JP2005125205A - Air diffuser, foam separator and wastewater purification system - Google Patents

Air diffuser, foam separator and wastewater purification system Download PDF

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JP2005125205A
JP2005125205A JP2003362282A JP2003362282A JP2005125205A JP 2005125205 A JP2005125205 A JP 2005125205A JP 2003362282 A JP2003362282 A JP 2003362282A JP 2003362282 A JP2003362282 A JP 2003362282A JP 2005125205 A JP2005125205 A JP 2005125205A
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liquid
air diffuser
foam
main body
bubbles
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JP2005125205A5 (en
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Osamu Yamamoto
修 山本
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Japan Techno Mate Corp
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Japan Techno Mate Corp
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

<P>PROBLEM TO BE SOLVED: To efficiently diffuse a large amount of fine bubbles into liquid to be treated, and to efficiently take out pollutants etc., in the liquid to be treated. <P>SOLUTION: An air diffuser 10 has a casing 11 having a gas outlet surface in which many small holes for spouting gas are formed, and a thin sheet-like bubble atomizing member 15 facing the gas outlet surface so as to leave a fixed gap between them. The bubble atomizing member 15 is freely rotatable in the casing 11, and, for example, has a radially extending slit. The bubbles discharged from the small holes are cut and atomized when they pass through the slit opening. Rotation of the bubble atomizing member 15 efficiently diffuses the bubbles in the liquid. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、気泡を液体中に吹出して分散させる散気装置と、散気装置を用いた泡沫分離装置および排水浄化システムに関する。   The present invention relates to an air diffuser that blows and disperses bubbles in a liquid, a foam separation device using the air diffuser, and a drainage purification system.

従来、例えば水棲生物の飼育水槽中の飼育水に含まれる微細な汚濁物質等を分離する泡沫分離装置として、次のような構成が知られている(特許文献1)。これは、飼育水槽から送られてきた被処理水を内筒内に導き、内筒内では散気装置によって微細な気泡を発生させるというものである。すなわち汚濁物質等は、気泡がその外周面に付着することによって液面まで浮上し、汚濁物質を含む多量の泡が液面上から泡沫分離装置の外部へ排出される。汚濁物質を含まない処理済水は内筒の外周を囲繞する外筒内に導かれ、外筒から排出されて飼育水槽に戻される。   2. Description of the Related Art Conventionally, for example, the following configuration is known as a foam separation device for separating fine pollutants contained in breeding water in aquatic creature breeding aquarium (Patent Document 1). In this method, the water to be treated sent from the breeding water tank is guided into the inner cylinder, and fine bubbles are generated in the inner cylinder by the air diffuser. That is, the pollutant or the like floats up to the liquid surface by the bubbles adhering to the outer peripheral surface, and a large amount of bubbles containing the pollutant are discharged from the liquid surface to the outside of the foam separation device. The treated water not containing the pollutant is guided into the outer cylinder surrounding the outer periphery of the inner cylinder, discharged from the outer cylinder, and returned to the breeding water tank.

従来の散気装置は通常、円筒状あるいは平板状の多孔質の燒結材を有している。しかし、燒結材から気泡を吹出すには高い圧力が必要なため、消費エネルギーが大きくなる。また大量の気体を吹出そうとすると気泡径が大きくなりすぎて、汚濁物質等の除去作用には適さない。これに対し、ある程度小さな気泡を発生させるためには気体の吹出し量に限界がある。したがって従来の散気装置を用いた泡沫分離装置では、被処理水の浄化性能を充分に高めることは困難であった。
特開2001−170617号公報
Conventional diffusers usually have a cylindrical or flat porous sintering material. However, since high pressure is required to blow bubbles from the sintered material, energy consumption increases. If a large amount of gas is blown out, the bubble diameter becomes too large, which is not suitable for removing pollutants. On the other hand, in order to generate a small bubble to some extent, there is a limit to the amount of gas blown out. Therefore, it has been difficult to sufficiently improve the purification performance of the water to be treated in the foam separation apparatus using the conventional air diffuser.
JP 2001-170617 A

本発明は、微細な気泡を効率よく大量に被処理液中に分散させることことができる散気装置を提供すること、この散気装置を用いて被処理液中の汚濁物質等を効率よく取出すことができる泡沫分離装置および排水浄化システムを提供することを目的としている。   The present invention provides an air diffuser capable of efficiently dispersing a large amount of fine bubbles in a liquid to be treated, and efficiently using this air diffuser to remove contaminants and the like in the liquid to be treated. It is an object of the present invention to provide a foam separation device and a waste water purification system that can be used.

