WO2013175994A1 - 散気装置 - Google Patents

散気装置 Download PDF

Info

Publication number
WO2013175994A1
WO2013175994A1 PCT/JP2013/063358 JP2013063358W WO2013175994A1 WO 2013175994 A1 WO2013175994 A1 WO 2013175994A1 JP 2013063358 W JP2013063358 W JP 2013063358W WO 2013175994 A1 WO2013175994 A1 WO 2013175994A1
Authority
WO
WIPO (PCT)
Prior art keywords
main body
injection nozzle
liquid
gas
air diffuser
Prior art date
Application number
PCT/JP2013/063358
Other languages
English (en)
French (fr)
Inventor
泰彦 増田
洋泰 増田
Original Assignee
株式会社ソルエース
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 株式会社ソルエース filed Critical 株式会社ソルエース
Priority to IN2744KON2014 priority Critical patent/IN2014KN02744A/en
Priority to EP13794303.1A priority patent/EP2853308B1/en
Priority to US14/402,149 priority patent/US9446357B2/en
Priority to KR1020147033356A priority patent/KR101638782B1/ko
Priority to CN201380026690.1A priority patent/CN104321134B/zh
Priority to CA2872601A priority patent/CA2872601C/en
Publication of WO2013175994A1 publication Critical patent/WO2013175994A1/ja

Links

Images

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
    • B01F23/23105—Arrangement or manipulation of the gas bubbling devices
    • B01F23/2312—Diffusers
    • B01F23/23121—Diffusers having injection means, e.g. nozzles with circumferential outlet
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232—Mixing 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
    • B01F23/2323—Mixing 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
    • B01F23/23231—Mixing 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
    • B01F23/232311—Mixing 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4317—Profiled elements, e.g. profiled blades, bars, pillars, columns or chevrons
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/43197—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor characterised by the mounting of the baffles or obstructions
    • B01F25/431974—Support members, e.g. tubular collars, with projecting baffles fitted inside the mixing tube or adjacent to the inner wall
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71—Feed mechanisms
    • B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
    • B01F35/7179—Feed mechanisms characterised by the means for feeding the components to the mixer using sprayers, nozzles or jets
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/02—Aerobic processes
    • C02F3/12—Activated sludge processes
    • C02F3/20—Activated sludge processes using diffusers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/305—Treatment of water, waste water or sewage
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4317—Profiled elements, e.g. profiled blades, bars, pillars, columns or chevrons
    • B01F25/43171—Profiled blades, wings, wedges, i.e. plate-like element having one side or part thicker than the other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/43197—Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor characterised by the mounting of the baffles or obstructions
    • B01F25/431971—Mounted on the wall
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/32—Nature of the water, waste water, sewage or sludge to be treated from the food or foodstuff industry, e.g. brewery waste waters
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
    • 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
    • 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00—Gas and liquid contact apparatus
    • Y10S261/42—Ozonizers

