JPH0871583A - Air diffusing stirrer for reaction tank - Google Patents
Air diffusing stirrer for reaction tankInfo
- Publication number
- JPH0871583A JPH0871583A JP6242040A JP24204094A JPH0871583A JP H0871583 A JPH0871583 A JP H0871583A JP 6242040 A JP6242040 A JP 6242040A JP 24204094 A JP24204094 A JP 24204094A JP H0871583 A JPH0871583 A JP H0871583A
- Authority
- JP
- Japan
- Prior art keywords
- air
- reaction tank
- hollow shaft
- diffuser
- rotary hollow
- 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
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)
- Mixers With Rotating Receptacles And Mixers With Vibration Mechanisms (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は反応槽用散気攪拌装置、
特に槽内廃水中への酸素供給効率を向上させる散気構造
の改良に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an agitating device for a reaction tank,
In particular, the present invention relates to improvement of a diffuser structure that improves the efficiency of oxygen supply to wastewater in a tank.
【0002】[0002]
【従来の技術】廃水中の有機物の除去方法として、好気
性微生物によって酸化分解させる活性汚泥法が汎用され
ている。前記活性汚泥法において最も重要なポイントの
一つとして、空気中の酸素を反応槽内の廃水に如何に効
率良く供給するかが挙げられる。これは、微生物による
有機物の酸化、微生物の増殖および自己酸化などの生物
学的反応を促進させるためには、廃水中の溶存酸素量を
増やさなければならず、酸素供給の効率が廃水の処理能
力に大きな影響を与えるからである。2. Description of the Related Art As a method for removing organic substances from wastewater, an activated sludge method in which aerobic microorganisms oxidize and decompose is widely used. One of the most important points in the activated sludge method is how to efficiently supply oxygen in the air to the wastewater in the reaction tank. This is because the amount of dissolved oxygen in wastewater must be increased in order to promote biological reactions such as the oxidation of organic substances by microorganisms, the growth of microorganisms and autooxidation. Because it has a great influence on.
【0003】このため、従来から図5に示すように反応
槽10内の底部に散気装置が設けられている。該散気装
置は、散気管12の一端から吸気管13を介してブロワ
ー14によって吸気し、該散気管12に設けられた散気
孔から気泡を吹出して廃水中に酸素を供給する。ここ
で、前記廃水中への酸素供給量を増やす方法としては、
散気孔からの気泡と廃水との接触面積を増やせばよいた
め、従来から各種形状の散気管が考えられており、例え
ば反応槽10の底部に大型の多孔性散気板や格子状散気
管を広範囲にわたって配置する方法がとられている。For this reason, conventionally, as shown in FIG. 5, an air diffuser is provided at the bottom of the reaction tank 10. The air diffuser sucks air from one end of the air diffuser 12 by the blower 14 through the intake pipe 13, blows bubbles from the air diffuser holes provided in the air diffuser 12, and supplies oxygen to the wastewater. Here, as a method of increasing the oxygen supply amount to the wastewater,
Since it suffices to increase the contact area between the bubbles from the diffuser holes and the waste water, diffuser pipes of various shapes have been conventionally considered. For example, a large porous diffuser plate or a grid-like diffuser pipe is provided at the bottom of the reaction tank 10. The method of arranging over a wide area is taken.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、前述し
た大型の多孔性散気板や格子状散気管はそれ自体が高価
な上、吸気のためのブロワーの出力が大きくなるためコ
スト高となってしまうという問題があった。However, the large-sized porous diffuser plate and the grid-like diffuser tube described above are themselves expensive, and the output of the blower for intake is large, resulting in high cost. There was a problem.
【0005】一方、前記散気孔から吹出した気泡の単位
量当りの酸素供給量を考えた場合、該気泡の廃水中への
滞留時間が長い程、溶解する酸素量が増すこととなる。
しかし、従来の散気装置においては、散気孔から吹出し
た気泡は、図6に示すようにほぼ真上に向って上昇して
いく。即ち、該気泡は同図のH1に示す散気孔から水面
までのほぼ最短距離で上昇し、滞留時間も短くなるた
め、酸素溶解効率は極めて低いものであった。なお、前
記図5に示すように、反応槽10内には、廃水と処理水
とを混合するため、或いは微生物のフロックや担体を廃
水と効率良く接触させるための攪拌装置が設けられてい
ることも多い。該攪拌装置は、反応槽10底部に垂下し
た回転軸16をモータ20で回転させ、該回転軸16下
端部に固定された羽根18の回転によって廃水を攪拌す
るものである。On the other hand, considering the oxygen supply amount per unit amount of bubbles blown out from the diffuser holes, the longer the residence time of the bubbles in the waste water, the more the dissolved oxygen amount increases.