本発明に係る散気装置は、気体を吹出すための多数の小孔が形成された気体吹出し面を有するケーシングと、気体吹出し面に対して、所定の間隙をもって対向するとともに相対移動自在に設けられ、スリット状開口を有する薄板状の気泡微細化部材とを備えることを特徴としている。   An air diffuser according to the present invention is provided with a casing having a gas blowing surface in which a large number of small holes for blowing gas are formed, and a gas blowing surface facing the gas blowing surface with a predetermined gap and being relatively movable. And a thin plate-like bubble refining member having a slit-like opening.

多数の小孔は気体吹出し面において例えば放射状に配列される。ケーシングは例えば円筒状を有する。この場合、気体吹出し面が円筒の上面または底面であることが好ましい。スリット状開口は放射状に延びていてもよい。好ましくは、気泡微細化部材は気体吹出し面に対して平行状態を保持しつつ、所定の軸周りに回転自在である。これにより、小孔から吹出される気泡はスリット状開口を通過することにより切断されて微細化され、被処理液全体が回転攪拌されることにより気泡は効率よく分散する。したがって汚濁物質等の表面に効率よく付着して、汚濁物質等の浮上を促進する。   A large number of small holes are arranged radially, for example, on the gas blowing surface. The casing has, for example, a cylindrical shape. In this case, the gas blowing surface is preferably the upper surface or the bottom surface of the cylinder. The slit-shaped openings may extend radially. Preferably, the bubble refining member is rotatable around a predetermined axis while maintaining a parallel state with respect to the gas blowing surface. Thereby, the bubbles blown out from the small holes are cut and refined by passing through the slit-like openings, and the bubbles are efficiently dispersed by rotating and stirring the entire liquid to be treated. Therefore, it effectively adheres to the surface of the pollutant and promotes the flotation of the pollutant.

本発明に係る泡沫分離装置は、上記散気装置により発生した気泡が被処理液中に含まれる汚濁物質の表面に吸着して液面に浮上した大量の泡から前記汚濁物質を取出す泡沫分離装置であって、本体と、本体に設けられ、液面上の泡を吸引して集める集泡部と、集泡部によって吸引された泡を液化させる消泡部とを備えることを特徴としている。   The foam separation apparatus according to the present invention is a foam separation apparatus that takes out the pollutant from a large amount of bubbles that are generated by the bubbles generated by the air diffuser adsorbed on the surface of the pollutant contained in the liquid to be treated and floated on the liquid surface And it is provided with the main body, the foam collection part which is provided in the main body and attracts | sucks and collects the foam | bubble on a liquid level, and the defoaming part which liquefies the foam suck | inhaled by the foam collection part.

泡沫分離装置は、本体内に設けられて散気室と溢流室に区画し、上端部が液面よりも下側に位置する溢流壁を備えることが好ましい。この構成によれば、汚濁物質等を除去された処理済液は溢流壁を越えて溢流室へ流入し、泡沫分離装置から外部へ排出される。   It is preferable that the foam separation device includes an overflow wall that is provided in the main body and divides into an aeration chamber and an overflow chamber, and an upper end portion is located below the liquid level. According to this configuration, the treated liquid from which contaminants and the like have been removed flows into the overflow chamber over the overflow wall and is discharged from the foam separation device to the outside.

本体の下部に、散気室内に被処理液を供給するための給液口が設けられ、また、溢流室から処理済液を排出するための排液口が設けられることが好ましい。給液口は、本体の底部であって散気装置に対向する部位に開口してもよい。また給液口は本体の側面に開口し、散気装置が給液口よりも上方に設けられる内床に載置され、内床の散気装置に対向した部位に、液導入口が形成されてもよい。   It is preferable that a liquid supply port for supplying the liquid to be processed is provided in the lower part of the main body, and a liquid discharge port for discharging the processed liquid from the overflow chamber is provided. The liquid supply port may be opened at a portion that is the bottom of the main body and faces the diffuser. The liquid supply port opens on the side surface of the main body, the air diffuser is placed on the inner floor provided above the liquid supply port, and the liquid inlet is formed at a portion of the inner floor facing the air diffuser. May be.

溢流壁は例えば平板状であるが、本体が円筒状を有している場合には、溢流壁は本体と同心的な円筒状を有していてもよい。   The overflow wall has a flat plate shape, for example, but when the main body has a cylindrical shape, the overflow wall may have a cylindrical shape concentric with the main body.

好ましくは、消泡部はハウジングと、ハウジング内に導かれる泡が衝突して破壊する邪魔板とを備える。これにより、汚濁物質等は効率よく取出される。   Preferably, the defoaming portion includes a housing and a baffle plate that is collided with and destroyed by bubbles guided into the housing. Thereby, a pollutant etc. are taken out efficiently.