Definitions

  • the present invention relates to an air diffuser for dispersing bubbles such as air in a liquid.
  • the air diffuser increases the amount of dissolved oxygen in the wastewater from sewage treatment plants, wastewater treatment plants in food factories and livestock farms, and other wastewater treatment facilities in other factories. It is used for applications such as preventing inadvertent spoilage of the liquid by increasing the amount.
  • a gas-liquid mixing device disclosed in Patent Document 1 filed by the present inventors is known.
  • This device comprises a pentagonal gas-liquid mixing cylinder that is open at the top and bottom, a collision blade arranged in multiple stages inside the gas-liquid mixing cylinder, and a gas jet nozzle arranged at the bottom of the gas-liquid mixing cylinder
  • the gas ejected from the gas ejection nozzle is refined by swirling and raising the gas-liquid mixing cylinder while colliding with the impingement blade, and is dissolved in the liquid.
  • the gas-liquid mixing device described above is capable of miniaturizing bubbles without causing clogging problems by the impingement blades arranged in the pentagonal gas-liquid mixing cylinder, is easy to maintain, and high It has the merit of obtaining oxygen dissolution efficiency.
  • the swirling flow is more effectively generated in the gas-liquid mixing cylinder by the gas ejection from the gas ejection nozzle, and the pulling-in force and stirring force such as sludge staying at the bottom is increased. there were.
  • an object of the present invention is to provide an air diffuser that can efficiently stir a liquid while miniaturizing the gas released into the liquid to achieve uniform dispersion.
  • the object of the present invention is to provide a main body having a flow channel inner surface having a pentagonal cross section formed in a cylindrical shape with both ends open, a wing member provided in multiple stages in a direction changed to the flow channel inner surface, and one of the main bodies And an injection nozzle provided at the opening end of the nozzle, immersed in a liquid in a state where the main body is erected so that the injection nozzle is on the lower side, and gas is injected into the main body from the injection nozzle
  • the spray nozzle has a center line of a spray port formed at a tip thereof intersecting the inner surface of the flow path below the blade member disposed at the lowest stage, and This is achieved by an air diffuser arranged so that an angle formed with the vertical direction is 45 degrees or less.
  • each of the wing members is preferably formed in a trapezoidal shape in plan view, and the upper bottom is preferably supported by one of the five flat surfaces constituting the inner surface of the flow path. It is preferable that the gas is jetted in a direction perpendicular to the plan view toward the plane portion where the upper bottom portion of the wing member arranged at the lowest stage is supported. It is more preferable that the wing members are arranged so that the circumferential interval between the flat portions where the upper bottom portion is supported in each step is gradually expanded from the lower step toward the upper step.
  • a support body that is placed on the floor and supports the main body and the injection nozzle, and the support body preferably has a circulation port through which liquid can pass under the main body.
  • an air diffuser that can efficiently stir a liquid while miniaturizing the gas released into the liquid to achieve uniform dispersion.
  • FIG. 1 is a front view
  • FIG. 2 is a plan view
  • FIG. 3 is a side view.
  • the air diffuser 1 includes a cylindrical main body 10, a plurality of blade units 20 provided inside the main body 10, a vent pipe 30 provided at a lower portion of the main body 10, And a support body 40 that supports the main body 10 and the vent pipe 30.
  • the main body 10 has openings at both ends and is formed in a regular pentagonal shape in plan view.
  • the main body 10 is formed of a metal material having a rust prevention effect such as stainless steel or a plastic material having water resistance or corrosion resistance such as engineering plastic. can do.
  • the blade unit 20 includes a frame body 22 and a blade member 24 supported by the frame body 22 as shown in a perspective view in FIG.
  • the frame 22 is formed in a regular pentagon shape so that the entire outer peripheral surface is in close contact with the inner peripheral surface of the main body 10, and the inner peripheral surface of the frame 22 has five flat portions 22 a, 22 b, 22 c, 22 d, 22e is continuously provided.
  • the wing member 24 is formed in a trapezoidal shape in plan view, the upper base 241 is supported by one flat portion 22a of the frame body 22, and the oblique sides 242 and 243 are other flat portions adjacent to both sides of the flat portion 22a. 22b and 22e are supported respectively.
  • the upper surface 24a and the lower surface 24b of the wing member 24 are both inclined surfaces so as to taper from the upper bottom portion 241 toward the lower bottom portion 244 on the distal end side, and a plurality of protrusions 24c are provided on the lower surface 24b. ing.
  • the inclination angles of the upper surface 24a and the lower surface 24b with respect to the horizontal plane are not particularly limited. For example, it is preferable to set the inclination angle of the upper surface 24a to 20 to 40 degrees and the inclination angle of the lower surface 24b to 10 to 30 degrees.
  • the wing unit 20 can be integrally formed of, for example, a resin material.
  • the plurality of blade units 20 having the above-described configuration are inserted into the main body 10 in multiple stages as indicated by broken lines in FIG.
  • the direction of the wing member 24 of each wing unit 20 is shown in a plan view in FIG.
  • five wing units 20 are arranged, and FIGS. 5A to 5E show from the top to the bottom in order from the top.
  • the wing unit 20 forms a flow path F of the main body 10 inside the frame body 22, and five plane portions F 1, F 2, F 2 are formed by the inner peripheral surface of the frame body 22.
  • a flow path inner surface having a regular pentagonal cross section in which F3, F4, and F5 are successively arranged counterclockwise is formed.
  • the lowermost wing unit 20 has a main body 10 in a direction in which a flat surface portion (hereinafter referred to as “support flat surface portion”) that supports the upper bottom portion 241 of the wing member 24 is a flat surface portion F1. Inserted into.
  • support flat surface portion a flat surface portion that supports the upper bottom portion 241 of the wing member 24
  • the blade unit 20 in the second stage from the bottom has a plane part adjacent to the support plane part F1 of the lowest stage blade unit 20 in the counterclockwise direction. It is inserted into the main body 10 in the direction to become the support plane part, that is, the direction in which the support plane part becomes the plane part F2. Then, as shown in FIG. 5C, the third wing unit 20 from the bottom has two adjacent flat portions counterclockwise with respect to the support flat portion F2 of the second wing unit 20 from the bottom. Is inserted into the main body 10 in such a direction as to become a support plane portion, that is, in a direction in which the support plane portion becomes a plane portion F4.
  • the circumferential interval between the support plane part of the wing unit 20 in an arbitrary stage other than the lowest stage and the support plane part of the wing unit 20 one lower stage is gradually increased from the lower stage toward the upper stage. It is configured to spread. That is, as shown in FIG. 5 (b), the support plane portion of the fourth stage blade unit 20 from the bottom is a plane portion F2 that is three adjacent counterclockwise from the plane portion F4, and the uppermost blade unit. As shown in FIG. 5A, the 20 support plane portions are the plane portions F1 that are four adjacent to each other in the counterclockwise direction from the plane portion F2.
