JPS59206096A - Aerating apparatus - Google Patents

Aerating apparatus

Info

Publication number
JPS59206096A
JPS59206096A JP58080903A JP8090383A JPS59206096A JP S59206096 A JPS59206096 A JP S59206096A JP 58080903 A JP58080903 A JP 58080903A JP 8090383 A JP8090383 A JP 8090383A JP S59206096 A JPS59206096 A JP S59206096A
Authority
JP
Japan
Prior art keywords
mixer
liquid
gas
bubbles
supply device
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
JP58080903A
Other languages
Japanese (ja)
Inventor
Isao Takahashi
功 高橋
Michiro Hirose
広瀬 道郎
Hiromichi Okada
岡田 宏道
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP58080903A priority Critical patent/JPS59206096A/en
Publication of JPS59206096A publication Critical patent/JPS59206096A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • B01F23/23231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
    • B01F23/232311Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit the conduits being vertical draft pipes with a lower intake end and an upper exit end
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4314Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles
    • B01F25/43141Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles composed of consecutive sections of helical formed elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/30Driving arrangements; Transmissions; Couplings; Brakes
    • B01F35/32Driving arrangements
    • B01F35/32005Type of drive
    • B01F35/3203Gas driven
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/30Driving arrangements; Transmissions; Couplings; Brakes
    • B01F35/32Driving arrangements
    • B01F35/32005Type of drive
    • B01F35/32015Flow driven

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

PURPOSE:To improve efficiency for treating filthy water by utilizing generated fine bubbles by providing a gas supplier and a liquid supplier both confronting the inlet of a stationary mixer and having an ejection port of gas and an ejection port of liquid respectively opening toward an axial direction of the stationary mixer for generating fine bubbles. CONSTITUTION:In an aerating appatatus, a gas supplier 2 ejects gas and generates bubbles, on one hand, a liquid supplier 3 ejects liquid. Filthy water 5 is sucked into a mixer 1 by the air-lifting effect of the bubbles. The filthy water 5 and the liquid ejected from the liquid supplier 3 rise upward through the inside of the mixer 1 while repeating collision with each other. During this stage, the bubbles are broken, therefore, fine bubbles are blown into the filthy water 5 from the outlet (upper end of the mixer). In the stationary mixer 1, plural numbers of twisted blades are arranged in a tubular passage 6 of fluid having an inlet and outlet of the fluid wherein the edges of the twisted blades cross with each other at a desired angle.

Description

【発明の詳細な説明】 本発明は曝気装置に関し、さらに詳しくは、汚水を処理
する際に使用する曝気装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an aeration device, and more particularly to an aeration device used in treating sewage.

たとえば、活性汚泥水処理装防や接触酸化水処理装置な
ど、主として好気性微生物を利用して汚水を処理する装
置においては、処理効率を向上させるために、汚水中に
曝気装置を浸漬して空気を吹き込み、汚水に酸素を溶解
して微生物の繁殖を促進するとともに、汚水を流動させ
て微生物との効率的な接触を促すようにしている。
For example, in equipment that mainly uses aerobic microorganisms to treat wastewater, such as activated sludge water treatment equipment and contact oxidation water treatment equipment, in order to improve treatment efficiency, an aeration device is immersed in the wastewater to generate air. is blown into the wastewater to dissolve oxygen and promote the growth of microorganisms, while also making the wastewater flow and promoting efficient contact with microorganisms.