本発明に係る排水浄化システムは、上記散気装置と、散気装置に気体を供給する給気手段と、上記泡沫分離装置とを備え、給気手段が消泡部を介して集泡部における泡の吸引を行い、この吸引によって発生する排気を散気装置に供給することを特徴としている。   The waste water purification system according to the present invention includes the above air diffuser, an air supply unit that supplies gas to the air diffuser, and the foam separation device, and the air supply unit is disposed in the foam collecting unit via the defoaming unit. It is characterized by sucking bubbles and supplying exhaust generated by this suction to the air diffuser.

以上のように本発明によれば、微細な気泡を効率よく大量に被処理液中に分散させることことができる散気装置、この散気装置を用いて被処理液中の汚濁物質等を効率よく取出すことができる泡沫分離装置および排水浄化システムが得られる。   As described above, according to the present invention, an air diffuser that can efficiently disperse a large amount of fine bubbles in a liquid to be treated, and a pollutant in the liquid to be treated can be efficiently used by using the air diffuser. A foam separation device and a waste water purification system that can be taken out well are obtained.

以下、本発明の実施形態を図面を参照して説明する。
図1は、本発明の一実施形態である散気装置と泡沫分離装置を備えた排水浄化システムを概略的に示す模式的な断面図である。この排水浄化システムは、例えばアコヤガイの洗浄に用いた海水である被処理液を浄化するために用いられるが、その他の被処理液を浄化するために用いてもよい。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a schematic cross-sectional view schematically showing a wastewater purification system including an air diffuser and a foam separator according to an embodiment of the present invention. This waste water purification system is used to purify the liquid to be treated, which is seawater used for cleaning pearl oysters, for example, but may be used to purify other liquids to be treated.

排水浄化システムは散気装置10と泡沫分離装置50とブロア90から構成される。散気装置10は泡沫分離装置50の本体51内に設けられ、本体51に貯留される被処理液Wに多数の気泡を吹出して分散させる。気泡は被処理液Wに含まれる汚濁物質の表面に付着し、汚濁物質は液面へ浮上する。これにより液面には大量の泡が発生し、泡は集泡部52によって吸引され、消泡部53において液化される。泡を吸引するための負圧はブロア90によって発生し、ブロア90の排気は散気装置10へ送られる。   The waste water purification system includes an air diffuser 10, a foam separator 50, and a blower 90. The air diffuser 10 is provided in the main body 51 of the foam separation device 50 and blows and disperses a large number of bubbles in the liquid W to be stored in the main body 51. Bubbles adhere to the surface of the pollutant contained in the liquid W to be treated, and the pollutant floats to the liquid surface. As a result, a large amount of bubbles are generated on the liquid surface, and the bubbles are sucked by the bubble collecting part 52 and liquefied in the defoaming part 53. Negative pressure for sucking bubbles is generated by the blower 90, and the exhaust of the blower 90 is sent to the air diffuser 10.

泡沫分離装置50の本体51の内部は、溢流壁54によって散気室55と溢流室56に区画される。溢流壁54の下端部は本体51の底面に固定され、上端部は液面よりも下方に位置する。本体51の下部の側面には、被処理液である海水を散気室55に供給するための給液口57が開口する。本体51の給液口57とは反対側の側面下部には、処理済液である海水を溢流室56から排出するための排液口58が設けられる。   The interior of the main body 51 of the foam separation device 50 is partitioned into an aeration chamber 55 and an overflow chamber 56 by an overflow wall 54. The lower end portion of the overflow wall 54 is fixed to the bottom surface of the main body 51, and the upper end portion is located below the liquid level. A liquid supply port 57 for supplying seawater, which is a liquid to be processed, to the aeration chamber 55 is opened on the side surface of the lower portion of the main body 51. A drainage port 58 for discharging seawater, which is a processed liquid, from the overflow chamber 56 is provided at the lower part of the side surface opposite to the liquid supply port 57 of the main body 51.

また散気室55内において、給液口57よりも上方には内床60が設けられる。散気装置10は、例えば複数本の支持脚61を介して内床60に設置され、内床60の散気装置10に対向した部位には液導入口62が形成される。   In the air diffuser chamber 55, an inner floor 60 is provided above the liquid supply port 57. The air diffuser 10 is installed on the inner floor 60 through, for example, a plurality of support legs 61, and a liquid inlet 62 is formed at a portion of the inner floor 60 facing the air diffuser 10.