However, in the conventional air diffuser, the bubbles blown out from the air diffuser rise almost upward as shown in FIG. That is, the air bubbles rise in the shortest distance from the diffuser holes shown in H 1 of the figure to the water surface and the residence time becomes short, so that the oxygen dissolution efficiency was extremely low. As shown in FIG. 5, the reaction tank 10 is provided with a stirrer for mixing waste water and treated water, or for efficiently contacting flocs and carriers of microorganisms with waste water. There are also many. The stirrer rotates a rotating shaft 16 hanging down at the bottom of the reaction tank 10 with a motor 20, and stirs waste water by rotating a blade 18 fixed to the lower end of the rotating shaft 16.
【0006】このため、前記廃水の攪拌によって生じる
水流が、散気孔から吹出した気泡の上昇移動に影響を与
えることもあるが、前記散気管12と羽根18とは別々
に設置されておりその影響は一定していないため、羽根
18による廃水攪拌が必ずしも気泡の滞留時間を長くす
るとは限らず、単に散気装置と攪拌装置を同時に作動さ
せるだけでは、廃水中への酸素溶解効率を向上させると
は言えなかった。本発明は前記従来技術の課題に鑑がみ
為されたものであり、その目的は小型の散気装置で、か
つ廃水への酸素供給効率の良い反応槽用散気攪拌装置を
提供することにある。Therefore, although the water flow generated by stirring the waste water may affect the upward movement of the bubbles blown out from the diffuser holes, the diffuser pipe 12 and the blades 18 are installed separately and the influence thereof is exerted. Is not constant, stirring the wastewater by the blades 18 does not always lengthen the retention time of the bubbles, and it is possible to improve the efficiency of dissolving oxygen in the wastewater simply by operating the air diffuser and the stirrer at the same time. I couldn't say. The present invention has been made to solve the above-mentioned problems of the prior art, and an object thereof is to provide a diffuser stirring device for a reaction tank, which is a small-sized diffuser and has a high oxygen supply efficiency to wastewater. is there.
【0007】[0007]
【課題を解決するための手段】前記目的を達成するため
に本発明にかかる反応槽用散気攪拌装置は、反応槽内の
底部へと垂下して設けられた回転中空軸と、前記回転中
空軸の上端口から下端口へと軸内に導気する導気手段
と、前記反応槽底部に配置され、前記回転中空軸により
回転するパドル羽根と、前記パドル羽根に沿って設けら
れ、前記回転中空軸の下端口が連通した通気管と、前記
通気管に設けられ、かつ散気孔を有する散気手段と、を
備えたことを特徴とする。In order to achieve the above object, a diffuser agitator for a reaction tank according to the present invention comprises a rotary hollow shaft that hangs down to the bottom of the reaction tank, and the rotary hollow shaft. Air guiding means for guiding air into the shaft from the upper end to the lower end of the shaft, paddle blades arranged at the bottom of the reaction tank and rotated by the rotary hollow shaft, and provided along the paddle blades, It is characterized by comprising a ventilation pipe having a lower end opening of the hollow shaft communicating with each other, and an air diffusing means provided in the ventilation pipe and having an air diffusing hole.
