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WO2010076843A1 - Microbubble generation device - Google Patents

Microbubble generation device Download PDF

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Publication number
WO2010076843A1
WO2010076843A1 PCT/JP2008/073879 JP2008073879W WO2010076843A1 WO 2010076843 A1 WO2010076843 A1 WO 2010076843A1 JP 2008073879 W JP2008073879 W JP 2008073879W WO 2010076843 A1 WO2010076843 A1 WO 2010076843A1
Authority
WO
WIPO (PCT)
Prior art keywords
introduction
gas
liquid
mixing
unit
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.)
Ceased
Application number
PCT/JP2008/073879
Other languages
French (fr)
Japanese (ja)
Inventor
祥規 久保田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
RYNCOSMOS LLC
Original Assignee
RYNCOSMOS LLC
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 RYNCOSMOS LLC filed Critical RYNCOSMOS LLC
Priority to PCT/JP2008/073879 priority Critical patent/WO2010076843A1/en
Priority to PCT/US2009/069844 priority patent/WO2010078442A2/en
Publication of WO2010076843A1 publication Critical patent/WO2010076843A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4316Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor the baffles being flat pieces of material, e.g. intermeshing, fixed to the wall or fixed on a central rod
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20Mixing gases with liquids
    • B01F23/23Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • B01F23/23231Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits being at least partially immersed in the liquid, e.g. in a closed circuit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3121Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31241Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the circumferential area of the venturi, creating an aspiration in the central part of the conduit
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30Injector mixers
    • B01F25/31Injector mixers in conduits or tubes through which the main component flows
    • B01F25/313Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
    • B01F25/3131Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4314Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor with helical baffles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/4317Profiled elements, e.g. profiled blades, bars, pillars, columns or chevrons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/42Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
    • B01F25/43Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
    • B01F25/431Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor
    • B01F25/43197Straight mixing tubes with baffles or obstructions that do not cause substantial pressure drop; Baffles therefor characterised by the mounting of the baffles or obstructions
    • B01F25/431972Mounted on an axial support member, e.g. a rod or bar