集泡部52は本体51の上部に設けられる。集泡部52は例えば円錐状を有し、円錐の頂点には排泡管63の一端が接続される。排泡管63の他端は消泡部53のハウジング67の上部に接続され、また消泡部53のハウジング67内において、排泡管63の先端には液化機構64が設けられる。また集泡部52のハウジング67の上部には吸気管65が接続され、吸気管65の他端はブロア90に接続される。ブロア90には排気管66が接続されており、排気管66は散気装置10に接続される。   The foam collecting part 52 is provided on the upper part of the main body 51. The bubble collecting part 52 has, for example, a conical shape, and one end of the bubble discharging pipe 63 is connected to the apex of the cone. The other end of the bubble removing pipe 63 is connected to the upper portion of the housing 67 of the defoaming part 53, and a liquefaction mechanism 64 is provided at the tip of the bubble removing pipe 63 in the housing 67 of the defoaming part 53. In addition, an intake pipe 65 is connected to the upper portion of the housing 67 of the foam collecting portion 52, and the other end of the intake pipe 65 is connected to the blower 90. An exhaust pipe 66 is connected to the blower 90, and the exhaust pipe 66 is connected to the air diffuser 10.

ブロア90が作動すると、吸気管65と集泡部52のハウジング67と排泡管63を介して、集泡部52における泡の吸引が行われる。この吸引によって発生する排気すなわち空気は、排気管65を介して散気装置10に供給される。   When the blower 90 is actuated, bubbles are sucked in the bubble collecting portion 52 through the intake pipe 65, the housing 67 of the bubble collecting portion 52, and the bubble removing pipe 63. Exhaust gas generated by the suction, that is, air is supplied to the air diffuser 10 through the exhaust pipe 65.

図2は泡沫分離装置50の本体51の内部を上から見た図である。すなわち本体51は上から見ると矩形を呈し、溢流壁54は平板状を有する。散気装置10は散気室55の略中央に位置し、上から見ると円形を呈する。   FIG. 2 is a view of the inside of the main body 51 of the foam separation device 50 as viewed from above. That is, the main body 51 has a rectangular shape when viewed from above, and the overflow wall 54 has a flat plate shape. The air diffuser 10 is located in the approximate center of the air diffuser chamber 55 and has a circular shape when viewed from above.

図3〜図6は散気装置10を示す。
図3と図4は散気装置10のケーシング11を上下反転させて示している。これらの図に示されるように、ケーシング11は扁平な円筒状を有し、円筒の底面である気体吹出し面12には、気体を吹出すための多数の小孔13が形成される。小孔13は気体吹出し面12の中央部を中心として放射状に配列される。小孔13の各列は等角度の間隔に配置される。なお、小孔13の配列は放射状である必要はなく、例えば気体吹出し面12において均一に分布してもよく、任意に定められる。
3 to 6 show the air diffuser 10.
3 and 4 show the casing 11 of the air diffuser 10 upside down. As shown in these drawings, the casing 11 has a flat cylindrical shape, and a large number of small holes 13 for blowing gas are formed in the gas blowing surface 12 which is the bottom surface of the cylinder. The small holes 13 are arranged radially around the center of the gas blowing surface 12. Each row of small holes 13 is arranged at equiangular intervals. In addition, the arrangement | sequence of the small hole 13 does not need to be radial, for example, may be uniformly distributed in the gas blowing surface 12, and is defined arbitrarily.

ケーシング11の側面には空気導入口14が設けられる。空気導入口14にはブロア90に接続された排気管66が連結され(図1参照)、ケーシング11内にはブロア90からの排気が導かれる。   An air inlet 14 is provided on the side surface of the casing 11. An exhaust pipe 66 connected to the blower 90 is connected to the air inlet 14 (see FIG. 1), and exhaust from the blower 90 is guided into the casing 11.

図5に示すように、薄い円板である気泡微細化部材15が、気体吹出し面12に対して所定の間隙をもって対向する。気泡微細化部材15は気体吹出し面12に対して回転自在に設けられる。すなわち気泡微細化部材15は、気体吹出し面12に対して平行状態を保持しつつ円板の中心軸周りに回転自在である。   As shown in FIG. 5, the bubble miniaturizing member 15, which is a thin disk, faces the gas blowing surface 12 with a predetermined gap. The bubble refining member 15 is provided to be rotatable with respect to the gas blowing surface 12. That is, the bubble refining member 15 is rotatable around the central axis of the disk while maintaining a parallel state with respect to the gas blowing surface 12.

気泡微細化部材15には、その中心から放射方向に直線的に延びる複数のスリット状開口16が形成される。各スリット状開口16は等角度の間隔を成すことが好ましいが、これには限定されない。またスリット状開口16は放射状である必要はなく、目的に応じて任意に決定される。   The bubble miniaturizing member 15 is formed with a plurality of slit-like openings 16 that extend linearly from the center in the radial direction. Each slit-shaped opening 16 preferably has an equiangular interval, but is not limited thereto. The slit-shaped openings 16 do not have to be radial, and are arbitrarily determined according to the purpose.