そのような場合に使用する曝気装置どしては、従来、多
数の微細な吐出孔を穿設してなる散気管や、」ニ記散気
管はどではないがやはりかなり細い吐出孔を穿設した散
気管と、この散気管の子方を被うように設けた、多数の
微細な散気孔を有する散気板とからなるようなものが知
られている。ずなわら、これら従来の装置は、吐出孔ま
たは散気孔の孔径を極力小さくすることによって汚水中
に微細な気泡を発生させ、これにより酸素溶解効率を高
め、もって処理効率を向」−ゼんとするものである。し
かしながら、かかる従来の曝気装置は、微細な吐出孔や
散気孔を有する構造を採っているので、汚水中の汚濁物
質や空気中のダストによってそれらの孔が閉塞されやす
いという欠点があった。この、いわゆる目詰りの問題は
、孔径を大きくすれば解決できようが、そうするとこん
どは気泡径が大きくなって酸素の溶解効率が低下し、高
い処理効率が1nられなくなってしまう。
Conventionally, the aeration equipment used in such cases is a diffuser pipe with many fine discharge holes, or a diffuser pipe with quite thin discharge holes. There is a known type of air diffuser which consists of a diffuser tube and a diffuser plate having a large number of fine diffuser holes, which is provided so as to cover the lower side of the diffuser tube. However, these conventional devices generate fine bubbles in wastewater by minimizing the pore diameter of the discharge hole or aeration hole, thereby increasing oxygen dissolution efficiency and thereby improving treatment efficiency. That is. However, since such conventional aeration devices have a structure having fine discharge holes and diffuser holes, there is a drawback that these holes are easily clogged by pollutants in the waste water and dust in the air. This problem of so-called clogging could be solved by increasing the pore diameter, but then the bubble diameter would become larger and the oxygen dissolution efficiency would decrease, making it impossible to achieve high treatment efficiency.

一方、近年、流体の入口および出口を有する流体通路内
に複数個のねじり翼を列状に配置してなる、いわゆる静
止型混合器を用い、その混合器の上記入口に対向して空
気ノズルを設置してなる曝気装置も提案されている。こ
の曝気装置は、混合器内を気泡が移動する際のエアリフ
ト効果を利用してその混合器内に周囲の汚水を吸い込み
、その汚水の衝突エネルギを利用して気泡を破砕し、小
さくするものである。したがって、空気ノズルの孔径は
大きくてよく、上述した目詰りの心配はまずない。また
、圧力損失も少ない。しかしながら、この装置は空気ノ
ズルのみを設けていること、換言すれば、空気のみを吐
出するものであるから、その吐出量がかなり大きくない
と十分なエアリフト効果が得られず、また混合器の寸法
が大きくないとレイノルズ数が小さくなって混合器内の
汚水の流れが層流になってしまい、いずれの場合も気泡
の破砕効果が低くなるという欠点があった。すなわち、
上記従来の装置は、空気吐出量や混合器寸法がある程度
以上である場合にのみ有効であるにすぎないのである。
On the other hand, in recent years, a so-called static mixer is used, in which a plurality of twisted blades are arranged in a row in a fluid passage having a fluid inlet and an outlet, and an air nozzle is installed opposite the inlet of the mixer. An aeration device that is installed has also been proposed. This aeration device uses the air lift effect when air bubbles move inside the mixer to suck surrounding wastewater into the mixer, and uses the collision energy of the wastewater to crush and reduce the size of the air bubbles. be. Therefore, the hole diameter of the air nozzle may be large, and there is almost no fear of clogging as described above. Also, pressure loss is low. However, since this device only has an air nozzle, in other words, only air is discharged, a sufficient air lift effect cannot be obtained unless the discharge amount is quite large, and the size of the mixer If it is not large, the Reynolds number will be small and the flow of sewage in the mixer will become laminar, which has the disadvantage that the bubble crushing effect will be low in either case. That is,
The above-mentioned conventional devices are only effective when the air discharge amount and mixer dimensions are above a certain level.

本発明の目的は、従来の曝気装置の上記欠点を解決し、
空気供給(イ)や混合器の寸法にかかわらず微細な気泡
を発生させることができ、高い汚水処理効率を1ワるこ
とができる曝気装置を提供するにある。
The purpose of the present invention is to solve the above-mentioned drawbacks of conventional aeration equipment,
To provide an aeration device that can generate fine air bubbles regardless of the size of the air supply (a) or the mixer, and can achieve high sewage treatment efficiency.