【0008】[0008]
【作用】本発明にかかる反応槽用散気攪拌装置は、前述
したようにパドル羽根に沿って通気管を設け、該通気管
に散気孔を有する散気手段を設けているため、該パドル
羽根と散気手段は一体的に回転する。ここで、前記回転
によってパドル羽根及び散気手段の表面付近には大きな
せん断力が生じる。従って、パドル羽根及び散気手段の
上方の廃水には、前記回転方向とは反対の斜め上方への
水流が生じるため、散気孔から吹出した気泡も真上には
上昇せず、図4に示すように斜め上方に向って上昇して
いく。In the diffuser agitator for a reaction tank according to the present invention, as described above, the ventilation pipe is provided along the paddle blade, and the ventilation pipe is provided with the diffusion means having the diffusion holes. And the aeration means rotate integrally. Here, a large shearing force is generated near the surface of the paddle blade and the air diffusing means by the rotation. Therefore, in the wastewater above the paddle blades and the air diffusing means, a water flow obliquely upward, which is the opposite of the rotation direction, is generated, so that the bubbles blown out from the air diffusing holes do not rise right above, and are shown in FIG. Ascends diagonally upward.
【0009】即ち、同図から明らかなように気泡の散気
孔から水面までの移動距離H2は、前記図6に示す気泡
が真上に上昇した時の移動距離H1よりも長くなり、そ
れだけ廃水中への滞留時間が長くなるため、酸素溶解効
率が極めて向上する。なお、前記反応槽用散気攪拌装置
により嫌気性処理を行なう場合には、前記回転中空軸上
端口からの空気供給を停止し、散気孔からの散気を行な
わずにパドル羽根による攪拌のみを行なう。That is, as is clear from the figure, the moving distance H 2 of the bubbles from the air diffuser hole to the water surface is longer than the moving distance H 1 when the bubbles as shown in FIG. Since the residence time in the waste water is long, the oxygen dissolution efficiency is extremely improved. In the case of performing anaerobic treatment by the aeration stirring device for the reaction tank, the air supply from the upper end opening of the rotary hollow shaft is stopped, and only the stirring by the paddle blade is performed without performing the air diffusion from the diffusion holes. To do.
【0010】[0010]
【実施例】以下、図面に基づき本発明の好適な実施例を
説明する。図1には、本発明の一実施例にかかる反応槽
用散気攪拌装置の概略構成図が示されており、同図
(A)は上面図、同図(B)は側面図である。同図に示
す散気攪拌装置は、反応槽110の上部開口の中央に上
部壁122が橋渡ししてあり、該上部壁122に軸台1
24が固定されている。そして、該軸台124には、上
部軸受126及び下部軸受128を介して管状の回転中
空軸116が回転可能に支持されつつ、反応槽110内
の底部へと垂下している。また、前記回転中空軸116
の上端側には該回転中空軸116に回転駆動力を加える
ためのモータ120が設置されている。DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows a schematic configuration diagram of a diffuser / agitator for a reaction tank according to an embodiment of the present invention. FIG. 1 (A) is a top view and FIG. 1 (B) is a side view. In the diffuser stirring device shown in the figure, an upper wall 122 is bridged in the center of the upper opening of the reaction tank 110, and the headstock 1 is attached to the upper wall 122.
24 is fixed. A tubular rotary hollow shaft 116 is rotatably supported by the shaft base 124 via an upper bearing 126 and a lower bearing 128, and hangs down to the bottom of the reaction tank 110. In addition, the rotary hollow shaft 116
A motor 120 for applying a rotational driving force to the rotary hollow shaft 116 is installed on the upper end side of the.
【0011】さらに、前記反応槽110内に垂下した回
転中空軸116の上部位置、及び下部位置の2箇所に
は、上部パドル羽根130及び下部パドル羽根132が
設けられている。そして、モータ120を駆動すること
により、回転中空軸116と共にパドル羽根130、1
32を回転させ、反応槽110内の廃水を攪拌する。一
方、前記回転中空軸116の上端口には吸気管134が
接続されており、該吸気管134に設置されたブロワー
114により、吸気管134の吸気口から空気を回転中
空軸116の軸内へ吸気する。また、回転中空軸116
の下端口には一端が連通した通気管136が前記下部パ
ドル羽根132に沿って設けられている。さらに、同図
(B)のA−A'方向から見た図2にも示すように、前
記通気管136には、下部パドル羽根132の先端側位
置において水平方向両側に枝分れした散気手段としての
散気管112が設けられており、該散気管112には散
気孔112aが形成されている。Further, an upper paddle blade 130 and a lower paddle blade 132 are provided at two positions, an upper position and a lower position, of the rotary hollow shaft 116 that hangs in the reaction tank 110. Then, by driving the motor 120, the paddle blades 130, 1
32 is rotated and the waste water in the reaction tank 110 is stirred. On the other hand, an intake pipe 134 is connected to the upper end of the rotary hollow shaft 116, and air is introduced from the intake port of the intake pipe 134 into the shaft of the rotary hollow shaft 116 by a blower 114 installed in the intake pipe 134. Inhale. In addition, the rotary hollow shaft 116
A ventilation pipe 136 having one end communicating with the lower end opening is provided along the lower paddle blade 132. Further, as shown in FIG. 2 when viewed from the AA ′ direction in FIG. 2B, the ventilation pipe 136 has an air diffuser branched horizontally on both sides at the tip end side position of the lower paddle blade 132. An air diffuser 112 as a means is provided, and the air diffuser 112 is formed with an air diffuser hole 112a.