Definitions

  • the present invention relates to an apparatus for making a gas having a pressure higher than that of the atmosphere into fine bubbles and releasing it into a liquid.
  • Patent Document 1 proposes a prior art including a casing, a liquid supply cylinder that introduces liquid into the casing, and a gas supply cylinder that introduces gas.
  • the liquid supplied from the liquid supply cylinder into the casing is swung, and the liquid supplied into the casing is swirled in the casing, whereby a negative pressure is generated near the center by the centrifugal force of swirling. generate.
  • An object of the present invention is to solve the above-mentioned problems.
  • a gas having a pressure higher than atmospheric pressure an apparatus capable of making the gas into fine bubbles and releasing it into a liquid is provided. Is to provide.
  • the technical means made by the present invention in order to achieve the above object is a fine bubble generating device that discharges compressed gas into fine bubbles and discharges it into the liquid, and introduces the pressurized gas into the gas introduction unit.
  • Is provided on one end side is disposed in the liquid, and has a cylindrical introduction pipe provided on the other end side with a discharge portion that discharges the introduced gas into the liquid, and introduces the liquid into the introduction pipe
  • the microbubble generator is characterized in that it is provided with a collision plate that is disposed between the units and that collides with the gas mixed in the mixing unit and the liquid.
  • the liquid introduction part is composed of a hole penetrating from the outer surface to the inner surface of the introduction pipe, and an introduction part that is arranged in the introduction pipe so as to communicate with the hole and that is opened at a position closer to the mixing part than the hole.
  • the liquid may be taken into the introduction pipe from the introduction portion by a negative pressure generated when the gas passes through the introduction pipe.
  • the mixing unit is provided between a plurality of blade members that are divided into a region on the liquid introduction unit side and a region on the discharge unit side, and between each of the blade members, and the region on the liquid introduction unit side and the discharge unit side And a mixing path that communicates with the area of the liquid introduction section.
  • the mixing path has a narrower cross-sectional area than the cross-sectional area of the introduction pipe on the liquid introduction section side, or the area on the liquid introduction section side and the discharge section side.
  • the cross-sectional area may be narrower than the cross-sectional area of the introduction pipe on the liquid introduction part side. In these cases, the gas and liquid introduced into the introduction pipe are efficiently mixed when passing through the mixing path having a narrow cross-sectional area.
  • the fine bubble generating device may include a gas intake unit that takes in gas outside the introduction tube between the mixing unit and the discharge unit in the introduction tube, or the gas introduction of the introduction tube is introduced into the introduction tube.
  • a gas introduction cylinder having a length extending from the discharge section to the discharge section is internally provided, and the gas introduction cylinder has a gas intake section at the same end as the gas introduction section side of the introduction pipe, and the discharge section side of the introduction pipe; Formed into a thin cylinder having a second discharge part at the same end, forming a gas introduction space extending from the gas introduction part to the discharge part between the outer surface of the gas introduction cylinder and the inner surface of the introduction tube, and mixing
  • the portion may be disposed in a gas introduction space between the outer surface of the gas introduction tube and the inner surface of the introduction tube, and the second discharge portion may be opened between the mixing portion and the collision plate.
  • the present invention by introducing a gas having a pressure higher than the atmospheric pressure, it is possible to provide a device that can make the gas into fine bubbles and discharge it into the liquid.
  • the exhaust gas (gas) forcedly fed by an air conditioner from an industrial machine or the like at a high pressure from the atmosphere is made into fine bubbles and discharged into water (liquid).
  • the gas that the fine bubble generating device makes fine bubbles may be any gas as long as it is pumped at a higher pressure than the atmosphere, and the liquid that is released as fine bubbles is also selected. It may be a liquid
  • the exhaust gas is efficiently filtered in water, or a chemical manufacturing apparatus.
  • the intermediate purified gas is discharged into the solution to cause an efficient chemical reaction, or a large amount of air is dissolved in water to prevent water pollution in rivers and lakes.
  • the fine bubble generating device 1 is provided with a gas introduction part 2 for introducing a pumped gas on one end 11 side (upstream side) and disposed in a liquid.
  • a discharge part 70 for releasing the gas introduced by the gas introduction part 20 into the liquid is provided with a cylindrical introduction pipe 10 provided on the other end 12 side (downstream side), and the liquid is introduced into the introduction pipe 10.
  • the gas introduction unit 20 is provided as an opening of one end 11 of the introduction pipe 10 (the free end of the first member 13), and introduces gas into the introduction pipe 10.
  • a pressure feed pipe (not shown) that conveys the gas discharged from the air conditioner is directly connected to the gas introduction unit 20, or the pressure feed pipe is connected by a relay pipe, so that the pressure feed pipe has a higher pressure than the atmosphere.
  • the gas sent out from is introduced into the introduction pipe 10 from the gas introduction part 20.
  • the discharge part 70 is provided as an opening at the other end 12 of the introduction tube 10 as shown in FIGS. 2, 3, and 5.
  • the discharge part 70 is disposed in the liquid and is supplied from the discharge part 70 to the gas introduction part 20.
  • the gas introduced from is turned into fine bubbles and released into the liquid.
  • the introduction pipe 10 of the first embodiment is provided with a circular tubular first member 13 having both ends open and the first member 13 in communication with each other, and both ends are open.
  • the second member 14 is formed in a tubular shape, and the third member is provided in communication with the second member 14 and is open at both ends. Therefore, according to the present embodiment, a circular channel having an internal space communicating from the first member to the third member is formed, and the opening on the free end side of the first member serves as the gas introduction portion 20.
  • the opening on the free end side of the three members is a discharge portion 70.
  • the first member 13 is formed in a linear shape having a shaft 13b in the horizontal direction.
  • the second member 14 is formed in a straight line having an axis 14b that intersects the axis 13b of the first member 13 at a right angle in the vertical direction.
  • the third member 15 is formed in a straight line having an axis 15 b that intersects the axis 14 b of the second member 14 at a right angle and is parallel to the axis 13 b of the first member 13.
  • the introduction pipe 10 has a so-called crank shape as shown in FIG.
  • the introduction tube 10 of the present embodiment is formed in a cylindrical shape having the same inner diameter.
  • the inner diameter of the introduction tube 10 is set to 60 mm.
  • the introduction pipe 10 has an upper portion of the first member 13 and the second member 14 positioned above the liquid surface W of the liquid, and a lower portion of the second member 14.
  • the third member 15 is installed so as to be immersed below the liquid surface W of the liquid.
  • the other end 12 of the introduction tube 10, that is, the discharge portion 70 provided at the end of the third member 15 is arranged so as to be immersed in the liquid.
  • the first member 13, the second member 14, and the third member 15 each formed in a circular tube shape are integrally connected in a crank shape to constitute the outer shape of the introduction tube 10.
  • the outer shape of the introduction tube 10 is not limited to the above shape.
  • the first member 13, the second member 14, and the third member 15 may be integrally connected in a straight line to constitute the introduction tube 10.
  • the first member 13, the second member 14, and the third member 15 may be formed in an S shape.
  • the introduction pipe 10 is configured by three members in the present embodiment, the number of components may be two or four or more, and is not limited.
  • the inner diameter of the introduction tube 10 is not limited to the above numerical setting, and may be set freely according to demands such as the purpose of use and usage environment of the fine bubble generating device 1. In this case, the inner diameter of the introduction tube 10 is not constant from the one end 11 to the other end 12 but may be changed by setting a portion having a large diameter or a small diameter.
  • the cross-sectional shape of the introduction tube 10 is circular, but the present invention is not limited to this, and the cross-sectional shape of other shapes may be provided as long as the introduction tube 10 is formed in a tubular shape. .
  • a rectangular cross-sectional shape may be used.
  • the liquid introduction part 30 is arranged on the upstream side of the mixing part described later, and communicates with the hole 31 penetrating from the outer surface to the inner surface of the introduction pipe 10.
  • an introduction part 32 arranged in the introduction pipe 10.
  • the hole 31 is on the gas introduction part 20 side of the second member 14, and at a position where the second member 14 is submerged in the liquid when the microbubble generator 1 is installed. It is formed so as to penetrate from the outer surface to the inner surface of (introducing tube 10).
  • the hole diameter of the hole 31 is set to 21 mm.
  • the hole diameter of the hole 31 is not limited to this, and may be set freely according to the demand for the amount of liquid introduced into the introduction tube 10.
  • the introduction part 32 is connected to the hole 31 without a gap, and intersects the axis 14 b of the second member 14 from the hole 31 to the inner space of the second member 14 at a right angle.