図6は散気装置10が実際に泡沫分離装置50内に設置される状態を示す。この図に示すように散気装置10は、気泡微細化部材15が下側にくるように設置される。ケーシング11の上面にはモータ17が載置される。モータ17には図示しない給電装置から電力が供給されるが、給電装置はブロア90(図1参照)の電源であってもよい。モータ17の回転軸18はケーシング11の軸心部分を貫通して延びる。気泡微細化部材15は、回転軸18のケーシング11の底面からの突出部分に固定される。   FIG. 6 shows a state where the air diffuser 10 is actually installed in the foam separator 50. As shown in this figure, the air diffuser 10 is installed so that the bubble refining member 15 is on the lower side. A motor 17 is placed on the upper surface of the casing 11. Electric power is supplied to the motor 17 from a power supply device (not shown), but the power supply device may be a power source for the blower 90 (see FIG. 1). The rotating shaft 18 of the motor 17 extends through the axial center portion of the casing 11. The bubble refining member 15 is fixed to a protruding portion of the rotating shaft 18 from the bottom surface of the casing 11.

ブロア90から空気が供給されている状態でモータ17が駆動されると、薄板状の気泡微細化部材15が回転軸18を中心として回転するので、小孔13から排出される気泡はスリット状開口16によって切断され、微細化される。また気泡微細化部材15の回転により、被処理液が全体的に回転攪拌されるので、微細化された気泡Aは旋回しつつ上昇し、また対流して効率よく被処理液内に分散する。   When the motor 17 is driven in a state where air is supplied from the blower 90, the thin plate-shaped bubble miniaturizing member 15 rotates about the rotation shaft 18, so that the bubbles discharged from the small holes 13 are slit-shaped openings. 16 is cut and refined. Further, since the liquid to be processed is rotated and stirred as a whole by the rotation of the bubble refining member 15, the refined bubbles A rise while rotating, and convect and efficiently disperse in the liquid to be processed.

図7は泡沫分離装置50の液化機構64を示している。液化機構64は排泡管63の先端に固定された筒状部材71と、筒状部材71の中に設けられた邪魔板72とを有する。筒状部材71は下側が開口しており、排泡管63の先端は筒状部材71の略中央まで延びる。邪魔板72は排泡管63の先端開口に対向し、適当な連結部材により筒状部材71の内壁に固定される。   FIG. 7 shows the liquefaction mechanism 64 of the foam separation device 50. The liquefaction mechanism 64 includes a cylindrical member 71 fixed to the tip of the bubble discharging pipe 63, and a baffle plate 72 provided in the cylindrical member 71. The cylindrical member 71 is open on the lower side, and the tip of the bubble discharging pipe 63 extends to the approximate center of the cylindrical member 71. The baffle plate 72 is opposed to the tip opening of the bubble discharging pipe 63 and is fixed to the inner wall of the cylindrical member 71 by an appropriate connecting member.

したがって排泡管63からケーシング11内に放出された多量の泡は、邪魔板72に衝突して破壊される。すなわち泡は液化され、汚濁物質とともに消泡部53のハウジング67の底部に落下する。   Therefore, a large amount of bubbles discharged from the bubble discharging pipe 63 into the casing 11 collides with the baffle plate 72 and is destroyed. That is, the foam is liquefied and falls to the bottom of the housing 67 of the defoaming part 53 together with the pollutant.

本実施形態の排水浄化システムでは、次のように作用して被処理液が浄化される。
まず、図示しない排液装置から被処理液が供給され、給液口57から本体51内に供給される。液面が溢流壁54の上端を越えると、モータ17の給電装置とブロア90が駆動される。これにより、気泡微細化部材15が回転し、本体51内に大量の気泡が生じる。気泡は旋回しつつ上昇し、被処理液に含まれる汚濁物質に付着して、液面上には大量の泡が発生する。泡は集泡部52から排泡管63によって吸引され、消泡部53に導かれる。消泡部53では泡が液化され、泡から汚濁物質が取出される。すなわち汚濁物質は液体に混じってハウジング67内に貯留される。
In the wastewater purification system of the present embodiment, the liquid to be treated is purified by the following action.
First, the liquid to be treated is supplied from a drainage device (not shown) and supplied into the main body 51 from the liquid supply port 57. When the liquid level exceeds the upper end of the overflow wall 54, the power feeding device of the motor 17 and the blower 90 are driven. As a result, the bubble refining member 15 rotates and a large amount of bubbles are generated in the main body 51. The bubbles rise while swirling, adhere to the pollutant contained in the liquid to be treated, and a large amount of bubbles are generated on the liquid surface. The bubbles are sucked from the bubble collecting portion 52 by the bubble removing pipe 63 and guided to the defoaming portion 53. In the defoaming section 53, the foam is liquefied and the pollutant is taken out from the foam. That is, the pollutant is mixed in the liquid and stored in the housing 67.