  • each wing unit 20 is supported at a predetermined height in the main body 10 and fixed by the fixing ring 16 inserted last in the main body 10.
  • the inner surface of the spacer 14 is flush with the inner surface of the wing unit 20 and constitutes a part of the inner surface of the flow path of the main body 10.
  • the vent pipe 30 has an injection nozzle 32 formed at one end.
  • the injection nozzle 32 is provided at the opening end on the lower side of the main body 10, and an injection port 32a is formed at the tip.
  • a mounting portion 34 to which a hose (not shown) or the like can be attached is provided, and connected to an air supply source (not shown) such as a compressor, a blower, or a cylinder.
  • a gas such as air can be injected into the flow path of the main body 10 from the injection port 32a of the injection nozzle 32.
  • the injection nozzle 32 has a flat surface in which the center line C of the injection port 32 a extending in the normal direction of the opening surface forms one flat surface portion F ⁇ b> 1 constituting the flow path inner surface of the main body 10. It arrange
  • the flat surface portion F1 is a support flat surface portion of the lowermost blade unit 20 indicated by a broken line in FIG. Further, as shown in the longitudinal sectional view of the main part in FIG.
  • the injection nozzle 32 is configured such that the center line C of the injection port 32 a is below the wing member 24 of the wing unit 20 arranged at the lowest stage. It is arranged obliquely upward so as to intersect the road inner surface S. An angle ⁇ between the center line C and the vertical direction along the flow path inner surface S is set to 45 degrees or less.
  • the support 40 can be formed by bending a thin metal plate such as stainless steel, and as shown in FIGS. 1 to 3, a pair of base members 42 and 42 having left and right lower portions formed in a bent shape are provided. Yes.
  • the main body 10 and the vent pipe 30 are supported between the pair of base members 42 and 42.
  • Mounting holes 42a and 42a through which screws, anchor bolts, etc. can be inserted are formed in the base portions 42 and 42, and an appropriate interval (for example, 10) is provided between the lower end of the standing body 10 and the floor surface F.
  • the base portions 42 and 42 can be fixed to the floor surface F in a state where about 15 cm is opened.
  • the support body 40 has a flow port 44 through which a liquid can pass between a pair of base members 42, 42 below the lower end of the main body 10.
  • the main body 10 is erected in the vertical direction so that the injection nozzle 32 is on the lower side in a storage tank or the like in which liquid such as waste water or sewage to be treated is stored, and the air diffuser 1 is installed.
  • the air diffuser 1 can be installed by fixing the base portion 42 of the support body 40 to the floor surface F as described above.
  • the main body 10 is suspended and supported from above without using the support body 40. It is also possible to do. You may make it mix aerobic microorganisms, such as activated sludge, in a storage tank.
  • compressed air or the like is supplied from an air supply source (not shown) connected to the vent pipe 30, and gas is supplied from the injection nozzle 32 into the flow path of the main body 10.
  • air supply source not shown
  • gas is supplied from the injection nozzle 32 into the flow path of the main body 10.
  • the liquid is drawn from the lower end of the main body 10 by the ejector effect, and rises with the injected gas.
  • the sludge or the like is also mixed with the liquid by stirring and introduced into the main body 10.
  • the injection nozzle 32 is arranged such that the center line C of the injection port 32a intersects the flow path inner surface S below the lowermost wing member 24, and further in the vertical direction.
  • the angle ⁇ formed is set to 45 degrees or less so as to approach vertically upward. Therefore, there is no possibility that the injected gas collides with the lower surface 24b of the wing member 24 and is reflected downward, and there is no problem that sufficient ascending force cannot be obtained because the injection direction is nearly horizontal. Therefore, the wing member 24 ascends smoothly to the lowermost wing member 24 along the flow path inner surface S, collides with the lower surface 24b of the wing member 24 together with liquid, sludge, etc., and is agitated and mixed.
  • the angle ⁇ formed by the center line C and the vertical direction There is no particular lower limit value of the angle ⁇ formed by the center line C and the vertical direction. However, if the angle ⁇ is too small, the height of the spacer 14 is required and the whole becomes bulky. It is preferable that it is 30 degrees or more.
  • the injection nozzle 32 injects gas in the vertical direction in plan view toward the flat surface portion F1 of the inner surface of the flow path.
  • the increase can be promoted, and the above effect can be enhanced.
  • the plurality of blade members 24 are provided in multiple stages with different directions, so that a liquid in which gas, sludge, or the like is mixed is horizontally distributed between the blade members 24 in each stage. Ascending while turning in the vertical direction, and ejected from the upper end of the main body 10. Thus, the liquid circulates in the storage tank while the mixed gas and sludge are stirred and refined. And the amount of dissolved oxygen in water increases because the air and liquid in a storage tank circulate effectively. When aerobic microorganisms such as activated sludge are mixed in the storage tank, the microorganisms are activated by the improvement of the dissolved oxygen amount, and the decomposition of organic matter in the liquid by the microorganisms is promoted. Purification is performed.
  • the circumferential intervals between the flat portions F1 to F5 on which the upper bottom portion 241 of the wing member 24 is supported in each step are arranged so as to gradually increase from the lower step toward the upper step. 5 (see FIG. 5), the swirl direction of the liquid drawn counterclockwise in plan view from the lower end of the main body 10 is reversed in the process in which the liquid rises vigorously in the main body 10 by the injection of the injection nozzle 32 ( According to the experiments by the present inventors, when the wing members 24 are arranged in five stages, the swirling direction of the liquid is reversed between the fourth stage and the fifth stage). 10 is ejected from the upper end.
  • the lower surface 24b of the wing member 24 is preferably provided with a plurality of protrusions 24c as in the present embodiment, which can facilitate gas-liquid turbulent mixing.
  • the support body 40 has a circulation port 44 through which the liquid can pass under the main body 10, sludge or the like that has volume between the pair of base members 42, 42 passes through the circulation port 44 together with the liquid and passes through the main body 10. Be drawn into.
  • the air diffusion device 1 of the present embodiment is designed to improve the liquid drawing force, the liquid drawing force does not become insufficient even if the circulation port 44 is formed. Effective purification is possible.
  • the wing unit 20 including the wing member 24 is provided in multiple stages so that the inner surface of the main body 10 is formed by the inner peripheral surface of the frame 22, and the wing member 24 is formed on the inner surface of the flow channel.
  • each wing member 24 may be directly attached to the inner peripheral surface of the main body 10 so that the inner peripheral surface of the main body 10 becomes the inner surface of the flow path.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Water Supply & Treatment (AREA)
  • Environmental & Geological Engineering (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