上記目的を達成するための本発明は、流体の入口および
出口を有する流体通路内に複数個のねじり翼を列状に配
置してなる静止型混合器の前記入口に対向して、前記入
口と出口とを結ぶ軸線方向に間口した吐出口を有する気
体供給器おJ:び液体供給器を並設してなる曝気装置を
特徴とするものである。
To achieve the above object, the present invention provides a static mixer comprising a plurality of torsion blades arranged in a row within a fluid passage having a fluid inlet and an outlet. This is characterized by an aeration device in which a gas supply device and a liquid supply device are arranged side by side, each having a discharge port opening in the axial direction connecting to the outlet.

本発明の詳細な説明するに、第1図(断面図を加味した
概略正面図)は、本発明の一実M態様に係るlσ気装置
を、汚水5を収容した曝気槽4の底部に設置した状態を
示すものである。。
To explain the present invention in detail, FIG. 1 (schematic front view with cross-sectional view) shows an lσ aeration device according to an embodiment M of the present invention installed at the bottom of an aeration tank 4 containing wastewater 5. This indicates the state in which the .

曝気装置は、曝気槽4内に立設した静1L型混合器1と
、その混合器1の下端、つまり流体入口に対向して、′
その入口と、混合器1の上端、つまり流体川口とを結ぶ
軸線方向に開口した吐出口を有する気体供給器2および
液体供給器3どを有している。上記気体供給器2は、空
気などの好気性気体や窒素ガスなどの嫌気性気体の供給
源(図示せず)に接続され、また上記液体供給器3は清
浄水の供給源(図示せず)に接続されている。これはま
た、汚水5の一部を取り出して供給することができるよ
うに、汚水5の循環系に接続されていてもよいし、また
原水などの供給源に接続されていてもよいものである。
The aeration device includes a static 1L type mixer 1 installed vertically in the aeration tank 4, and a lower end of the mixer 1, that is, facing the fluid inlet.
It has a gas supply device 2 and a liquid supply device 3, each having a discharge port opening in the axial direction connecting the inlet and the upper end of the mixer 1, that is, the fluid mouth. The gas supply device 2 is connected to a supply source (not shown) of an aerobic gas such as air or an anaerobic gas such as nitrogen gas, and the liquid supply device 3 is connected to a source of clean water (not shown). It is connected to the. It may also be connected to the circulation system of the waste water 5 or to a source such as raw water so that a portion of the waste water 5 can be extracted and supplied. .

上記曝気装置は、気体供給器2から気体を吐出して気泡
を発生させ、一方液体供給器3から液体を吐出すること
により、気泡と、いわゆるエアリフト効果によって混合
器1内に吸い込まれる汚水5および液体供給器3から吐
出される液体とが衝突を繰り返しながら混合器1内を上
昇し、その間に気泡が破砕され、流体出口から汚水5中
に微細な気泡を吹き込むことができるものである。
The aeration device generates air bubbles by discharging gas from the gas supply device 2, while discharging liquid from the liquid supply device 3, thereby producing air bubbles and sewage 5 and sewage sucked into the mixer 1 by the so-called air lift effect. The liquid discharged from the liquid supply device 3 rises in the mixer 1 while repeatedly colliding with the liquid, during which air bubbles are crushed and fine air bubbles can be blown into the waste water 5 from the fluid outlet.

上記において、静止型混合器は、第2図(概略斜視図)
に示すように、流体の入口および出口を有する管状の流
体通路6内に、複数個のねじり翼7を、その端縁が所望
の角度で互に交差するように列状に配置したようなもの
で、攪拌翼の如き可5− 動部を一切有しないものである。もつとも、本発明にお
いては、第2図に示したものに限らず、たとえば、特公
昭zz−829o号公報、同53−36182号公報や
、米国特許第3,404..8698″、明1ift書
などに記載されているJ:うな他の静止型混合器を使用
してもよいものである。なお、第2図に示した混合器に
おい−C1ねじり翼7は、その端縁が隣接するねじり製
のそれと接触していてもよいし、離れていてもよい。
In the above, the static mixer is shown in Fig. 2 (schematic perspective view).
As shown in FIG. 2, a plurality of twisted wings 7 are arranged in a row in a tubular fluid passage 6 having a fluid inlet and an outlet so that their edges intersect with each other at a desired angle. It does not have any moving parts such as stirring blades. However, the present invention is not limited to what is shown in FIG. 2, but is also applicable to, for example, Japanese Patent Publication No. Shozz-829o, Japanese Patent Publication No. 53-36182, and U.S. Patent No. 3,404. .. 8698'', Mei 1ift, etc. Other static mixers may also be used.In addition, in the mixer shown in FIG. The edge may be in contact with the adjacent twist or may be separate.