一方、本体51内において、汚濁物質が除去された処理済液は溢流壁54を越えて散気室55から溢流室56へ流動する。そして処理済液は、溢流室56の排液口58から外部へ排出される。   On the other hand, in the main body 51, the treated liquid from which the contaminants have been removed flows from the diffuser chamber 55 to the overflow chamber 56 over the overflow wall 54. Then, the treated liquid is discharged to the outside from the drain port 58 of the overflow chamber 56.

以上のように本実施形態では、多孔質の燒結材を用いるのではなく、多数の小孔を有するケーシング11に微小隙間をもって対向する気泡微細化部材15を回転させることによって微細化された気泡を発生させている。したがって、従来よりも少ない消費エネルギーによって大量の気泡を液体中に吹出すことができるだけでなく、気泡を液体中において広範囲に拡散させることができ、被処理液の浄化性能が充分に高められる。また気泡は液中において効率よく分散するので、本体51の内壁面に付着したり、粗粒化することはない。   As described above, in the present embodiment, instead of using a porous sintered material, the air bubbles refined by rotating the air bubble refining member 15 facing the casing 11 having a large number of small holes with minute gaps are removed. Is generated. Therefore, not only can a large amount of bubbles be blown into the liquid with less energy consumption than before, but also the bubbles can be diffused over a wide range in the liquid, and the purification performance of the liquid to be treated is sufficiently enhanced. Further, since the bubbles are efficiently dispersed in the liquid, they do not adhere to the inner wall surface of the main body 51 or become coarse.

図8は、排水浄化システムの他の実施形態を示す。図1の排水浄化システムとの相違点は散気装置10が内床60(図1)ではなく、本体51の底部81の上に脚部材82を介して載置される。また給液口57は底部81において、散気装置1に対向する部位に開口する。その他の構成は図1と同様であるので、その説明を省略する。   FIG. 8 shows another embodiment of the waste water purification system. The difference from the waste water purification system of FIG. 1 is that the air diffuser 10 is placed not on the inner floor 60 (FIG. 1) but on the bottom 81 of the main body 51 via the leg member 82. Further, the liquid supply port 57 opens at a portion facing the diffuser 1 at the bottom 81. Since other configurations are the same as those in FIG. 1, the description thereof is omitted.

図9は散気装置10の他の実施形態を示す。気体吹出し面12がケーシング11の上面に形成され、気泡微細化部材15はケーシング11の上側に設けられる。モータ17は散気装置10の上方であって液面Bよりも上に設けられ、モータ17の回転軸18は垂直下方に延びて気泡微細化部材15の中心に固定される。したがって気泡微細化部材15によって微細化された気泡は、気泡微細化部材15から直接上方に吹出され、液中に拡散される。その他の構成は図1〜図6に示す例と同じである。   FIG. 9 shows another embodiment of the air diffuser 10. A gas blowing surface 12 is formed on the upper surface of the casing 11, and the bubble refining member 15 is provided on the upper side of the casing 11. The motor 17 is provided above the air diffuser 10 and above the liquid level B. The rotating shaft 18 of the motor 17 extends vertically downward and is fixed to the center of the bubble miniaturizing member 15. Accordingly, the air bubbles refined by the air bubble refining member 15 are directly blown upward from the air bubble refining member 15 and diffused into the liquid. Other configurations are the same as the example shown in FIGS.

図10は泡沫分離装置50の本体51の他の例を示す。本体51は円筒状を有し、散気装置10は本体51の略中央に設けられる。溢流壁54は本体51の中心から排液口58側にずれた位置に形成される。その他の構成は図1、2と同様である。   FIG. 10 shows another example of the main body 51 of the foam separation device 50. The main body 51 has a cylindrical shape, and the air diffuser 10 is provided at substantially the center of the main body 51. The overflow wall 54 is formed at a position shifted from the center of the main body 51 to the drainage port 58 side. Other configurations are the same as those in FIGS.