【課題】　液中に放出した気体を微細化して均一な分散を図りつつ、液体を効率良く撹拌することができる散気装置を提供する。 【解決手段】　両端が開口する筒状に形成され断面五角形状の流路内面を有する本体１０と、流路内面に向きを変えて多段に設けられた翼部材２４と、本体１０の一方の開口端部に設けられた噴射ノズル３２とを備え、噴射ノズル３２が下側となるように本体１０を起立させた状態で液中に浸漬し、噴射ノズル３２から本体１０内に気体を噴射して散気する散気装置１であって、噴射ノズル３２は、先端に形成された噴射口３２ａの中心線Ｃが、最下段に配置された翼部材２４よりも下方において流路内面と交差し、且つ、鉛直方向とのなす角度が４５度以下となるように配置されている。

Description

散気装置
　本発明は、液体中に空気等の気泡を分散する散気装置に関する。
　散気装置は、下水処理場、食品工場や畜産農場における排水処理場、その他工場の排水処理設備における排水中の溶存酸素量を高め、さらに、ため池や河川、養殖池等の液中の溶存酸素量を高めることによって液の不用意な腐敗を防止する等の用途に用いられる。従来の散気装置として、本発明者らの出願による特許文献１に開示された気液混合装置が知られている。この装置は、上下が開口する五角形の気液混合筒と、気液混合筒の内部に多段に配置された衝突翼と、気液混合筒の下部に配置された気体噴出ノズルとを備えており、気体噴出ノズルから噴出した気体が衝突翼に衝突しながら気液混合筒を旋回上昇することで微細化され、液中に溶け込むように構成されている。
特許第４９０７２５８号公報
　上記の気液混合装置は、五角形の気液混合筒内に配置した衝突翼により、目詰まりの問題を生じさせることなく気泡を微細化することが可能であり、メンテナンスが容易であると共に、高い酸素溶解効率が得られる等のメリットを有する。但し、気体噴出ノズルからの気体の噴出により気液混合筒内でより効果的に旋回流を生じさせて、底部に滞留した汚泥等の引込力や撹拌力を高める点において、更に改良の余地があった。
　そこで、本発明は、液中に放出した気体を微細化して均一な分散を図りつつ、液体を効率良く撹拌することができる散気装置の提供を目的とする。
　本発明の前記目的は、両端が開口する筒状に形成され断面五角形状の流路内面を有する本体と、前記流路内面に向きを変えて多段に設けられた翼部材と、前記本体の一方の開口端部に設けられた噴射ノズルとを備え、前記噴射ノズルが下側となるように前記本体を起立させた状態で液中に浸漬し、前記噴射ノズルから前記本体内に気体を噴射して散気する散気装置であって、前記噴射ノズルは、先端に形成された噴射口の中心線が、最下段に配置された前記翼部材よりも下方において前記流路内面と交差し、且つ、鉛直方向とのなす角度が４５度以下となるように配置されている散気装置により達成される。
　この散気装置において、前記各翼部材は、平面視台形状に形成され、上底部が前記流路内面を構成する５つの平面部の１つに支持されることが好ましく、前記噴射ノズルは、最下段に配置された前記翼部材の上底部が支持された前記平面部に向けて平面視垂直方向に気体を噴射することが好ましい。前記各翼部材は、各段において上底部が支持される前記平面部同士の周方向の間隔が、下段から上段に向けて段階的に拡がるように配置されていることがより好ましい。
　また、床面に載置されて前記本体および噴射ノズルを支持する支持体を更に備えることが可能であり、前記支持体は、前記本体の下方に液体が通過可能な流通口を有することが好ましい。
　本発明によれば、液中に放出した気体を微細化して均一な分散を図りつつ、液体を効率良く撹拌することができる散気装置を提供することができる。
本発明の一実施形態に係る散気装置の正面図である。 前記散気装置の平面図である。 前記散気装置の側面図である。 前記散気装置が備える翼ユニットの斜視図である。 前記散気装置における翼ユニットの配置を説明するための要部平面図である。 前記散気装置の要部縦断面図である。 前記散気装置における噴射ノズルの配置を説明するための要部平面図である。 前記散気装置における噴射ノズルの配置を説明するための要部縦断面図である。
　以下、本発明の実施の形態について、添付図面を参照して説明する。図１から図３は、本発明の一実施形態に係る散気装置を示しており、図１は正面図、図２は平面図、図３は側面図である。図１から図３に示すように、散気装置１は、筒状の本体１０と、本体１０の内部に複数設けられた翼ユニット２０と、本体１０の下部に設けられた通気管３０と、本体１０および通気管３０を支持する支持体４０とを備えている。本体１０は、両端に開口を有し、平面視正五角形状に形成されており、例えばステンレス等の防錆効果を有する金属材料や、エンジニアリングプラスチックなどの耐水性や耐食性を有するプラスチック材料などから形成することができる。