  • a hollow cylindrical first cylindrical portion 34a provided to project, and a hollow cylindrical shape that communicates with the first cylindrical portion 34a and that is disposed in parallel with the shaft 14b toward the downstream side (downward in the drawing).
  • the second cylindrical portion 34b is provided, and an opening 33 is provided on the free end side of the second cylindrical portion 34b.
  • the introduction part 32 is arranged so that the opening 33 is closer to the mixing part 40 described later than the hole 31.
  • the second cylindrical portion 34 b is formed so that the opening 33 is positioned near the shaft 15 b of the third member 15. Accordingly, when the gas passes through the introduction pipe 10, the pressure around the liquid introduction portion 30 becomes negative due to the flow velocity, so that the liquid outside the introduction pipe 10 is introduced into the second member 14 (introduction from the hole 31. The air is drawn into the inner space of the pipe 10) and discharged from the opening 33 on the downstream side of the hole 31 into the inner space of the introduction pipe 10.
  • the opening 33 is formed so as to be positioned near the shaft 15b of the third member 15, and the opening 33 opens near the shaft 15b, so that the liquid introduced into the introduction pipe 10 Is pulled by a gas stream sent in the direction of the mixing unit 40, which will be described later, and proceeds in the direction of the mixing unit 40 efficiently.
  • the liquid introduction unit 30 is not construed as being limited to the configuration described in the present embodiment, and can be changed in design within the scope of the present invention. Further, in the present embodiment, one embodiment in which the hole 31 is provided at a predetermined position of the second member 14 that is submerged in the liquid is described. However, the hole 31 is located outside the liquid. It may be a form. That is, as long as the outer pipe (not shown) arranged in the liquid is connected to the hole 31 located outside the liquid, the same effects as the present invention can be achieved. The outer pipe is required to have a length that allows the liquid to be drawn into the introduction pipe 10 by the negative pressure generated in the introduction pipe 10.
  • the mixing unit 40 is formed in a propeller shape with three blade members 42 a, 42 b, 42 c, and the blade members 42 a, 42 b, 42 c are connected by a connecting member 53, respectively.
  • the connecting member 53 includes a hollow inner region 53 a in which one surface (a surface that becomes a so-called triangular pyramid-shaped bottom surface) is a triangular opening 53 e.
  • the introduction pipe is formed such that the axis connecting the opening 53e and the apex 55a of the triangular pyramid facing the opening 53e is the same as the axis 15b of the third member 15. 10 is arranged in the center of the cross-sectional direction.
  • the opening 53 e of the connecting member 53 is located closest to the discharge unit 70 of the mixing unit 40.
  • the blade members 42a, 42b, and 42c are inclined surfaces (opening portions from the apex 55a of the triangular pyramid to the bottom surface) except for the opening 53e of the connecting member 53.
  • 53c, 53d, and 53e (inclined toward 53e) and the inner surface of the third member 15 are arranged in a substantially fan shape.
  • the blade member 42a has a surface 53c extending from a triangular vertex 55b of the opening 53e to a position 45a that is a predetermined distance away from the other vertex 55c on the side 43a connecting the other vertex 55c of the triangle and the vertex 55a of the triangular pyramid.
  • the base end portion 44a is integrally fixed to the base member 44, and the base end portion 44a and the inner surface of the third member 15 are formed with a rising portion 46a formed in an expanded shape.
  • the upper end of the rising portion 46 a is formed in the same arc shape as the inner surface of the third member 15 and is fixed integrally with the inner surface of the third member 15. That is, the blade member 42 a has a shape of an inclined blade to which an inclination is added when viewed in the radial direction of the third member 15.
  • the blade member 42b has a surface 53d extending from a triangular vertex 55c of the opening 53e to a position 45b that is a predetermined distance away from the other vertex 55d on the side 43b connecting the other vertex 55d of the triangle and the vertex 55a of the triangular pyramid.
  • a base end portion 44b fixed integrally with the base end portion 44b, and a rising portion 46b formed between the base end portion 44b and the inner surface of the third member 15 so as to expand.
  • the upper end of the rising portion 46 b is formed in the same arc shape as the inner surface of the third member 15 and is fixed integrally with the inner surface of the third member 15.
  • the blade member 42 b has a shape of an inclined blade to which an inclination is added as viewed in the radial direction of the third member 15.
  • the blade member 42c has a surface 53e extending from a triangular vertex 55d of the opening 53e to a position 45c at a predetermined distance from the other vertex 55b on the side 43c connecting the other vertex 55b of the triangle and the vertex 55a of the triangular pyramid.
  • the base end portion 44c is integrally fixed to the base member 44, and the base end portion 44c and the inner surface of the third member 15 are provided with a rising portion 46c formed in an expanded shape.
  • the upper end of the rising portion 46 c is formed in the same arc shape as the inner surface of the third member 15 and is fixed integrally with the inner surface of the third member 15. That is, the blade member 42c has a shape of an inclined blade to which an inclination is added in the radial view of the third member 15.
  • the blade members 42a, 42b, 42c formed in this way are adjacent to each other between the blade members 42a and 42b, 42b and 42c, and 42c and 42a, respectively.
  • overlapping regions that are separated from each other by a predetermined distance are formed, and in each of the overlapping regions, the mixing paths 41a, 41b, and 41c that respectively connect the region on the liquid introduction unit 30 side and the region on the discharge unit 70 side. Is formed. Accordingly, with the above-described configuration, the liquid mixture that has reached the mixing unit 40 passes only through the mixing paths 41a, 41b, and 41c, and is located upstream of the mixing unit 40 (on the liquid introduction unit 30 side with the mixing unit 40 as a boundary). ) And the downstream area (area on the discharge section 70 side of the mixing section 40).
  • the mixing paths 41a, 41b, and 41c have a cross-sectional area that is narrower than the cross-sectional area of the introduction pipe 10 on the liquid introduction part 30 side. Thereby, the liquid mixture in which the gas introduced from the gas introduction part 20 and the liquid introduced from the liquid introduction part 30 coexist along the inclination of the three surfaces 53c, 53d, and 53e of the connecting member 53.
  • the third member 15 is gradually guided in the direction toward the inner surface side of the third member 15, and the flow rate becomes faster when passing through the mixing paths 41a, 41b, 41c. A spiral turning motion along the axis of.
  • the connecting member 53 is formed in a triangular pyramid shape.
  • the shape of the connecting member 53 is not limited to this, and the flow resistance in the inner region of the introduction pipe 10 is not limited thereto.
  • Other shapes may be used as long as a shape that is difficult to form is employed.
  • it may be formed in a shell-shaped conical shape, and the bottom of the conical shape may be an opening.
  • the connecting member 53 is not an essential constituent element in the present invention, but only the blade members 42a, 42b, and 42c. It may be configured.
  • the blade member structure mentioned above it is not limited to this and a design change is possible within the scope of the present invention.
  • the embodiment in which the base end portions 44a, 44b, and 44c are provided from the respective triangular vertices 55b, 55c, and 55d of the opening 53e has been described, but from a position away from each of the vertices 55b, 55c, and 55d. Even the provided form is within the scope of the present invention.
  • the base end portions 44a, 44b, and 44c may be provided in parallel with the triangular sides of the opening 53e.
  • the mixing paths 41a, 41b, and 41c through which the mixed liquid passes are introduced pipes
  • the configuration is not particularly limited as long as a configuration having a cross-sectional area narrower than 10 is adopted.
  • the gas intake unit 50 includes a tube 52 that introduces a gas from the outside of the introduction tube 10 and takes it closer to the discharge unit 70 than the mixing unit 40.
  • the tube 52 intersects the shaft 15b of the third member 15 at a right angle from the connecting member 53 of the mixing unit 40 through a through hole 54 provided in the upper portion of the third member 15, and one end of the tube 52
  • the opening 52c of 52a is arranged so as to be positioned above the liquid surface W of the liquid.
  • the other end 52b of the tube 52 is inserted into the internal region of the third member 15 through the through hole 54, and the opening 52d of the other end 52b is formed as a blade member. It communicates with the hollow inner region 53a of the connecting member 53 on the upstream side (the liquid introduction part 30 side) with respect to 42a, 42b, and 42c.
  • the through hole 54 is formed to have a diameter slightly larger than the outer diameter of the tube 52, the gap between the through hole 54 and the tube 52 is closed, so that the third member extends from the through hole 54.
  • the liquid outside 15 does not enter the inner region of the third member 15.
  • the gas outside the introduction pipe 10 is introduced from one end 52a of the pipe 52, and taken into the internal region 53a of the connecting member 53 from the other end 53b.
  • the opening 53 e of the connecting member 53 is positioned closest to the discharge unit 70 of the mixing unit 40, the gas outside the introduction pipe 10 is taken closer to the discharge unit 70 than the mixing unit 40. become.
  • an air pump (not shown) is connected to one end 52a of the pipe 52 of the gas intake unit 50, and outside air is forcibly introduced from the air pump. Therefore, the amount of gas discharged from the connecting member 53 of the gas intake unit 50 can be changed according to the operating amount of the air pump.
  • the outer diameter of the pipe 52 of this embodiment is set to 6 mm, and the inner diameter is set to 4 mm.
  • the outer diameter and inner diameter of the pipe 52 are not limited to this, and may be set freely according to the demand for the amount of gas introduced outside the introduction pipe 10.