【0012】このため、前記回転中空軸116を回転さ
せると、散気管112は下部パドル羽根132と一体的
に回転しながら、該回転中空軸116の軸内に吸引した
空気を散気孔112aから吹出すこととなり、攪拌と散
気を同時に行なう。ここで、前述したように下部パドル
羽根132及び散気管112の回転時には、その周りに
斜め上方向へのせん断力が生じるため、散気孔112a
から吹出した気泡も前記図4に示すように斜め上方向に
上昇することとなり、水面に到達するまでの滞留時間が
極めて長くなる。Therefore, when the rotary hollow shaft 116 is rotated, the air diffuser 112 rotates integrally with the lower paddle blades 132 while blowing the air sucked into the rotary hollow shaft 116 through the air diffuser holes 112a. It will be discharged, and stirring and aeration will be performed simultaneously. Here, as described above, when the lower paddle blade 132 and the air diffusing tube 112 rotate, a shearing force in an obliquely upward direction is generated around them, so that the air diffusing hole 112a is formed.
The bubbles blown out of the container also rise obliquely upward as shown in FIG. 4, and the residence time before reaching the water surface becomes extremely long.
【0013】このように、本実施例においては、散気孔
112aを有する散気管112を下部パドル羽根132
に密接して設け、該下部パドル羽根132と共に一体的
に回転させながら散気することにより、散気した気泡の
水面までの移動距離を常に長く確保することができ、廃
水中への酸素溶解効率を向上させ、小型の散気装置でも
充分な酸素供給が可能となる。As described above, in this embodiment, the air diffuser 112 having the air diffuser holes 112a is attached to the lower paddle blade 132.
And the lower paddle blades 132 are rotated integrally with the lower paddle blades 132 to diffuse air, so that it is possible to always secure a long moving distance of the diffused bubbles to the water surface, and the efficiency of dissolving oxygen in waste water. Therefore, it is possible to sufficiently supply oxygen even with a small air diffuser.
【0014】なお、前記散気攪拌装置において、嫌気性
処理を行なう場合には、ブロワー114を駆動せず回転
中空軸116内への吸気を停止する。このため、散気管
112からは廃水中へは散気されず、該廃水を嫌気状態
にしながらパドル羽根130、132の回転による攪拌
のみを行なう。また、本実施例においては、前記上部パ
ドル羽根130、及び下部パドル羽根132の直径を反
応槽の内幅に対して1/2〜4/5の大きさに形成し、
その回転数を5〜15rpmとしている。When the anaerobic treatment is performed in the diffuser stirring device, the blower 114 is not driven and the intake of air into the rotary hollow shaft 116 is stopped. Therefore, the waste water is not diffused from the air diffuser 112, and only the stirring is performed by rotating the paddle blades 130 and 132 while keeping the waste water in an anaerobic state. In the present embodiment, the upper paddle blade 130 and the lower paddle blade 132 are formed to have a diameter of 1/2 to 4/5 with respect to the inner width of the reaction tank.
The rotation speed is 5 to 15 rpm.