　翼ユニット２０は、図４に斜視図で示すように、枠体２２と、枠体２２に支持される翼部材２４とを備えている。枠体２２は、外周面全体が本体１０の内周面に密着するように正五角形状に形成されており、枠体２２の内周面は、５つの平面部２２ａ，２２ｂ，２２ｃ，２２ｄ，２２ｅを連設して構成されている。翼部材２４は、平面視台形状に形成されており、上底部２４１が枠体２２の１つの平面部２２ａに支持され、斜辺部２４２，２４３が平面部２２ａの両側に隣接する他の平面部２２ｂ，２２ｅにそれぞれ支持されている。翼部材２４の上面２４ａおよび下面２４ｂは、上底部２４１から先端側となる下底部２４４に向けて先細となるようにいずれも傾斜面とされており、下面２４ｂには複数の突起２４ｃが設けられている。水平面に対する上面２４ａおよび下面２４ｂの傾斜角度は特に限定されるものではないが、例えば、上面２４ａの傾斜角度を２０～４０度、下面２４ｂの傾斜角度を１０～３０度に設定することが好ましい。翼ユニット２０は、例えば樹脂材料により一体成形することが可能である。
　上記の構成を備える複数の翼ユニット２０は、それぞれ翼部材２４の向きを変えて、図３に破線で示すように本体１０内に多段に挿入される。各翼ユニット２０の翼部材２４の向きを図５に平面図で示す。本実施形態においては、翼ユニット２０が５つ配置されており、図５（ａ）～（ｅ）は、最上段から最下段までを上から順に示している。図５（ｅ）に示すように、翼ユニット２０は、枠体２２の内部に本体１０の流路Ｆを構成しており、枠体２２の内周面によって、５つの平面部Ｆ１，Ｆ２，Ｆ３，Ｆ４，Ｆ５が反時計回りに順次連設されてなる断面正五角形状の流路内面が構成されている。最下段の翼ユニット２０は、図５（ｅ）に示すように、翼部材２４の上底部２４１を支持する平面部（以下、「支持平面部」という）が平面部Ｆ１となる向きで本体１０に挿入される。
　これに対し、下から２段目の翼ユニット２０は、図５（ｄ）に示すように、最下段の翼ユニット２０の支持平面部Ｆ１に対して反時計回りに１つ隣りの平面部が支持平面部となる向き、すなわち支持平面部が平面部Ｆ２となる向きで、本体１０に挿入される。そして、下から３段目の翼ユニット２０は、図５（ｃ）に示すように、下から２段目の翼ユニット２０の支持平面部Ｆ２に対して反時計回りに２つ隣りの平面部が支持平面部となる向き、すなわち支持平面部が平面部Ｆ４となる向きで、本体１０に挿入される。このように、最下段以外の任意の段における翼ユニット２０の支持平面部と、その１つ下段の翼ユニット２０の支持平面部との周方向の間隔が、下段から上段に向けて段階的に拡がるように構成されている。すなわち、下から４段目の翼ユニット２０の支持平面部は、図５（ｂ）に示すように、平面部Ｆ４から反時計回りに３つ隣りの平面部Ｆ２であり、最上段の翼ユニット２０の支持平面部は、図５（ａ）に示すように、平面部Ｆ２から反時計回りに４つ隣りの平面部Ｆ１である。
　図６に要部縦断面図で示すように、本体１０の下部内周面には内方に突出する係合部１２が設けられており、本体１０に対する翼ユニット２０の挿入は、正五角筒状のスペーサ１４を挿入して係合部１２に係止させた後に行われる。こうして、各翼ユニット２０は、本体１０内の所定の高さ位置に支持され、本体１０内に最後に挿入される固定リング１６により固定される。スペーサ１４の内面は、翼ユニット２０の内面と面一になって、本体１０の流路内面の一部を構成する。
　通気管３０は、図１に破線で示すように、一方端部に噴射ノズル３２が形成されている。噴射ノズル３２は、本体１０の下側の開口端部に設けられており、先端に噴射口３２ａが形成されている。通気管３０の他方端部には、ホース（図示せず）等を装着可能な装着部３４が設けられており、コンプレッサ、ブロワ、ボンベ等の給気源（図示せず）に接続することで、噴射ノズル３２の噴射口３２ａから本体１０の流路内に空気等の気体を噴射することができる。
　噴射ノズル３２は、図７に要部平面図で示すように、開口面の法線方向に延びる噴射口３２ａの中心線Ｃが、本体１０の流路内面を構成する１つの平面部Ｆ１と平面視で直交するように配置されており、平面部Ｆ１の中央に向けて平面視垂直方向に気体を噴射するように構成されている。この平面部Ｆ１は、図７に破線で示す最下段の翼ユニット２０の支持平面部である。また、噴射ノズル３２は、図８に要部縦断面図で示すように、噴射口３２ａの中心線Ｃが、最下段に配置された翼ユニット２０の翼部材２４よりも下方において本体１０の流路内面Ｓと交差するように、斜め上方に向けて配置されている。中心線Ｃと流路内面Ｓに沿った鉛直方向とのなす角度θは、４５度以下に設定される。
　支持体４０は、ステンレス等の金属薄板を折り曲げて形成することができ、図１から図３に示すように、左右の下部を折曲状に形成した一対のベース部材４２，４２が設けられている。本体１０および通気管３０は、一対のベース部材４２，４２間に支持される。ベース部４２，４２には、ビスやアンカーボルト等を挿通可能な取付孔４２ａ，４２ａが形成されており、起立状態の本体１０の下端と床面Ｆとの間に適当な間隔（例えば、１０～１５ｃｍ程度）をあけた状態で、ベース部４２，４２を床面Ｆに固定することができる。図１に示すように、支持体４０は、一対のベース部材４２，４２間において本体１０の下端よりも下方に、液体が通過可能な流通口４４が形成されている。