図11は泡沫分離装置50のさらに他の例を示す。本体51は円筒状を有し、溢流壁54は本体51と同心的な円筒状を有する。すなわち溢流室56は散気室55を囲繞する筒状を呈する。その他の構成は図1、2と同様である。   FIG. 11 shows still another example of the foam separation device 50. The main body 51 has a cylindrical shape, and the overflow wall 54 has a cylindrical shape concentric with the main body 51. That is, the overflow chamber 56 has a cylindrical shape surrounding the air diffusion chamber 55. Other configurations are the same as those in FIGS.

本発明の一実施形態である散気装置と泡沫分離装置を備えた排水浄化システムを概略的に示す模式的な断面図である。It is typical sectional drawing which shows roughly the waste water purification system provided with the diffuser and foam separation apparatus which are one Embodiment of this invention. 泡沫分離装置の本体の内部を上から見た図である。It is the figure which looked at the inside of the main part of a foam separation device from the top. 散気装置のケーシングを上下反転させて示す斜視図である。It is a perspective view which shows the casing of an air diffuser upside down. 散気装置のケーシングを上下反転させて示す断面図である。It is sectional drawing which shows the casing of an air diffuser upside down. 散気装置の気泡微細化部材を示す斜視図である。It is a perspective view which shows the bubble refinement | miniaturization member of an air diffuser. 散気装置が実際に泡沫分離装置内に設置される状態を示す側面図である。It is a side view which shows the state by which an air diffuser is actually installed in a foam separation apparatus. 泡沫分離装置の液化機構を示す断面図である。It is sectional drawing which shows the liquefaction mechanism of a foam separator. 排水浄化システムの他の実施形態を示す模式的な断面図である。It is typical sectional drawing which shows other embodiment of a waste water purification system. 散気装置の他の実施形態を示す側面図である。It is a side view which shows other embodiment of a diffuser. 泡沫分離装置の本体の他の例を示す平面図である。It is a top view which shows the other example of the main body of a foam separation apparatus. 泡沫分離装置の本体のさらに他の例を示す平面図である。It is a top view which shows the further another example of the main body of a foam separation apparatus.

符号の説明Explanation of symbols

10 散気装置
11 ケーシング
12 気体吹出し面
13 小孔
15 気泡微細化部材
16 スリット状開口
50 泡沫分離装置
51 本体
53 消泡部
DESCRIPTION OF SYMBOLS 10 Air diffuser 11 Casing 12 Gas blowing surface 13 Small hole 15 Bubble refinement member 16 Slit-shaped opening 50 Foam separator 51 Main body 53 Defoaming part

Claims (16)