【0015】これは、従来のパドル羽根と比較して極め
て大型、かつ低回転であり、このようにすることによ
り、微生物のフロックや槽内に浮遊させたスポンジ状多
孔質担体などを破壊することなく廃水全体を良好に攪拌
することができる。また、前記下部パドル羽根132を
大型化することにより、その先端側に設けられた前記散
気管112が広範囲にわたって移動しながら気泡を吹出
すため、廃水への酸素溶解効率をより向上させることが
可能となる。さらに、本実施例においては、前記上部パ
ドル羽根130、及び下部パドル羽根132の形状をね
じれ形状に形成している。即ち、図3に示すようにパド
ル羽根130、132の面の傾き角を水平方向に対し
て、付け根部における45度(同図(A))から先端部
における30度(同図(B))となるように形成してい
る。This is extremely large in size and low in rotation as compared with a conventional paddle blade, and by doing so, it is possible to destroy flocs of microorganisms and sponge-like porous carriers suspended in a tank. It is possible to satisfactorily agitate the entire wastewater. Also, by enlarging the lower paddle blade 132, the air diffuser 112 provided on the tip side thereof blows air bubbles while moving over a wide range, so that it is possible to further improve the oxygen dissolution efficiency in wastewater. Becomes Further, in this embodiment, the upper paddle blade 130 and the lower paddle blade 132 are formed in a twisted shape. That is, as shown in FIG. 3, the angle of inclination of the surfaces of the paddle blades 130 and 132 with respect to the horizontal direction is 45 degrees at the root (FIG. 3A) to 30 degrees at the tip (FIG. 3B). It is formed so that.
【0016】そして、このような形状とすることによ
り、線速度の大きい外周部と線速度の小さい内周部の上
方流速度、パドル羽根各部に付加されるモーメント力の
均一化が図られ攪拌効率が向上すると共に、下部パドル
羽根132の先端側において作用するせん断力の方向
が、前記散気孔112aから吹き出た気泡をより斜め方
向に移動させるように働くため、酸素溶解効率も一層向
上する。With such a shape, the upward flow velocities of the outer peripheral portion having a high linear velocity and the inner peripheral portion having a low linear velocity, and the moment force applied to each portion of the paddle blades are made uniform, whereby the stirring efficiency is improved. In addition, the direction of the shearing force acting on the tip side of the lower paddle blade 132 works so as to move the bubbles blown out from the diffuser holes 112a in a more oblique direction, so that the oxygen dissolution efficiency is further improved.
【0017】[0017]
【発明の効果】以上説明したように、本発明にかかる反
応槽用散気攪拌装置によれば、散気手段をパドル羽根と
共に回転させながら散気させることにより、散気された
気泡の水面までの移動距離を長くすることができ、廃水
中への酸素溶解効率を向上させることが可能となる。As described above, according to the diffuser / stirrer for the reaction tank of the present invention, the diffuser is diffused while rotating together with the paddle blades, so that even the water surface of the diffused bubbles can be reached. It is possible to lengthen the moving distance of oxygen and improve the efficiency of oxygen dissolution in wastewater.
【図1】本発明の一実施例にかかる反応槽用散気攪拌装
置の概略構成の説明図である。FIG. 1 is an explanatory diagram of a schematic configuration of a diffuser stirring device for a reaction tank according to an embodiment of the present invention.
【図2】図1に示すA−A'方向から拡大した散気攪拌
装置の構成説明図である。FIG. 2 is an explanatory diagram of the structure of a diffuser stirring device enlarged from the AA ′ direction shown in FIG.
【図3】前記図1に用いられるパドル羽根の形状の説明
図である。FIG. 3 is an explanatory view of a shape of a paddle blade used in FIG.
【図4】本発明にかかる反応槽用散気攪拌装置を用いた
場合の気泡の軌道説明図である。FIG. 4 is an explanatory diagram of the trajectory of bubbles when the diffuser agitator for a reaction tank according to the present invention is used.
【図5】従来の散気装置及び攪拌装置の構成説明図であ
る。FIG. 5 is a structural explanatory view of a conventional air diffuser and stirring device.
【図6】従来の散気装置を用いた場合の気泡の軌道説明
図である。FIG. 6 is an explanatory diagram of the trajectory of bubbles when a conventional air diffuser is used.