　次に、上記構成を備える散気装置１の作動を説明する。まず、処理対象となる排水や汚水などの液体が貯留される貯留槽等に、噴射ノズル３２が下側となるように本体１０を鉛直方向に起立させて、散気装置１を設置する。散気装置１の設置は、上記のように支持体４０のベース部４２を床面Ｆに固定して行うことが可能であるが、支持体４０を用いずに本体１０を上方から吊り下げ支持することも可能である。貯留槽等には、活性汚泥などの好気性の微生物を混入するようにしてもよい。
　そして、本体１０が液中に浸漬された状態で、通気管３０に接続された給気源（図示せず）から圧縮空気等を供給し、噴射ノズル３２から本体１０の流路内に気体を噴射して散気すると、エジェクタ効果によって本体１０の下端から液体が引き込まれ、噴射した気体と共に上昇する。床面Ｆに汚泥等が堆積している場合には、この汚泥等も撹拌により液体と混合されて、本体１０内に導入される。
　噴射ノズル３２は、図８に示すように、噴射口３２ａの中心線Ｃが、最下段の翼部材２４よりも下方において流路内面Ｓと交差するように配置されており、更に、鉛直方向となす角度θが鉛直上方に近づくように４５度以下に設定されている。したがって、噴射した気体は、翼部材２４の下面２４ｂと衝突して下方に反射するおそれがなく、また、噴射方向が水平に近いことで十分な上昇力が得られないという問題も生じることがないので、最下段の翼部材２４まで流路内面Ｓに沿ってスムーズに上昇し、液体や汚泥等と共に翼部材２４の下面２４ｂに衝突して撹拌・混合される。この結果、噴射した気体による液体や汚泥等の引込力や撹拌力を向上させることができる。中心線Ｃと鉛直方向とのなす角度θの下限値は特に存在しないが、角度θが小さすぎるとスペーサ１４の高さが必要になり全体として嵩高になることから、例えば、１５度以上であることが好ましく、３０度以上であることがより好ましい。
　また、噴射ノズル３２は、図７に示すように、流路内面の平面部Ｆ１に向けて平面視垂直方向に気体を噴射するため、この構成からも流路内面Ｓに沿った気体のスムーズな上昇を促すことができ、上記の効果を高めることができる。
　本体１０内の流路においては、複数の翼部材２４がそれぞれ向きを変えて多段に設けられているため、気体や汚泥等が混合された液体が、各段における翼部材２４の間で水平方向および垂直方向に旋回しながら上昇し、本体１０の上端から噴出する。こうして、混合された気体や汚泥の撹拌、微細化が行われながら液体が貯留槽内を循環する。そして、貯留槽内の空気と液体が効果的に循環することによって水中の溶存酸素量が高まる。貯留槽内に活性汚泥などの好気性の微生物が混入されている場合、当該溶存酸素量の向上によって微生物が活性化し、微生物による液中の有機物などの分解が促進されることとなり、貯留槽内の浄化が行われる。
　特に、本実施形態においては、各段において翼部材２４の上底部２４１が支持される平面部Ｆ１～Ｆ５同士の周方向の間隔が、下段から上段に向けて段階的に拡がるように配置されているため（図５参照）、本体１０の下端から平面視で反時計回りに引き込まれた液体の旋回方向が、噴射ノズル３２の噴射により本体１０内を液体が勢いよく上昇する過程で反転され（本発明者らの実験によれば、翼部材２４を５段に配置した場合に、４段目と５段目との間で液体の旋回方向が反転する）、平面視時計回りとなって本体１０の上端から噴出する。このような反転作用によって気体や汚泥の微細化や撹拌が促されるので、浄化等を効率良く行うことができる。翼部材２４の下面２４ｂには、本実施形態のように複数の突起２４ｃが設けられていることが好ましく、これによって気液の乱流混合を生じ易くすることができる。
　また、支持体４０は、本体１０の下方に液体が通過可能な流通口４４を有するため、一対のベース部材４２，４２間に体積した汚泥等が、液体と共に流通口４４を通過して本体１０に引き込まれる。上記のように、本実施形態の散気装置１は、液体の引込力の向上が図られているため、流通口４４を形成しても液体の引込力が不十分になるおそれがなく、より効果的な浄化が可能である。
　以上、本発明の一実施形態について詳述したが、本発明の具体的な態様は上記実施形態に限定されるものではない。例えば、本実施形態においては、翼部材２４を備える翼ユニット２０を多段に設けることで、枠体２２の内周面により本体１０の流路内面を形成し、この流路内面に翼部材２４を設けた構成にしているが、各翼部材２４を本体１０の内周面に直接取り付けて、本体１０の内周面を流路内面にすることもできる。
　１　散気装置
１０　本体
２０　翼ユニット
２４　翼部材
２４１　上底部
３０　通気管
３２　噴射ノズル
３２ａ　噴射口
４０　支持体
４４　流通口
　Ｃ　中心線
Ｆ１～Ｆ５　平面部