  • a swirl of the mixed liquid is formed by the mixing unit 40 along the shaft 15 b of the third member 15, and is taken in from the gas intake unit 50 at a substantially central portion of the swirl.
  • the gas discharged from the opening 53b of the connecting member 53 joins.
  • the pressure in the substantially central portion of the spiral is lower than that in the outer diameter side portion of the spiral, and the gas in the gas introduction unit 20 is higher than the atmospheric pressure.
  • the gas from the gas intake unit 50 is efficiently sucked into the introduction pipe 10 without the mixed liquid flowing backward. And the gas from the gas taking-in part 50 becomes a fine bubble by repeating a turning motion with the liquid mixture in which the gas and the liquid were mixed.
  • the collision plate 60 is a plate disposed between the mixing unit 40 and the discharge unit 70, and extends from the inner surface of the introduction tube 10 along the axis 15 b of the third member 15. It is extended.
  • the collision plate 60 is raised from the lower inner surface of the third member 15 toward the shaft 15b to a height that is half the inner diameter of the introduction tube 10, and the upstream side of the collision plate 60 is It is formed in an arc shape.
  • the swirled mixed liquid takes in the gas from the gas take-in portion 50 and collides with the collision plate 60 as a swirl while continuing swirling. At this time, relatively large bubbles that did not become fine bubbles when passing through the mixing unit 40 and gas from the gas intake unit 50 are sheared to become fine bubbles.
  • the flow in the swirling direction of the mixed liquid is rectified by the collision plate 60 into a flow in a direction in which the mixed liquid is discharged into the liquid.
  • the gas introduced into the introduction pipe 10 from the gas introduction part 20 causes the liquid outside the introduction pipe 10 to enter the introduction pipe 10 due to the negative pressure when passing through the liquid introduction part 30.
  • the gas introduced into the introduction pipe 10 and the liquid introduced from the liquid introduction part 30 are efficiently mixed when passing through the mixing paths 41a, 41b, 41c of the mixing part 40.
  • the gas and the liquid mixed through the mixing unit 40 collide with the collision plate 60 while forming fine bubbles, thereby generating a large amount of fine bubbles (microbubbles) and releasing them into the liquid.
  • the amount of fine bubbles can be increased by additionally introducing outside air from the gas intake unit 50.
  • the fine bubble generating device 1 is economical because it does not need to pump the liquid into the casing (inside the device) when generating fine bubbles.
  • the exhaust from a factory or internal combustion engine can be dissolved in liquid and purified, or the biological or chemical of gas and liquid This is suitable for promoting a typical reaction.
  • the configuration in which the liquid introduction unit 30 is disposed at a position where the liquid introduction unit 30 is submerged in the liquid has been described, but the liquid introduction unit 30 is not submerged in the liquid and is positioned above the liquid surface W of the liquid. It can also be set as the structure arranged so.
  • the liquid is supplied to the hole 31, such as providing an introduction tube that extends from the hole 31 of the liquid introduction part 30 without a gap and whose tip side is submerged in the liquid. Just do it.
  • the configuration including the gas intake unit 50 has been described.
  • the configuration is not limited thereto, and a configuration without the gas intake unit 50 may be used.
  • only the pressurized gas from the gas introduction unit 20 is introduced into the introduction pipe 10, and thus the fine bubbles released from the discharge unit 70 include gas. Since only the pressurized gas from the introduction part 20 is included and the gas outside the introduction pipe 10 is not included, it may be selected according to the demand for generating fine bubbles of only the pressurized gas from the gas introduction part 20. .
  • the gas introduction unit 20 for introducing the pumped gas is provided on the one end 11 side (upstream side), and the gas introduced into the liquid is introduced in the gas introduction unit 20.
  • a cylindrical introduction pipe 10 provided with a discharge part 70 for discharging the liquid into the other end 12 (downstream side), a liquid introduction part 30 for introducing the liquid into the introduction pipe 10, and the introduction pipe 10, the mixing unit 40 disposed between the liquid introduction unit 30 and the discharge unit 70, and the mixing unit 40 in the introduction tube 10, which is incorporated in the introduction tube 10, is connected to the mixing unit 40 in the introduction tube 10.
  • a gas introduction cylinder 80 to be taken in between the discharge section 70 and a collision plate 60 disposed between the mixing section 30 and the discharge section 70 in the introduction pipe 10 are provided (see FIGS. 7 to 14).
  • the schematic shape of the introduction pipe 10 and the configuration of the gas introduction section 20 and the discharge section 70 are the same as those in the first embodiment, so that the description thereof will be omitted.
  • the configurations of the liquid introduction unit 30, the mixing unit 40, the gas introduction cylinder 80, and the collision plate 60, which are characteristic configurations of the above, will be described.
  • the introduction pipe 10 is configured such that the upper parts of the first member 13 and the second member 14 are located above the liquid surface W of the liquid, and the middle part of the second member 14 and the third member 15 are provided.
  • the liquid introduction part 30 is disposed so as to be submerged below the liquid surface W of the liquid, and thereby the liquid introduction part 30 disposed in the middle part of the second member 14 and the discharge part provided at the end part of the third member 15. 70 is submerged in the liquid.
  • the gas introduction cylinder 80 is disposed and arranged from the gas introduction part 20 to the discharge part 70 of the introduction pipe 10.
  • the gas introduction cylinder 80 has a gas intake part 81c at the same end 81a as the gas introduction part 20 side of the introduction pipe 10 and a second end 81b same as the discharge part 70 side of the introduction pipe 10 at the second end 81b. It is formed in a thin cylindrical shape having two discharge portions 81d.
  • the gas introduction cylinder 80 is formed along the shafts 13b, 14b, and 15b in the extending directions of the first member 13, the second member 14, and the third member 15 of the introduction pipe 10, and is a gas intake portion.
  • 81 c opens in the same plane as the gas introduction part 20 of the introduction pipe 10, and the second discharge part 81 d opens between the mixing part 40 and the collision plate 60.
  • the gas introduction cylinder 80 By arranging the gas introduction cylinder 80 in this way, a part of the gas introduced into the introduction pipe 10 from the gas introduction part 20 is introduced into the gas introduction cylinder 80 from the gas intake part 81c, and the first It is discharged between the mixing part 40 and the collision plate 60 via the two discharge parts 81d.
  • the gas intake part 81c of the gas introduction cylinder 80 is open on the same surface as the gas introduction part 20 of the introduction pipe 10, the amount of gas discharged from the second discharge part 81d is , And changes depending on the amount of gas introduced by being pumped to the gas introduction unit 20.
  • a gas introduction space 10 a extending from the gas introduction part 20 of the introduction pipe 10 to the discharge part 80 is formed between the outer surface of the gas introduction cylinder 80 and the inner surface of the introduction pipe 10.
  • this gas introduction space 10a there is a path for conveying the gas introduced into the introduction pipe 10 from the gas introduction part 20 through the periphery of the liquid introduction part 30 along the introduction pipe 10 to the mixing part 40.
  • the outer diameter of the gas introduction cylinder 80 is set to a sufficiently smaller diameter than the inner diameter of the introduction pipe 10 in order to leave a gas introduction space 10a through which gas can sufficiently pass in the inner region of the introduction pipe 10.
  • the diameter of the introduction tube 10 is 60 mm, whereas the outer diameter of the gas introduction tube 80 is set to 17 mm and the inner diameter is set to 15 mm.
  • the outer diameter of the gas introduction cylinder 80 is not limited to the above numerical setting, and may be set freely according to the demand for the amount of gas introduced by the gas introduction cylinder 80.
  • the gas introduction cylinder 80 is provided by a thin rod-shaped support member 80 a provided from the inner wall surface of the introduction pipe 10 toward the gas introduction cylinder 80.
  • a cross-sectional view of the introduction tube 10 is supported at a substantially central portion.
  • the support member 80a includes the vicinity of the gas introduction part 20 of the first member 13 (introduction pipe 10), the downstream side 13a of the first member 13 (introduction pipe 10), and the third member 15 (introduction pipe 10).
  • each support member 80 a is provided with four support members 80 a at intervals of 90 ° in cross-sectional view of the introduction pipe 10 in the vicinity of the gas introduction part 20 of the first member 13.
  • three support members 80a are provided at intervals of 90 ° in a sectional view of the introduction tube 10.
  • the liquid introduction part 30 includes a hole 31 for sucking the liquid on the outer surface side of the introduction pipe 10 toward the inner surface side, and a mixing part for sucking the liquid sucked from the hole 31 through the hole 31. It is comprised with the introduction part 32 which discharge
  • the hole 31 is the second member 14 positioned on the downstream side of the gas introduction unit 20, and penetrates from the outer surface of the introduction tube 10 to the inner surface at a position where it is submerged in the liquid when the fine bubble generating device 1 is installed. Is formed.
  • the hole 31 includes four holes 31a, a hole 31b, a hole 31c, and a hole 31d.
  • the two holes 31a and 31c are formed so as to oppose each other in the radial direction of the second member 14 of the introduction tube 10 as shown in FIGS.
  • the holes 31b are formed so as to be arranged in the vertical direction with the holes 31a. Furthermore, as shown in FIGS.