気体供給器は、ノズルや、上述した散気管のようなもの
である。しかしながら、散気管を使用する場合、その吐
出孔の孔径は、従来の曝気装置にお【プるそれほど微細
である必要はない。かかる気体供給器は、その吐出口が
混合器の流体入日と同一平面上になるように設置しても
よいし、混合器内になるように設置してもよい。また、
この気体供給器によって発生せしめられる気泡の大部分
が混合器内に導かれる範囲で、混合器外になるように設
置してもJ:いものである。要するに、混合器の流体入
口に対向して設()ておけばよい。なお、6− 気体供給器はただ1個である必要はなく、複数個並設し
てもよいものである。
The gas supply device is a nozzle or a diffuser pipe as described above. However, when using an aeration pipe, the diameter of the discharge hole does not need to be as fine as in conventional aeration equipment. Such a gas supply device may be installed so that its discharge port is on the same plane as the entrance of the fluid into the mixer, or it may be installed so that it is inside the mixer. Also,
As long as most of the bubbles generated by this gas supply device are introduced into the mixer, it is acceptable to install it outside the mixer. In short, it may be installed opposite the fluid inlet of the mixer. Note that the number of gas supply devices does not need to be just one, and a plurality of gas supply devices may be installed in parallel.

液体供給器としては、通常、ノズルが使用される。この
液体供給器の吐出口は、上記気体供給器のそれと同様、
混合器の流体入口と同一平面上にあってもよいし、混合
器の内または外にあってもよい。ただ、混合器外になる
ように設置する場合、吐出された液体の速度が周囲の汚
水によって大きく減速されると気泡の破砕効果が低くな
るので、混合器の流体入口からあまり離れないようにす
るのが好ましい。また、液体供給器の吐出口は、吐出さ
れた液体が気体供給器に邪魔されて運動エネルギを失わ
ないように、気体供給器よりも、混合器の流体入口側に
あるのが好ましい。なお、この液体供給器もまた、上記
気体供給器と同様、複数個設置してもよいものである。
A nozzle is usually used as a liquid supplier. The discharge port of this liquid supply device is similar to that of the above gas supply device,
It may be flush with the fluid inlet of the mixer, within or outside the mixer. However, if it is installed outside the mixer, the bubble crushing effect will be reduced if the speed of the discharged liquid is significantly slowed down by surrounding waste water, so make sure it is not too far away from the fluid inlet of the mixer. is preferable. Further, the discharge port of the liquid supply device is preferably located on the fluid inlet side of the mixer rather than the gas supply device so that the discharged liquid is not obstructed by the gas supply device and loses kinetic energy. Note that a plurality of liquid supply devices may be installed similarly to the gas supply device described above.

液体供給器による液体の吐出速度は、気体供給器によっ
て発生せしめられる気泡の移動速度よりも大きくしてお
く。また、気泡の破砕効果は、ある程度の領域までは液
体の吐出量に比例して太きくなる。しかしながら、吐出
に要する動力エネルギを考慮すると、むやみに大ぎくす
ることは1q策でない。そのため、液体の吐出量は、通
常、気体のそれの1/20〜1倍程度にしておく。好ま
しいのは、1/10〜1倍である。
The liquid discharge speed by the liquid supply device is set higher than the moving speed of bubbles generated by the gas supply device. Furthermore, the effect of crushing bubbles increases in proportion to the amount of liquid discharged up to a certain extent. However, when considering the power energy required for ejection, it is not a good idea to increase the pressure unnecessarily. Therefore, the amount of liquid discharged is usually set to about 1/20 to 1 times that of gas. Preferably, it is 1/10 to 1 times.