Claims (4)

  1. 　両端が開口する筒状に形成され断面五角形状の流路内面を有する本体と、
    　前記流路内面に向きを変えて多段に設けられた翼部材と、
    　前記本体の一方の開口端部に設けられた噴射ノズルとを備え、
    　前記噴射ノズルが下側となるように前記本体を起立させた状態で液中に浸漬し、前記噴射ノズルから前記本体内に気体を噴射して散気する散気装置であって、
    　前記噴射ノズルは、先端に形成された噴射口の中心線が、最下段に配置された前記翼部材よりも下方において前記流路内面と交差し、且つ、鉛直方向とのなす角度が４５度以下となるように配置されている散気装置。
  2. 　前記各翼部材は、平面視台形状に形成され、上底部が前記流路内面を構成する５つの平面部の１つに支持されており、
    　前記噴射ノズルは、最下段に配置された前記翼部材の上底部が支持された前記平面部に向けて平面視垂直方向に気体を噴射する請求項１に記載の散気装置。
  3. 　前記各翼部材は、各段において上底部が支持される前記平面部同士の周方向の間隔が、下段から上段に向けて段階的に拡がるように配置されている請求項２に記載の散気装置。
  4. 　床面に載置されて前記本体および噴射ノズルを支持する支持体を更に備え、
    　前記支持体は、前記本体の下方に液体が通過可能な流通口を有する請求項１に記載の散気装置。
PCT/JP2013/063358 2012-05-21 2013-05-14 散気装置 WO2013175994A1 (ja)

Priority Applications (6)

Application Number Priority Date Filing Date Title
IN2744KON2014 IN2014KN02744A (ja) 2012-05-21 2013-05-14
EP13794303.1A EP2853308B1 (en) 2012-05-21 2013-05-14 Aeration equipment
US14/402,149 US9446357B2 (en) 2012-05-21 2013-05-14 Aeration equipment
KR1020147033356A KR101638782B1 (ko) 2012-05-21 2013-05-14 산기장치
CN201380026690.1A CN104321134B (zh) 2012-05-21 2013-05-14 气体分散装置
CA2872601A CA2872601C (en) 2012-05-21 2013-05-14 Aeration equipment

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2012115201A JP5835776B2 (ja) 2012-05-21 2012-05-21 散気装置
JP2012-115201 2012-05-21

Publications (1)

Publication Number Publication Date
WO2013175994A1 true WO2013175994A1 (ja) 2013-11-28

Family

ID=49623688

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2013/063358 WO2013175994A1 (ja) 2012-05-21 2013-05-14 散気装置

Country Status (9)

Country Link
US (1) US9446357B2 (ja)
EP (1) EP2853308B1 (ja)
JP (1) JP5835776B2 (ja)
KR (1) KR101638782B1 (ja)
CN (1) CN104321134B (ja)
CA (1) CA2872601C (ja)
IN (1) IN2014KN02744A (ja)
MY (1) MY168890A (ja)
WO (1) WO2013175994A1 (ja)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102092499B1 (ko) * 2019-01-15 2020-03-23 주식회사 승일 과압해소가 가능한 분사용기 및 그의 밸브 어셈블리
KR102201783B1 (ko) 2020-07-21 2021-01-12 신상곤 산기장치
CN113304684B (zh) * 2021-06-02 2022-06-07 浙江大学 一种设置内套筒的连续流好氧颗粒污泥反应装置及方法
KR102562233B1 (ko) 2022-03-07 2023-08-02 주식회사 한국환경기술 회전체가 구비된 산기장치

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0641898U (ja) * 1992-09-22 1994-06-03 充弘 藤原 空気混合式流体攪拌装置
JPH08192035A (ja) * 1995-01-19 1996-07-30 Chem Grouting Co Ltd 微細気泡を発生する方法及び装置
JP2007038067A (ja) * 2005-08-01 2007-02-15 Noritake Co Ltd 流体混合装置及び流体混合方法
JP2007289915A (ja) * 2006-03-27 2007-11-08 Yasuhiko Masuda 気液混合装置
JP2008212908A (ja) * 2006-03-10 2008-09-18 Osaka Gas Engineering Co Ltd 気液混合吹き出しノズル

