である。FIG. 2 is an explanatory diagram showing an embodiment of the second invention.
本発明では、第一の発明に、更にエアレータ1の散水口
から散水可能な範囲内に水車またはタービン6を設け、
水車またはタービン6は曝気槽底を撹拌する撹拌機7と
伝達ベルト8を介して接続されている。In the present invention, in addition to the first invention, a water wheel or turbine 6 is further provided within a range where water can be sprayed from the water sprinkling port of the aerator 1,
The water wheel or turbine 6 is connected via a transmission belt 8 to an agitator 7 that stirs the bottom of the aeration tank.
そうしてノズル4からの散水によって、水車またはター
ビン6を回し、それを動力源として伝達ベルト8により
回転される撹拌機7作動させる。Then, the water sprinkling from the nozzle 4 turns a water wheel or turbine 6, which is used as a power source to operate the agitator 7 which is rotated by a transmission belt 8.
即ち、撹拌機7により槽底部101を撹拌するので、汚
泥の堆積を防ぎ、気泡の滞留率を上げることにもなるの
で酸素供給効率も高くなる。That is, since the tank bottom 101 is stirred by the stirrer 7, the accumulation of sludge is prevented and the retention rate of bubbles is increased, so that the oxygen supply efficiency is also increased.
本実施例における撹拌装置は、撹拌のための新たな動力
は必要でなく、また構造も簡単なので、第一の発明の曝
気槽の酸素供給効率を高めるための装置として、非常に
有用である。The stirring device in this example does not require any new power for stirring and has a simple structure, so it is very useful as a device for increasing the oxygen supply efficiency of the aeration tank of the first invention.
(発明の効果)
本発明は上記構成により曝気槽の循環効率を高めており
循環水量の調整も容易なので、次のような効果が生じる
。(Effects of the Invention) The present invention improves the circulation efficiency of the aeration tank with the above configuration, and the amount of circulating water can be easily adjusted, so that the following effects are produced.
(a)溶存酸素の制御が連続運転をしながらできるので
、間欠運転の必要がない。(a) Dissolved oxygen can be controlled during continuous operation, so there is no need for intermittent operation.
(b)汚水を槽底から吸い上げるため循環効率が良く、
デッドスペースが小さくなるので汚泥堆積が防止できる
。(b) Good circulation efficiency as wastewater is sucked up from the bottom of the tank.
Since the dead space is reduced, sludge accumulation can be prevented.
(C)排水水処理設備の過負荷が問題となっている現在
、設備拡張は急務であるが、その一方、特に大都市では
用地難や地価の高騰などて装置の立体化を指向せざるを
得ない。(C) Currently, overloading of wastewater treatment equipment is a problem, and there is an urgent need to expand the equipment.However, on the other hand, especially in large cities, due to land shortages and rising land prices, there is no choice but to aim for three-dimensional equipment. I don't get it.
そのため、設置スペースをそれ程必要とせず補修等の作
業性が良く、増設にも適した本発明はこの問題を解決で
きるものである。Therefore, the present invention, which does not require much installation space, has good workability for repairs, etc., and is suitable for expansion can solve this problem.
図面は本発明の実施例を示し、第1図−1は、第1の発
明の詳細な説明図、第1図−2は吸い込み口を槽底に接
して設けた状態を示す説明図、第2図は第2の発明の実
施例を示す説明図、第3図、第4図はノズル部の鳩面説
明図、第5図にはブロア式曝気槽の、第6図は表面撹拌
式(フロートタイプ)曝気槽の説明図である。
l:エアレータ 5:吸い込み口
特許出願人 北 島 晧 胤
代理人弁理士 梶原克彦The drawings show embodiments of the present invention, and FIG. 1-1 is a detailed explanatory diagram of the first invention, FIG. 1-2 is an explanatory diagram showing a state where the suction port is provided in contact with the bottom of the tank, and FIG. Fig. 2 is an explanatory diagram showing an embodiment of the second invention, Figs. 3 and 4 are explanatory diagrams of the dovetail surface of the nozzle section, Fig. 5 is an explanatory diagram of a blower type aeration tank, and Fig. 6 is a surface agitation type ( It is an explanatory view of a float type aeration tank. l: Aerator 5: Suction port Patent applicant: Akira Kitajima Patent attorney representing Tanane: Katsuhiko Kajiwara
Claims (1)
槽底に近接して設けるとともに散水量を調節する調節装
置を備えたエアレータ1を有しており、エアレータlは
槽に固定されていることを特徴とする曝気槽。 2・吸い込み口5を槽底に接して配設するか、あるいは
槽底に近接して設けるとともに散水量を調節する調節装
置を備えたエアレータ1を有しており、エアレータlは
槽に固定され、エアレータ1の散水口から散水可能な範
囲内に水車またはタービンを設け、水車またはタービン
は曝気槽底を撹拌する撹拌部材と伝達手段を介して接続