上記実施態様においては、静止型混合器を立設している
場合について説明したが、横置配置してもよいし、斜設
してもよいものである。
In the above embodiment, the static mixer is installed vertically, but it may also be installed horizontally or diagonally.

本発明の曝気装置は、気体供給器から吐出せしめる気体
の種類により、いろいろな種類の水処理装置に使用する
ことができる。すなわち、空気を吐出すれば、活性汚泥
水処理装置や接触酸化水処理装置など、主どして好気性
微生物を利用して汚水を処理する装置の曝気装置として
使用することができる。また、窒素ガスなどの嫌気11
1気体を吐出すれば、脱硝などを行う目的の水処理装置
に適用することができる。また、本発明の曝気装置は、
水処理装置に設置して使用するばかりでなく、湖沼や河
川などにそのまま浸漬設置してその水を浄化するのに使
用することができる。
The aeration device of the present invention can be used in various types of water treatment devices depending on the type of gas discharged from the gas supply device. That is, by discharging air, the device can be used as an aeration device for devices that mainly utilize aerobic microorganisms to treat wastewater, such as activated sludge water treatment devices and catalytic oxidation water treatment devices. In addition, anaerobic gas such as nitrogen gas
If one gas is discharged, it can be applied to water treatment equipment for purposes such as denitrification. Furthermore, the aeration device of the present invention includes:
Not only can it be used by installing it in water treatment equipment, but it can also be used to purify water by immersing it in lakes, rivers, etc.

以上説明したように、本発明の曝気装置は、静止型混合
器の流体入口に対向して気体供給器と液体供給器を並設
しているからして、混合器内を移動する気泡は、その移
動の際のエアリフト効果によって周囲から吸い込まれる
汚水と、液体供給器から吐出され、混合器内に強制的に
流される液体との相乗作用によって細く破砕される。そ
のため、気体の溶解効率が大きく向上し、汚水の処理効
率が向上する。しかも、気体供給器によって発生される
気泡の孔径は大きくてよく、従来の曝気装置のような、
微細な気泡を発9−させるための散気管などは必要でな
いから、目詰りの心配もない。また、従来の曝気装置の
ように、気泡の破砕をエアリフト効果によって吸い込ま
れる汚水のみにたよるのではなく、液体供給器から吐出
される液体の作用をあわせ利用するから、気体の吐出量
が少ない場合でも十分に大きな破砕効果を1nることが
でき、溶解効率が向上する。さらに、従来の曝気装置に
おいては、混合器の寸法が小さい場合に混合器内に乱流
を発生させるのが難しく、気泡の破砕−〇− 効果が低下づ−るという欠点があったが、本発明の曝気
装置は、液体供給器を並設していて、混合器内に強制的
に液体を流し、乱流状態を発現することができるからそ
のような心配がない。
As explained above, since the aeration device of the present invention has the gas supply device and the liquid supply device arranged side by side facing the fluid inlet of the static mixer, the air bubbles moving inside the mixer are The waste water sucked in from the surrounding area by the air lift effect during its movement and the liquid discharged from the liquid supply device and forced into the mixer are combined to crush the waste into fine pieces. Therefore, gas dissolution efficiency is greatly improved, and wastewater treatment efficiency is improved. Moreover, the pore size of the bubbles generated by the gas supply device can be large, so that
Since there is no need for an air diffuser to generate fine air bubbles, there is no need to worry about clogging. In addition, unlike conventional aeration equipment, the air bubbles are broken only by the sewage sucked in by the air lift effect, but because the action of the liquid discharged from the liquid supply device is also used, the amount of gas discharged is small. Even in such cases, a sufficiently large crushing effect can be achieved and the dissolution efficiency is improved. Furthermore, in conventional aeration equipment, when the size of the mixer is small, it is difficult to generate turbulent flow inside the mixer, which reduces the effectiveness of breaking bubbles. The aeration device of the invention eliminates such concerns because the liquid supply devices are arranged in parallel, and the liquid can be forced to flow into the mixer to create a turbulent flow state.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本発明の一実施態様に係る曝気装置を曝気槽
内に設置した状態を示す、断面図を加味した概略正面図
、第2図は、本発明において使用する静止型混合器の一
例を示す概略斜視図である。 1:静止型混合器 2:気体供給器 3;液体供給器 /I:1σ気槽 5:汚水 6:流体通路 7:ねじり翼 特〃[出願人  東し株式会ネ1 10− 第1図 第2図
FIG. 1 is a schematic front view including a sectional view showing an aeration device according to an embodiment of the present invention installed in an aeration tank, and FIG. 2 is a schematic front view of a static mixer used in the present invention. It is a schematic perspective view showing an example. 1: Static mixer 2: Gas supply device 3; Liquid supply device/I: 1σ gas tank 5: Sewage 6: Fluid passage 7: Twisted blade special [Applicant Toshi Co., Ltd. 1 10- Figure 1 Figure 2