被処理液中に設置され、気泡を前記被処理液中に吹出して分散させる散気装置であって、
前記気体を吹出すための多数の小孔が形成された気体吹出し面を有するケーシングと、
前記気体吹出し面に対して、所定の間隙をもって対向するとともに相対移動自在に設けられ、スリット状開口を有する薄板状の気泡微細化部材と
を備えることを特徴とする散気装置。
An air diffuser that is installed in a liquid to be treated and blows and disperses bubbles in the liquid to be treated.
A casing having a gas blowing surface in which a large number of small holes for blowing the gas are formed;
An air diffuser comprising: a thin-plate-shaped bubble refining member that is opposed to the gas blowing surface with a predetermined gap and is relatively movable, and has a slit-like opening.
前記多数の小孔が前記気体吹出し面において放射状に配列されることを特徴とする請求項1に記載の散気装置。   The air diffuser according to claim 1, wherein the plurality of small holes are arranged radially on the gas blowing surface. 前記ケーシングが円筒状を有することを特徴とする請求項1に記載の散気装置。   The air diffuser according to claim 1, wherein the casing has a cylindrical shape. 前記気体吹出し面が円筒の上面または底面であることを特徴とする請求項3に記載の散気装置。   The air diffuser according to claim 3, wherein the gas blowing surface is an upper surface or a bottom surface of a cylinder. 前記スリット状開口が放射状に延びることを特徴とする請求項1に記載の散気装置。   The air diffuser according to claim 1, wherein the slit-shaped openings extend radially. 前記気泡微細化部材が前記気体吹出し面に対して平行状態を保持しつつ、所定の軸周りに回転自在であることを特徴とする請求項1に記載の散気装置。   The air diffuser according to claim 1, wherein the bubble refining member is rotatable around a predetermined axis while maintaining a parallel state with respect to the gas blowing surface. 請求項1に記載の散気装置により発生した気泡が被処理液中に含まれる汚濁物質の表面に吸着して液面に浮上した大量の泡から前記汚濁物質を取出す泡沫分離装置であって、
本体と、
前記本体に設けられ、液面上の前記泡を吸引して集める集泡部と、
前記集泡部によって吸引された泡を液化させる消泡部と
を備えることを特徴とする泡沫分離装置。
A foam separation device that takes out the pollutant from a large amount of bubbles that are generated by the air bubbles generated by the air diffuser according to claim 1 adsorbed on the surface of the pollutant contained in the liquid to be treated and floated on the liquid surface,
The body,
A foam collecting part provided in the main body, for sucking and collecting the bubbles on the liquid surface;
A foam separating apparatus comprising: a defoaming unit that liquefies foam sucked by the foam collecting unit.
前記本体内に設けられて散気室と溢流室に区画し、上端部が前記液面よりも下側に位置する溢流壁を備えることを特徴とする請求項7に記載の泡沫分離装置。   The foam separation device according to claim 7, further comprising an overflow wall provided in the main body, divided into a diffuser chamber and an overflow chamber, and having an upper end portion located below the liquid level. . 前記本体の下部に、前記散気室内に被処理液を供給するための給液口が設けられることを特徴とする請求項8に記載の泡沫分離装置。   The foam separating apparatus according to claim 8, wherein a liquid supply port for supplying a liquid to be processed is provided in the lower part of the main body. 前記本体の下部に、前記溢流室から処理済液を排出するための排液口が設けられることを特徴とする請求項9に記載の泡沫分離装置。   The foam separating apparatus according to claim 9, wherein a drainage port for discharging the treated liquid from the overflow chamber is provided at a lower portion of the main body. 前記給液口が、前記本体の底部であって前記散気装置に対向する部位に開口することを特徴とする請求項9に記載の泡沫分離装置。   The foam separating apparatus according to claim 9, wherein the liquid supply port opens at a part of the bottom of the main body that faces the diffuser. 前記給液口が前記本体の側面に開口し、前記散気装置が前記給液口よりも上方に設けられる内床に載置され、前記内床の前記散気装置に対向した部位に、液導入口が形成されることを特徴とする請求項9に記載の泡沫分離装置。   The liquid supply port opens on a side surface of the main body, the air diffuser is placed on an inner floor provided above the liquid supply port, and a liquid is provided at a portion of the inner floor facing the air diffuser. The foam separation device according to claim 9, wherein an introduction port is formed. 前記溢流壁が平板状であることを特徴とする請求項8に記載の泡沫分離装置。   The foam separating apparatus according to claim 8, wherein the overflow wall has a flat plate shape. 前記本体が円筒状を有し、前記溢流壁が前記本体と同心的な円筒状を有することを特徴とする請求項8に記載の泡沫分離装置。   The foam separating apparatus according to claim 8, wherein the main body has a cylindrical shape, and the overflow wall has a cylindrical shape concentric with the main body. 前記消泡部がハウジングと、前記ハウジング内に導かれる泡が衝突して破壊する邪魔板とを備えることを特徴とする請求項7に記載の泡沫分離装置。   The foam separating apparatus according to claim 7, wherein the defoaming portion includes a housing and a baffle plate that is collided with and destroys the foam guided into the housing. 請求項1に記載の散気装置と、
前記散気装置に気体を供給する給気手段と、
請求項7に記載の泡沫分離装置と
を備え、前記給気手段は、前記消泡部を介して前記集泡部における泡の吸引を行い、この吸引によって発生する排気を前記散気装置に供給することを特徴とする排水浄化システム。

An air diffuser according to claim 1;
An air supply means for supplying gas to the air diffuser;
The foam separation device according to claim 7, wherein the air supply unit sucks bubbles in the bubble collecting unit via the defoaming unit, and supplies exhaust generated by the suction to the diffuser. A wastewater purification system characterized by

JP2003362282A 2003-10-22 2003-10-22 Air diffuser, foam separator and wastewater purification system Pending JP2005125205A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008212868A (en) * 2007-03-06 2008-09-18 Mitsubishi Electric Corp Sludge treatment apparatus
JP2009119338A (en) * 2007-11-13 2009-06-04 Kurita Water Ind Ltd Dissolved air floatation system
JP2017196563A (en) * 2016-04-27 2017-11-02 西松建設株式会社 Purification treatment device of contaminated water
JP7390912B2 (en) 2020-02-03 2023-12-04 オルガノ株式会社 Foam separator and breeding equipment equipped with the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008212868A (en) * 2007-03-06 2008-09-18 Mitsubishi Electric Corp Sludge treatment apparatus
JP2009119338A (en) * 2007-11-13 2009-06-04 Kurita Water Ind Ltd Dissolved air floatation system
JP2017196563A (en) * 2016-04-27 2017-11-02 西松建設株式会社 Purification treatment device of contaminated water
JP7390912B2 (en) 2020-02-03 2023-12-04 オルガノ株式会社 Foam separator and breeding equipment equipped with the same

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