されている曝気槽。[Claims] 1. It has an aerator 1 with a suction port 5 disposed in contact with the tank bottom or in close proximity to the tank bottom, and equipped with an adjustment device for adjusting the amount of water sprayed. An aeration tank characterized in that l is fixed to the tank. 2. It has an aerator 1 with a suction port 5 disposed in contact with or close to the tank bottom and an adjustment device for adjusting the amount of water sprayed, and the aerator 1 is fixed to the tank. , an aeration tank in which a water wheel or turbine is provided within a range where water can be sprayed from the water sprinkling port of the aerator 1, and the water wheel or turbine is connected via a transmission means to a stirring member that stirs the bottom of the aeration tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59063788A JPS60206492A (en) | 1984-03-30 | 1984-03-30 | Aeration tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59063788A JPS60206492A (en) | 1984-03-30 | 1984-03-30 | Aeration tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60206492A true JPS60206492A (en) | 1985-10-18 |
| JPH0437758B2 JPH0437758B2 (en) | 1992-06-22 |
Family
ID=13239460
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59063788A Granted JPS60206492A (en) | 1984-03-30 | 1984-03-30 | Aeration tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60206492A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63171699A (en) * | 1987-01-07 | 1988-07-15 | Shin Meiwa Ind Co Ltd | Aeration system for pond or the like |
| JPH0217300U (en) * | 1988-07-11 | 1990-02-05 |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4418377Y1 (en) * | 1965-07-24 | 1969-08-07 | ||
| JPS49128537A (en) * | 1973-04-12 | 1974-12-09 | ||
| JPS5636998A (en) * | 1979-09-03 | 1981-04-10 | Hitachi Ltd | Clothing drier |
-
1984
- 1984-03-30 JP JP59063788A patent/JPS60206492A/en active Granted
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4418377Y1 (en) * | 1965-07-24 | 1969-08-07 | ||
| JPS49128537A (en) * | 1973-04-12 | 1974-12-09 | ||
| JPS5636998A (en) * | 1979-09-03 | 1981-04-10 | Hitachi Ltd | Clothing drier |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63171699A (en) * | 1987-01-07 | 1988-07-15 | Shin Meiwa Ind Co Ltd | Aeration system for pond or the like |
| JPH0217300U (en) * | 1988-07-11 | 1990-02-05 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0437758B2 (en) | 1992-06-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4733972A (en) | Floating mixer apparatus with foam dispersing spray | |
| JPS60206492A (en) | Aeration tank | |
| CN206843182U (en) | Anaerobic reactor | |
| CN210065328U (en) | A jet aerator and a sewage treatment tank composed thereof | |
| JPS60114397A (en) | Water treating device | |
| JPS6136475B2 (en) | ||
| CN223430164U (en) | Stirring device and desulfurization equipment | |
| KR200470651Y1 (en) | advanced forming plate | |
| CN218741628U (en) | Pulse type stirring device and sewage treatment system | |
| KR100459671B1 (en) | A mixing-aerator integrated with pump and the controlling me thod there of | |
| CN206970295U (en) | A kind of drop aeration | |
| JPH0642796Y2 (en) | Submersible mechanical aerator | |
| JP3650856B2 (en) | Deep water treatment equipment | |
| CN105366825A (en) | Suction-type inverted-umbrella-shaped surface aerator | |
| JPS588588A (en) | Aerator | |
| CN2623676Y (en) | Cavitation air flotation device | |
| CN215439832U (en) | Oxygen deficiency pond agitating unit for integration sewage treatment device | |
| CN224078357U (en) | A drainage device for a water collection tank | |
| CN208594104U (en) | A kind of sewage treatment aeration tank high efficient aeration machine | |
| SU1629256A1 (en) | Aeration tank | |
| CN223033186U (en) | Grit waste water flocculation treatment device | |
| JPH04197496A (en) | Fluid mixing method | |
| JP2003236582A (en) | Aeration device | |
| JP2002113488A (en) | Method and apparatus for treating liquid | |
| KR100463704B1 (en) | Bubble romoval device and its method of underwater type in a wastewater disposal plant |