  • the holes 31 d are arranged in the longitudinal direction with respect to the holes 31 b and are formed so as to face the radial direction of the holes 31 b and the second member 14.
  • the holes 31a and 31b have an inner diameter of 8 mm
  • the holes 31c and 31d have an inner diameter of 10 mm.
  • the vertical positions of the holes 31a and 31b and the holes 31c and 31d facing each other in the radial direction of the second member 14 are not positioned at the same height in the second embodiment, but from the top, the holes 31a and 31d are positioned at the same height.
  • Holes 31c, holes 31b, and holes 31d are alternately arranged in this order.
  • the inner diameters of the holes 31a and 31b and the holes 31c and 31d are the above-described inner diameters.
  • the hole diameter can be freely set according to the use environment and the demand for performance to generate fine bubbles. It ’s fine.
  • the case where the four holes 31a, 31b, 31c, and 31d are provided as the holes 31 of the liquid introduction unit 30 has been described.
  • the number of the holes 31 is not limited thereto.
  • the amount of gas introduced from the gas introduction unit 20 and the diameter of the introduction tube 10 may be set freely.
  • the positions of the hole 31a, the hole 31c, the hole 31b, and the hole 31d are not limited and may be set freely according to the use environment.
  • the introduction portion 32 is a box-shaped member formed so as to be in close contact with the inner surface of the second member 14 and to cover the hole 31 from the inner region side of the second member 14.
  • an opening 33 is provided on the downstream side of the hole 31.
  • an introduction portion 32a is provided in each hole 31a
  • an introduction portion 32b is provided in each hole 31b.
  • Each hole 31c is provided with an introduction portion 32c
  • each hole 31d is provided with an introduction portion 32d.
  • the introduction part 32a (introduction part 32b, introduction part 32c, introduction part 32d) is formed in the same shape, and is upstream of the hole 31a (holes 31b, 31c, 31d). Side (upper side in the figure) and both lateral sides, and has an opening 33a (opening parts 33b, 33c, 33d) directed toward the downstream side (lower side in the figure).
  • the two members 14 are formed so as to protrude toward the shaft 14b. Thereby, each cover 32a (32b, 32c, 32d) communicates with the hole 31a (holes 31b, 31c, 31d) and the opening 33a (openings 33b, 33c, 33d) and the inner surface of the introduction pipe 10 It is integrally formed.
  • the gas that is vigorously introduced into the gas introduction part 20 is the second member 14 of the introduction pipe 10.
  • the vicinity of the introduction portions 32a, 32b, 32c, 32d becomes negative pressure.
  • the liquid outside the second member 14 (introducing pipe 10) is drawn into and introduced into the introducing pipe 10 having a negative pressure from the holes 31a, 31b, 31c, and 31d.
  • the openings 33a, 33b, 33c, and 33d of the introduction portions 32a, 32b, 32c, and 32d are arranged toward the downstream side (the lower side in the figure) has been described.
  • the opening directions are not limited to the opening directions, and the holes 31a, 31b, 31c, and 31d may be used in order to prevent the gas inside the introduction pipe 10 from flowing backward when the liquid is introduced.
  • the opening is not particularly limited as long as the opening is further downstream.
  • the openings 33a, 33b, 33c, and 33d may be arranged in the direction along the inner peripheral surface of the introduction pipe 10 on the downstream side of the holes 31a, 31b, 31c, and 31d.
  • the mixing unit 40 is between the liquid introduction unit 30 and the discharge unit 70 in the third member 15 positioned on the downstream side of the liquid introduction unit 30, and includes a gas introduction cylinder 80. Is disposed in the gas introduction space 10 a between the outer surface of the gas and the inner surface of the introduction pipe 10.
  • the mixing unit 40 has a spiral shape (spiral winding) that is divided into a region on the liquid introduction unit 30 side and a region on the discharge unit 70 side in the gas introduction space 10 a.
  • the continuously arranged wall 41 is formed integrally with the inner surface of the introduction tube 10 to form a spiral mixing path 41a that connects the region on the liquid introduction unit 30 side and the region on the discharge unit 70 side. is doing.
  • the cross-sectional area of the mixing path 41a is set to be narrower than the cross-sectional area of the introduction pipe 10 on the liquid introduction part 30 side.
  • a mixed liquid in which the gas introduced from the gas introducing part 20 and the liquid introduced from the liquid introducing part 30 are mixed is increased in flow velocity when passing through the mixing path 41a, and is efficiently mixed.
  • a spiral turning motion along the axis 15b of the third member 15 is performed.
  • the centrifugal force toward the outer periphery side of the swirl (the side where the inner surface of the introduction pipe 10 is located).
  • the pressure on the outer peripheral side increases, and the pressure on the center side (the side where the shaft 15b of the third member 15 is present) decreases.
  • the bubbles become fine bubbles by dissolving bubbles generated at this time and generating bubbles due to cavitation.
  • a spiral of the mixed liquid is formed by the mixing unit 40 along the axis 15 b in the extending direction of the third member 15, and the gas intake unit is formed at a substantially central portion of the spiral.
  • the gas discharged from the 80 second discharge part 81d merges.
  • the pressure in the substantially central portion of the spiral is lower than that in the outer diameter side portion of the spiral, and the gas in the gas introduction unit 20 is higher in pressure than the atmospheric pressure, so that it is mixed into the second discharge unit 81d.
  • the gas passing through the gas intake part 80 is efficiently sucked into the introduction pipe 1 without the liquid flowing backward.
  • the gas sucked into the introduction pipe 1 from the gas intake part 80 is taken into the spiral by the mixing part 40.
  • the tube 81 of the gas intake unit 80 is formed with a small diameter, the gas discharged from the second discharge unit 81d of the gas intake unit 580 is a relatively small bubble, and the small bubble is swirled. It becomes a fine bubble by being taken in.
  • the collision plate 60 is a plate disposed between the second discharge portion 81 d of the gas intake portion 80 and the discharge portion 70, and is an inner surface of the introduction pipe 10.
  • the collision plate 60 is raised from the inner side surface of the third member 15 toward the shaft 15b.
  • the swirled mixed liquid takes in the gas from the gas intake unit 80 and collides with the collision plate 60 as a swirl while continuing swirling. At this time, a relatively large bubble that has not become a fine bubble or a gas from the gas intake unit 80 is sheared to become a fine bubble.
  • the flow in the swirling direction of the mixed liquid is rectified by the collision plate 60 into a flow in a direction in which the mixed liquid is discharged into the liquid.
  • the configuration including the gas intake unit 80 has been described.
  • the configuration is not limited thereto, and a configuration without the gas intake unit 80 may be used.
  • only the pressure-feed gas from the gas introduction unit 20 is introduced into the introduction pipe 10, so that the fine bubbles released from the discharge unit 70 include gas Since only the pressurized gas from the introduction part 20 is included and the gas outside the introduction pipe 10 is not included, it may be selected according to the demand for generating fine bubbles of only the pressurized gas from the gas introduction part 20. .
  • the gas introduction tube 80 of the second embodiment may be combined with the mixing unit 40 of the first embodiment. Even with such a configuration, the same effects as those of the first and second embodiments can be obtained. That is, the gas introduction cylinder 80 is arranged from the gas introduction part 20 to the discharge part 70 of the introduction pipe 10, and is further formed between the outer surface of the gas introduction cylinder 80 and the inner surface of the introduction pipe 10. Propeller-like blade members 42a, 42b, and 42c may be formed in the gas introduction space 10a to have a mixing path 41a between the blade members 42a, 42b, and 42c. Since other configurations are the same as those of the first and second embodiments, the description thereof is omitted.
  • the gas intake section 50 of the first embodiment may be combined with the mixing section 40 of the second embodiment. Even with such a configuration, the same effects as those of the first and second embodiments can be obtained. That is, the wall 41 continuously arranged in a spiral shape (spiral winding) divided into a region on the liquid introduction unit 30 side and a region on the discharge unit 70 side is formed integrally with the inner surface of the introduction tube 10. Thus, a spiral mixing path 41a that connects the region on the liquid introduction unit 30 side and the region on the discharge unit 70 side is formed, and the introduction is performed between the mixing unit 40 and the discharge unit 70 having such a configuration. The opening 52d of the other end 52b of the pipe 52 of the gas intake part 50 for taking in the gas outside the pipe 10 may be communicated. Since other configurations are the same as those of the first and second embodiments, the description thereof is omitted.
  • FIG. 1 is an external perspective view of a fine bubble generator according to Embodiment 1.
  • FIG. (A) is a perspective view which shows the internal structure of the microbubble generator by Example 1
  • (b) is a perspective view which shows the structure of a blade member and a connection member.
  • FIG. 1 is a longitudinal sectional view taken along line AA in FIG.
  • FIG. 3 is an end view taken along line BB in FIG.
  • FIG. 3 is an end view taken along the line CC in FIG.
  • FIG. 3 is a longitudinal sectional view taken along line DD in FIG.
  • It is an external appearance perspective view of the microbubble generator by Example 2.
  • FIG. It is a perspective view which shows the internal structure of the microbubble generator by Example 2.
  • FIG. FIG. 7 is a longitudinal sectional view taken along line EE.
  • FIG. 9 is an end view taken along line FF.
  • FIG. 9 is an end view taken along line GG.
  • FIG. 9 is a longitudinal sectional view taken along line HH.
  • FIG. 9 is a longitudinal sectional view taken along line II.
  • FIG. 9 is a sectional view taken along line JJ.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)