Family Cites Families (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3148509A (en) * 1960-10-24 1964-09-15 Pneumatic Breakwaters Ltd Wave reduction, de-icing and destratification apparatus
US3452966A (en) * 1967-08-24 1969-07-01 Polcon Corp Liquid treatment apparatus and method
GB1254179A (en) * 1969-02-05 1971-11-17 Polcon Corp Liquid treatment apparatus and method
US3969446A (en) * 1974-06-03 1976-07-13 Franklin Jr Grover C Apparatus and method for aerating liquids
JPS552410U (ja) * 1978-06-20 1980-01-09
JPS5895293U (ja) * 1981-12-21 1983-06-28 斉藤　晃四郎 間欠式旋回流空気揚水装置
JP2979741B2 (ja) 1991-06-13 1999-11-15 荒川化学工業株式会社 製紙用添加剤の製造法
JPH05146792A (ja) * 1991-11-27 1993-06-15 Oshima Koki Kk 排水処理装置
WO1997022562A1 (en) * 1995-12-05 1997-06-26 Inglewood Technologies Pty. Ltd. An aeration device
JP3121271B2 (ja) * 1996-10-16 2000-12-25 チュラルテック株式会社 エアレータ
TR200000936T1 (tr) * 1998-08-11 2000-11-21 Mitsubishi Heavy Industries, Ltd. Egzoz gazını kükürtten arıtmak için ıslak gaz kükürtten arıtma düzeneği.
ATE299392T1 (de) * 1999-04-19 2005-07-15 Sulzer Chemtech Ag Statischer wirbelmischer und methode zur verwendung desselben
JP4328904B2 (ja) * 1999-08-26 2009-09-09 株式会社オーエイチ・アール 気液混合装置
JP4309021B2 (ja) * 2000-05-10 2009-08-05 鈴木産業株式会社 排水処理システム
EP1358928A4 (en) * 2001-02-05 2007-01-10 Ohr Co Ltd THE FLOWING POWER OF INTERNAL FLUID-RECEIVING SUPPORT STRUCTURE AND MOUNTING FOR ONE-PIP DRIPPER
US7008644B2 (en) * 2002-03-20 2006-03-07 Advanced Inhalation Research, Inc. Method and apparatus for producing dry particles
AU2003277531A1 (en) * 2003-10-29 2005-05-11 Anemos Company Ltd. Air diffusing device
JP2005144425A (ja) * 2003-11-14 2005-06-09 Anemosu:Kk 散気処理装置
WO2007110972A1 (ja) * 2006-03-27 2007-10-04 Yasuhiko Masuda 気液混合装置
JP4749961B2 (ja) * 2006-07-12 2011-08-17 株式会社アイエンス 気泡発生装置
JP2008086937A (ja) * 2006-10-03 2008-04-17 Anemosu:Kk 流体混合器、流体混合装置及びノズル部材
WO2008139728A1 (ja) * 2007-05-11 2008-11-20 Seika Corporation 気液混合循環装置
DE102012005472A1 (de) * 2012-03-17 2013-09-19 Arnold Jäger Holding GmbH Vorrichtung zum Belüften von Wasser, insbesondere Abwasser

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0641898U (ja) * 1992-09-22 1994-06-03 充弘 藤原 空気混合式流体攪拌装置
JPH08192035A (ja) * 1995-01-19 1996-07-30 Chem Grouting Co Ltd 微細気泡を発生する方法及び装置
JP2007038067A (ja) * 2005-08-01 2007-02-15 Noritake Co Ltd 流体混合装置及び流体混合方法
JP2008212908A (ja) * 2006-03-10 2008-09-18 Osaka Gas Engineering Co Ltd 気液混合吹き出しノズル
JP2007289915A (ja) * 2006-03-27 2007-11-08 Yasuhiko Masuda 気液混合装置
JP4907258B2 (ja) 2006-03-27 2012-03-28 泰彦 増田 気液混合装置

Also Published As

Publication number Publication date
CA2872601C (en) 2016-08-02
US20150306551A1 (en) 2015-10-29
EP2853308A1 (en) 2015-04-01
KR101638782B1 (ko) 2016-07-12
IN2014KN02744A (ja) 2015-05-08
CN104321134A (zh) 2015-01-28
US9446357B2 (en) 2016-09-20
KR20150008425A (ko) 2015-01-22
JP5835776B2 (ja) 2015-12-24
JP2013240748A (ja) 2013-12-05
CA2872601A1 (en) 2013-11-28
EP2853308A4 (en) 2016-01-13
CN104321134B (zh) 2018-01-30
EP2853308B1 (en) 2018-08-08
MY168890A (en) 2018-12-04

Similar Documents

Publication Publication Date Title
KR101730031B1 (ko) 아토마이징 장치
US8002246B2 (en) Aeration apparatus
WO2013175994A1 (ja) 散気装置
KR100352166B1 (ko) 기체의 효율적 용해와 슬러지 교반을 위한 방법 및 장치
US8128070B1 (en) Venturi aeration circulation system
JP4706665B2 (ja) 微細気泡発生装置
JP3747261B2 (ja) 気液混合流体の分散方法及び該方法に使用する分散装置
JP2007289915A (ja) 気液混合装置
JP2007313464A (ja) 気体溶解装置
JP6345546B2 (ja) 省動力型曝気撹拌装置
KR20240044052A (ko) 폐수처리시설의 미세기포산기장치
JP3762771B2 (ja) 曝気槽の消泡装置及び消泡方法
US10857506B2 (en) Gas dissolution accelerating device
KR102601504B1 (ko) 산기 장치
KR102562116B1 (ko) 미세기포를 이용한 고도산화장치 및 이를 구비하는 고농도 유기성 수처리시스템
KR100589219B1 (ko) 산기장치 및 이를 적용한 폭기 시스템
CN210505782U (zh) 一种用于处理黑臭水体的曝气结构
JP6604676B1 (ja) 導水路装置
KR101604462B1 (ko) 산소 용해기
KR101306905B1 (ko) 가축분뇨를 이용한 양액 제조장치
JP2023033626A (ja) 攪拌槽
JP2012232226A (ja) 気泡排出装置
KR20230061667A (ko) 폐수 및 오수 처리용 산기장치
KR20230153804A (ko) 급속 공기 산화 장치
JP2020062621A (ja) 攪拌槽

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 13794303

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2872601

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 14402149

Country of ref document: US

WWE Wipo information: entry into national phase

Ref document number: IDP00201407196

Country of ref document: ID

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 20147033356

Country of ref document: KR

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 2013794303

Country of ref document: EP