Claims (1)

【特許請求の範囲】[Claims] 流体の入口および出口を有する流体通路内に複数個のね
じり翼を列状に配置してなる静止型混合器の前記入口に
対向して、前記入口と出口とを結ぶ軸線方向に開口した
吐出口を有する気体供給器および液体供給器を並設して
なる曝気装置。
A discharge port opening in the axial direction connecting the inlet and outlet, facing the inlet of a static mixer comprising a plurality of twisted blades arranged in a row in a fluid passage having a fluid inlet and outlet. An aeration system consisting of a gas supply device and a liquid supply device arranged in parallel.
JP58080903A 1983-05-11 1983-05-11 Aerating apparatus Pending JPS59206096A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58080903A JPS59206096A (en) 1983-05-11 1983-05-11 Aerating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58080903A JPS59206096A (en) 1983-05-11 1983-05-11 Aerating apparatus

Publications (1)

Publication Number Publication Date
JPS59206096A true JPS59206096A (en) 1984-11-21

Family

ID=13731326

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58080903A Pending JPS59206096A (en) 1983-05-11 1983-05-11 Aerating apparatus

Country Status (1)

Country Link
JP (1) JPS59206096A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030029416A (en) * 2001-10-08 2003-04-14 김학수 Air Lift Power Generation Equipment
WO2005039746A1 (en) * 2003-10-29 2005-05-06 Anemos Company Ltd. Air diffusing device
WO2007110972A1 (en) * 2006-03-27 2007-10-04 Yasuhiko Masuda Gas-liquid mixer
KR100808633B1 (en) 2006-11-27 2008-02-29 (주) 그린킹 Rotating aeration aeration oxidizer and organic wastewater treatment device comprising the same
JP2011062614A (en) * 2009-09-15 2011-03-31 Yonezaki:Kk Stirring device having air lift pump
CN103203195A (en) * 2003-10-29 2013-07-17 风神有限公司 Gas diffusion treatment device
JP2015120100A (en) * 2013-12-20 2015-07-02 三菱電機株式会社 Gas-liquid mixer, and bath hot water supply device

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030029416A (en) * 2001-10-08 2003-04-14 김학수 Air Lift Power Generation Equipment
WO2005039746A1 (en) * 2003-10-29 2005-05-06 Anemos Company Ltd. Air diffusing device
US7264231B2 (en) 2003-10-29 2007-09-04 Anemos Company Ltd. Diffused gas aeration apparatus
CN103203195A (en) * 2003-10-29 2013-07-17 风神有限公司 Gas diffusion treatment device
WO2007110972A1 (en) * 2006-03-27 2007-10-04 Yasuhiko Masuda Gas-liquid mixer
KR100808633B1 (en) 2006-11-27 2008-02-29 (주) 그린킹 Rotating aeration aeration oxidizer and organic wastewater treatment device comprising the same
JP2011062614A (en) * 2009-09-15 2011-03-31 Yonezaki:Kk Stirring device having air lift pump
JP2015120100A (en) * 2013-12-20 2015-07-02 三菱電機株式会社 Gas-liquid mixer, and bath hot water supply device

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