Abstract

A device which introduces thereinto gas having a higher pressure than atmospheric pressure and discharges the gas as microbubbles into liquid. A microbubble generation device (1) has an introduction tube (10) having at one end (11) thereof a gas introduction section (20) into which gas supplied under pressure is introduced and at the other end (12) thereof a discharge section (70) placed in liquid and discharging the introduced gas into the liquid; a liquid introduction section (30) for introducing the liquid into the introduction tube; a mixing section (40) placed in the introduction tube at a place between the liquid introduction section and the discharge section and mixing the gas and the liquid; a gas intake section (50) for taking gas outside the introduction tube into the introduction tube to a place between the mixing section and the discharge section; and a collision plate (60) placed in the introduction tube at a place between the mixing section and the discharge section and with which the gas and liquid mixed by the mixing section collide.

Description

微細気泡発生装置Microbubble generator

 本発明は、大気よりも高圧な気体を微細な気泡にして、液体中に放出する装置に関する。 The present invention relates to an apparatus for making a gas having a pressure higher than that of the atmosphere into fine bubbles and releasing it into a liquid.

 従来から、気体を液体に効率よく溶解したり、気体と液体の生物学的あるいは化学的な反応を促進したりする目的で、気体を液体に放出する際に、微細な気泡(マイクロバブル)にする微細気泡発生装置が用いられている。
 このような装置として、例えば、特許文献1は、ケーシングと、該ケーシング内部に液体を導入する液体供給筒と、気体を導入する気体供給筒とで構成されている先行技術を提案している。この先行技術は、前記液体供給筒からケーシング内部に液体を導入する際の勢いで、ケーシング内に供給された液体をケーシング内で旋回させ、これにより、旋回の遠心力によって中心付近に負圧を発生させる。この構成において、前記気体供給筒の気体導入口を、前記負圧となる部分に配し、ケーシング内部で生じている負圧部分にケーシング外部の気体を導入させる構成を開示している。
 このとき、旋回している混合液では、旋回の外周付近に、昇圧された部分が発生しており、前記混合液が負圧部分と昇圧部分とを通過する際に圧力が変化することに加えて、旋回流によるせん断力によって、微細な気泡が発生すると考えられる。
Conventionally, when a gas is released into a liquid for the purpose of efficiently dissolving the gas in the liquid or promoting a biological or chemical reaction between the gas and the liquid, the bubbles are made into fine bubbles (microbubbles). A fine bubble generator is used.
As such an apparatus, for example, Patent Document 1 proposes a prior art including a casing, a liquid supply cylinder that introduces liquid into the casing, and a gas supply cylinder that introduces gas. In this prior art, the liquid supplied from the liquid supply cylinder into the casing is swung, and the liquid supplied into the casing is swirled in the casing, whereby a negative pressure is generated near the center by the centrifugal force of swirling. generate. In this configuration, a configuration is disclosed in which the gas inlet of the gas supply cylinder is arranged in the portion that becomes the negative pressure, and the gas outside the casing is introduced into the negative pressure portion generated inside the casing.
At this time, in the swirling mixed liquid, a pressurized portion is generated in the vicinity of the outer periphery of the swirling, and the pressure changes when the mixed liquid passes through the negative pressure portion and the pressure increasing portion. Thus, it is considered that fine bubbles are generated by the shearing force generated by the swirling flow.

 上記従来の微細気泡発生装置では、ケーシング内に液体を圧送して旋回流を作り、その旋回流によって発生する負圧を利用して装置の外部から気体を取り込む構成となっているため、液体中に放出し得る気体の量は、ケーシング内に液体を圧送する量によって制限されている。従って、大量の気体を微細な気泡を要する場合には、大量の液体が圧送可能な装置と、その大量の液体を収容できる大型のケーシングが必要であるなど、装置が大型化する問題があった。
 そこで、ケーシング内に液体を圧送することなく、大量の気体を微細気泡にして、液体中に放出することのできる装置の開発が望まれていたが、現時点では、そのような装置は知られていない。
特開2006-142300号公報
In the above-described conventional fine bubble generator, liquid is pumped into the casing to create a swirl flow, and the negative pressure generated by the swirl flow is used to take in gas from the outside of the device. The amount of gas that can be released into the casing is limited by the amount of liquid pumped into the casing. Therefore, when a large amount of gas requires fine bubbles, there is a problem that the device becomes large, such as a device capable of pumping a large amount of liquid and a large casing capable of storing the large amount of liquid. .
Therefore, it has been desired to develop a device capable of making a large amount of gas into fine bubbles and discharging it into the liquid without pumping the liquid into the casing. At present, such a device is known. Absent.
JP 2006-142300 A

 本発明の目的は、上記問題点を解決するためになされており、大気圧よりも高圧な気体を導入することにより、その気体を微細な気泡にして、液体中に放出することのできる装置を提供することである。 An object of the present invention is to solve the above-mentioned problems. By introducing a gas having a pressure higher than atmospheric pressure, an apparatus capable of making the gas into fine bubbles and releasing it into a liquid is provided. Is to provide.

 上記課題を達成するために本発明がなした技術的手段は、圧送された気体を微細な気泡にして液体中に放出する微細気泡発生装置であって、圧送された気体を導入する気体導入部が一端側に設けられ、液体中に配されるとともに前記導入した気体を液体中に放出する吐出部が他端側に設けられた筒状の導入管と、前記液体を導入管の内部に導入する液体導入部と、前記導入管内にて、液体導入部と吐出部の間に配され、前記導入管内に導入された気体と液体とを混合させる混合部と、前記導入管内の混合部と吐出部の間に配され、混合部で混合された気体と液体が衝突する衝突板とを備えたことを特徴とする微細気泡発生装置としたことである。
 その場合、液体導入部は、導入管の外面から内面に貫通した穴と、該穴と連通して導入管内に配されるとともに前記穴よりも混合部よりの位置で開口する導入部とからなり、前記導入管内を気体が通過する際に生じる負圧により、前記導入部から導入管内に液体が取り込まれる構成であっても良い。
The technical means made by the present invention in order to achieve the above object is a fine bubble generating device that discharges compressed gas into fine bubbles and discharges it into the liquid, and introduces the pressurized gas into the gas introduction unit. Is provided on one end side, is disposed in the liquid, and has a cylindrical introduction pipe provided on the other end side with a discharge portion that discharges the introduced gas into the liquid, and introduces the liquid into the introduction pipe A liquid introduction section, a mixing section disposed between the liquid introduction section and the discharge section in the introduction pipe and mixing the gas and the liquid introduced into the introduction pipe, and the mixing section and the discharge section in the introduction pipe The microbubble generator is characterized in that it is provided with a collision plate that is disposed between the units and that collides with the gas mixed in the mixing unit and the liquid.
In this case, the liquid introduction part is composed of a hole penetrating from the outer surface to the inner surface of the introduction pipe, and an introduction part that is arranged in the introduction pipe so as to communicate with the hole and that is opened at a position closer to the mixing part than the hole. The liquid may be taken into the introduction pipe from the introduction portion by a negative pressure generated when the gas passes through the introduction pipe.

 また、混合部は、液体導入部側の領域と吐出部側の領域とに区分けする複数枚の羽根部材と、それぞれの羽根部材の間に設けられ、前記液体導入部側の領域と吐出部側の領域とを連通する混合経路とで構成され、該混合経路は、液体導入部側の導入管の断面積よりも狭い断面積を有する場合や、あるいは、液体導入部側の領域と吐出部側の領域とに区分けする螺旋状に連通するとともに、液体導入部側の導入管の断面積よりも狭い断面積を有する場合もある。これらの場合には、導入管内に導入された気体と液体が、断面積の狭い混合経路を通過する際に効率良く混合される。 The mixing unit is provided between a plurality of blade members that are divided into a region on the liquid introduction unit side and a region on the discharge unit side, and between each of the blade members, and the region on the liquid introduction unit side and the discharge unit side And a mixing path that communicates with the area of the liquid introduction section. The mixing path has a narrower cross-sectional area than the cross-sectional area of the introduction pipe on the liquid introduction section side, or the area on the liquid introduction section side and the discharge section side. In some cases, the cross-sectional area may be narrower than the cross-sectional area of the introduction pipe on the liquid introduction part side. In these cases, the gas and liquid introduced into the introduction pipe are efficiently mixed when passing through the mixing path having a narrow cross-sectional area.