10、110 … 反応槽 12、112 … 散気管 14、114 … ブロワー 16、116 … 回転中空軸(回転軸) 18 … 羽根 20、120 … モータ 130 … 上部パドル羽根 132 … 下部パドル羽根 134 … 吸気管 136 … 通気管 10, 110 ... Reaction tank 12, 112 ... Air diffuser 14, 114 ... Blower 16, 116 ... Rotating hollow shaft (rotating shaft) 18 ... Blade 20, 120 ... Motor 130 ... Upper paddle blade 132 ... Lower paddle blade 134 ... Intake pipe 136 ... Ventilation pipe
Claims (1)
回転中空軸と、 前記回転中空軸の上端口から下端口へと軸内に導気する
導気手段と、 前記反応槽底部に配置され、前記回転中空軸により回転
するパドル羽根と、 前記パドル羽根に沿って設けられ、前記回転中空軸の下
端口が連通した通気管と、 前記通気管に設けられ、かつ散気孔を有する散気手段
と、を備えたことを特徴とする反応槽用散気攪拌装置。1. A rotary hollow shaft that hangs down to the bottom of the reaction tank, an air guiding means that guides air into the rotary hollow shaft from an upper end opening to a lower opening, and the reaction tank bottom. A paddle blade that is disposed on the rotating hollow shaft and that rotates by the rotating hollow shaft; a ventilation pipe that is provided along the paddle blade and that communicates with a lower end opening of the rotating hollow shaft; and a ventilation hole that is provided in the ventilation pipe. An air diffuser for a reaction tank, comprising: an air diffuser.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6242040A JPH0871583A (en) | 1994-09-08 | 1994-09-08 | Air diffusing stirrer for reaction tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6242040A JPH0871583A (en) | 1994-09-08 | 1994-09-08 | Air diffusing stirrer for reaction tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0871583A true JPH0871583A (en) | 1996-03-19 |
Family
ID=17083387
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6242040A Pending JPH0871583A (en) | 1994-09-08 | 1994-09-08 | Air diffusing stirrer for reaction tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0871583A (en) |
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US20110042305A1 (en) * | 2008-02-21 | 2011-02-24 | Farm Renewable Environmental Energy Ltd | Gas actuated mixing system and method |
KR101114524B1 (en) * | 2011-07-13 | 2012-02-27 | 덕인환경주식회사 | Air supply device |
KR101156056B1 (en) * | 2010-03-25 | 2012-06-27 | 대한민국 | Water purifying device |
KR20160069403A (en) * | 2014-12-08 | 2016-06-16 | 주식회사 포스코 | Apparatus for storing solution |
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1994
- 1994-09-08 JP JP6242040A patent/JPH0871583A/en active Pending
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US8608965B2 (en) * | 2008-02-21 | 2013-12-17 | Farm Renewable Environmental Energy Ltd. | Gas actuated mixing system and method |
US20110042305A1 (en) * | 2008-02-21 | 2011-02-24 | Farm Renewable Environmental Energy Ltd | Gas actuated mixing system and method |
KR101156056B1 (en) * | 2010-03-25 | 2012-06-27 | 대한민국 | Water purifying device |
KR101114524B1 (en) * | 2011-07-13 | 2012-02-27 | 덕인환경주식회사 | Air supply device |
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CN106396090A (en) * | 2016-10-16 | 2017-02-15 | 李根生 | Suspended underwater plug flow aeration machine |
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CN109231615A (en) * | 2018-11-06 | 2019-01-18 | 冷应杰 | A kind of electroplating waste water treatment equipment |
CN110074974A (en) * | 2019-05-09 | 2019-08-02 | 浙江厚达智能科技股份有限公司 | Bias stirring air blowing type Traditional Chinese medicine decocting method |
CN110074975A (en) * | 2019-05-09 | 2019-08-02 | 浙江厚达智能科技股份有限公司 | The Traditional Chinese medicine decocting bucket of eccentric setting tracheae |
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CN114653275A (en) * | 2022-04-24 | 2022-06-24 | 罗赛洛(温州)明胶有限公司 | Utilize gelatin automated production system of compressed air technique |
CN114849598A (en) * | 2022-06-06 | 2022-08-05 | 宿州汉泰化工有限公司 | Phosphorus pentachloride production reactor |
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CN115888508A (en) * | 2023-02-21 | 2023-04-04 | 喜跃发国际环保新材料股份有限公司 | Processing technology and processing system of water-based paint |
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