 さらに、微細気泡発生装置は、導入管外部の気体を導入管内の混合部と吐出部との間に取り込む気体取り込み部を備えていても良く、あるいは、導入管内には、該導入管の気体導入部から吐出部にわたる長さの気体導入筒が内装されており、前記気体導入筒は、導入管の気体導入部側と同一の端部に気体取り込み部を有するとともに、導入管の吐出部側と同一の端部に第2の吐出部を有した細い筒状に形成され、前記気体導入筒の外面と導入管の内面との間に気体導入部から吐出部にわたる気体導入空間を形成し、混合部は、気体導入筒の外面と導入管の内面との間の気体導入空間に配設され、第2の吐出部は、混合部と衝突板との間に開口していても良い。 Further, the fine bubble generating device may include a gas intake unit that takes in gas outside the introduction tube between the mixing unit and the discharge unit in the introduction tube, or the gas introduction of the introduction tube is introduced into the introduction tube. A gas introduction cylinder having a length extending from the discharge section to the discharge section is internally provided, and the gas introduction cylinder has a gas intake section at the same end as the gas introduction section side of the introduction pipe, and the discharge section side of the introduction pipe; Formed into a thin cylinder having a second discharge part at the same end, forming a gas introduction space extending from the gas introduction part to the discharge part between the outer surface of the gas introduction cylinder and the inner surface of the introduction tube, and mixing The portion may be disposed in a gas introduction space between the outer surface of the gas introduction tube and the inner surface of the introduction tube, and the second discharge portion may be opened between the mixing portion and the collision plate.

 本発明によれば、大気圧よりも高圧な気体を導入することにより、その気体を微細な気泡にして、液体中に放出することのできる装置を提供することができる。 According to the present invention, by introducing a gas having a pressure higher than the atmospheric pressure, it is possible to provide a device that can make the gas into fine bubbles and discharge it into the liquid.

 以下、本発明の実施形態による微細気泡発生装置について説明する。なお、本実施形態では、産業機械等から空調装置によって強制的に大気より高圧で圧送された排気(気体)を微細な気泡にして水(液体)の中に放出する場合を想定している。
 なお、微細気泡発生装置が微細な気泡にする気体は、大気よりも高圧で圧送されていればどのような気体でも良く、該気体が微細な気泡となって放出される液体もまた、どのような液体でも良い。
 その一例として、廃棄物を焼却する焼却炉から排出された排気ガスの有害物質が大気中に拡散することを防止するために、該排気ガスを水中で効率よく濾過する場合や、薬品の製造装置において、中間精製されたガスを溶液中に放出して効率よく化学反応させる場合や、河川や湖沼において、水質汚染を防止するために、水中に大量の大気を溶解させる場合等が挙げられる。
Hereinafter, a fine bubble generator according to an embodiment of the present invention will be described. In the present embodiment, it is assumed that the exhaust gas (gas) forcedly fed by an air conditioner from an industrial machine or the like at a high pressure from the atmosphere is made into fine bubbles and discharged into water (liquid).
The gas that the fine bubble generating device makes fine bubbles may be any gas as long as it is pumped at a higher pressure than the atmosphere, and the liquid that is released as fine bubbles is also selected. It may be a liquid
As an example, in order to prevent the harmful substances of exhaust gas discharged from an incinerator that incinerates waste from diffusing into the atmosphere, the exhaust gas is efficiently filtered in water, or a chemical manufacturing apparatus. In this case, the intermediate purified gas is discharged into the solution to cause an efficient chemical reaction, or a large amount of air is dissolved in water to prevent water pollution in rivers and lakes.

 実施例1による微細気泡発生装置1は、図1~図6に示すように、圧送された気体を導入する気体導入部2が一端11側(上流側)に設けられるとともに、液体中に配され、前記気体導入部20で導入した気体を液体中に放出する吐出部70が他端12側(下流側)に設けられた筒状の導入管10と、前記液体を導入管10の内部に導入する液体導入部30と、前記導入管10内にて、液体導入部30と吐出部70の間に配された混合部40と、前記導入管10の外部の気体を導入管10内の混合部40と吐出部70との間に取り込む気体取り込み部50と、前記導入管内の混合部と吐出部の間に配された衝突板60とからなる。 As shown in FIGS. 1 to 6, the fine bubble generating device 1 according to the first embodiment is provided with a gas introduction part 2 for introducing a pumped gas on one end 11 side (upstream side) and disposed in a liquid. A discharge part 70 for releasing the gas introduced by the gas introduction part 20 into the liquid is provided with a cylindrical introduction pipe 10 provided on the other end 12 side (downstream side), and the liquid is introduced into the introduction pipe 10. The liquid introduction unit 30, the mixing unit 40 disposed between the liquid introduction unit 30 and the discharge unit 70 in the introduction pipe 10, and the mixing unit in the introduction pipe 10 for supplying gas outside the introduction pipe 10. 40 and a gas intake part 50 to be taken in between the discharge part 70 and a collision plate 60 arranged between the mixing part and the discharge part in the introduction pipe.

 気体導入部20は、図2乃至図4に示すように、導入管10の一端11(第1部材13の遊端)の開口として設けられ、気体を導入管10内に導入する。
 気体導入部20には、空調装置から排出された気体を搬送する圧送パイプ(図示しない)を直接連結するか、あるいは、圧送パイプを中継パイプにより連結することにより、大気よりも高い圧力で圧送パイプから送り出された気体が、気体導入部20から導入管10内に導入される。
As shown in FIGS. 2 to 4, the gas introduction unit 20 is provided as an opening of one end 11 of the introduction pipe 10 (the free end of the first member 13), and introduces gas into the introduction pipe 10.
A pressure feed pipe (not shown) that conveys the gas discharged from the air conditioner is directly connected to the gas introduction unit 20, or the pressure feed pipe is connected by a relay pipe, so that the pressure feed pipe has a higher pressure than the atmosphere. The gas sent out from is introduced into the introduction pipe 10 from the gas introduction part 20.

 吐出部70は、図2,図3及び図5に示すように、導入管10の他端12の開口として設けられており、液体中に配されて、該吐出部70から、気体導入部20から導入された気体が微細な気泡となって、液体中に放出される。 The discharge part 70 is provided as an opening at the other end 12 of the introduction tube 10 as shown in FIGS. 2, 3, and 5. The discharge part 70 is disposed in the liquid and is supplied from the discharge part 70 to the gas introduction part 20. The gas introduced from is turned into fine bubbles and released into the liquid.

 本実施例1の導入管10は、図2及び図3に示すように、両端を開口した円管状の第1部材13と、前記第1部材13と連通して設けられるとともに、両端を開口した円管状の第2部材14と、前記第2部材14と連通して設けられ、両端を開口した円管状の第3部材とで構成されている。従って、本実施形態によれば、第1部材から第3部材にわたって内部空間が連通した円管状の流路が形成されるとともに、第1部材の遊端側の開口が気体導入部20となり、第3部材の遊端側の開口が吐出部70となる。 As shown in FIGS. 2 and 3, the introduction pipe 10 of the first embodiment is provided with a circular tubular first member 13 having both ends open and the first member 13 in communication with each other, and both ends are open. The second member 14 is formed in a tubular shape, and the third member is provided in communication with the second member 14 and is open at both ends. Therefore, according to the present embodiment, a circular channel having an internal space communicating from the first member to the third member is formed, and the opening on the free end side of the first member serves as the gas introduction portion 20. The opening on the free end side of the three members is a discharge portion 70.

 また、図2及び図3に示すように、前記第1部材13は、水平方向に軸13bを有する直線状に形成されている。
 第2部材14は、前記第1部材13の軸13bと縦方向で直角に交差する軸14bを有する直線状に形成されている。第3部材15は、前記第2部材14の軸14bと直角に交差するとともに前記第1部材13の軸13bと平行な軸15bを有する直線状に形成されている。
 これにより、導入管10は、図3に示すように、いわゆるクランク形状を成している。
 また、本実施形態の導入管10は、同一の内径を有する筒状に形成され、例えば導入管10の内径は60mmに設定されている。
As shown in FIGS. 2 and 3, the first member 13 is formed in a linear shape having a shaft 13b in the horizontal direction.
The second member 14 is formed in a straight line having an axis 14b that intersects the axis 13b of the first member 13 at a right angle in the vertical direction. The third member 15 is formed in a straight line having an axis 15 b that intersects the axis 14 b of the second member 14 at a right angle and is parallel to the axis 13 b of the first member 13.
Thereby, the introduction pipe 10 has a so-called crank shape as shown in FIG.
In addition, the introduction tube 10 of the present embodiment is formed in a cylindrical shape having the same inner diameter. For example, the inner diameter of the introduction tube 10 is set to 60 mm.

 そして、導入管10は、図3と図4に示すように、第1部材13と第2部材14の上部が、液体の液体面Wよりも上側に位置するとともに、第2部材14の下部と第3部材15が、液体の液体面Wよりも下側に没するように設置される。このように設置されることにより、導入管10の他端12、すなわち、第3部材15の端部に設けられた吐出部70が液体中に没して配されることとなる。 As shown in FIGS. 3 and 4, the introduction pipe 10 has an upper portion of the first member 13 and the second member 14 positioned above the liquid surface W of the liquid, and a lower portion of the second member 14. The third member 15 is installed so as to be immersed below the liquid surface W of the liquid. By being installed in this manner, the other end 12 of the introduction tube 10, that is, the discharge portion 70 provided at the end of the third member 15 is arranged so as to be immersed in the liquid.

 なお、本実施例1では、それぞれ円管状に形成された第1部材13と第2部材14および第3部材15が、クランク形状に一体に連結されて導入管10の外形形状を構成している場合を挙げたが、該導入管10の外形形状は、上記形状に限定されることはない。
 例えば、第1部材13と第2部材14及び第3部材15が一直線状に一体に連結されて導入管10を構成していても良い。また、第1部材13と第2部材14及び第3部材15はS字状に形成されていても良い。
 さらに、導入管10は、本実施形態では3本の部材で構成されているが、構成本数は2本であっても4本以上であってもよく限定はされない。また、本実施形態のように複数の部材から構成されているものでなく、一本の連通した長尺の管状に形成されているものであってもよく本発明の範囲内である。また、この形態の場合であっても全体の外観形状は、直線状であっても、クランク状であってもS字状であってもよく限定解釈されない。
 また、導入管10の内径は、上述の数値設定に限定されず、微細気泡発生装置1の使用目的や使用環境などの要望に応じて自由に設定されれば良い。また、その際には、導入管10の内径は、一端11から他端12まで一定ではなく、大径や小径となる部分が設定されることにより変化していても良い。
 また、本実施例では、導入管10の断面形状を円形としたが、これに限定されず、導入管10が管状に形成されていれば、他の形状の断面形状を有していても良い。例えば、矩形の断面形状であっても良い。
In the first embodiment, the first member 13, the second member 14, and the third member 15 each formed in a circular tube shape are integrally connected in a crank shape to constitute the outer shape of the introduction tube 10. Although cases have been mentioned, the outer shape of the introduction tube 10 is not limited to the above shape.
For example, the first member 13, the second member 14, and the third member 15 may be integrally connected in a straight line to constitute the introduction tube 10. The first member 13, the second member 14, and the third member 15 may be formed in an S shape.
Furthermore, although the introduction pipe 10 is configured by three members in the present embodiment, the number of components may be two or four or more, and is not limited. Moreover, it is not comprised from several members like this embodiment, The thing formed in the shape of one continuous elongate tube may be sufficient, and it is in the scope of the present invention. Even in this case, the overall external shape may be linear, crank or S-shaped, and is not limitedly interpreted.
In addition, the inner diameter of the introduction tube 10 is not limited to the above numerical setting, and may be set freely according to demands such as the purpose of use and usage environment of the fine bubble generating device 1. In this case, the inner diameter of the introduction tube 10 is not constant from the one end 11 to the other end 12 but may be changed by setting a portion having a large diameter or a small diameter.
In the present embodiment, the cross-sectional shape of the introduction tube 10 is circular, but the present invention is not limited to this, and the cross-sectional shape of other shapes may be provided as long as the introduction tube 10 is formed in a tubular shape. . For example, a rectangular cross-sectional shape may be used.

 液体導入部30は、図2及び図3に示すように、後述する混合部よりも上流側に配されており、導入管10の外面から内面に貫通した穴31と、該穴31と連通して導入管10内に配された導入部32とからなる。
 穴31は、図3及び図4に示すように、第2部材14の気体導入部20側であって、微細気泡発生装置1を設置した場合に液体中に没する位置に、第2部材14(導入管10)の外面から内面に貫通して形成されている。
 本実施例では、穴31の穴径は、21mmに設定されている。なお、穴31の穴径は、これに限定されず、導入管10に導入する液体量の要望に応じて自由に設定されれば良い。
As shown in FIGS. 2 and 3, the liquid introduction part 30 is arranged on the upstream side of the mixing part described later, and communicates with the hole 31 penetrating from the outer surface to the inner surface of the introduction pipe 10. And an introduction part 32 arranged in the introduction pipe 10.
As shown in FIGS. 3 and 4, the hole 31 is on the gas introduction part 20 side of the second member 14, and at a position where the second member 14 is submerged in the liquid when the microbubble generator 1 is installed. It is formed so as to penetrate from the outer surface to the inner surface of (introducing tube 10).
In the present embodiment, the hole diameter of the hole 31 is set to 21 mm. The hole diameter of the hole 31 is not limited to this, and may be set freely according to the demand for the amount of liquid introduced into the introduction tube 10.

 導入部32は、図3に示すように、前記穴31に隙間なく連結されるとともに、該穴31から第2部材14の内側空間に、第2部材14の軸14bと直角に交差するように突出して備えた中空円筒状の第一円筒部34aと、該第一円筒部34aと連通するとともに、前記軸14bと平行して下流側(図では下向き)に向けて配された中空円筒状の第二円筒部34bとからなり、該第二円筒部34bの遊端側に開口部33を設けている。また、導入部32は、前記開口部33が、前記穴31よりも後述する混合部40寄りとなるように配されている。 As shown in FIG. 3, the introduction part 32 is connected to the hole 31 without a gap, and intersects the axis 14 b of the second member 14 from the hole 31 to the inner space of the second member 14 at a right angle. A hollow cylindrical first cylindrical portion 34a provided to project, and a hollow cylindrical shape that communicates with the first cylindrical portion 34a and that is disposed in parallel with the shaft 14b toward the downstream side (downward in the drawing). The second cylindrical portion 34b is provided, and an opening 33 is provided on the free end side of the second cylindrical portion 34b. Further, the introduction part 32 is arranged so that the opening 33 is closer to the mixing part 40 described later than the hole 31.

 また、本実施形態では、図3に示すように、第二円筒部34bは、前記開口部33が第3部材15の軸15b付近に位置するように形成されている。
 従って、前記導入管10内を気体が通過する際には、その流速によって液体導入部30の周辺は負圧となるので、導入管10の外部の液体が前記穴31から第2部材14(導入管10)の内側空間に引き込まれ、穴31よりも下流側の開口部33から導入管10の内側空間に放出されることとなる。
 また、本実施形態では、前記開口部33が第3部材15の軸15b付近に位置するように形成され、開口部33が該軸15b付近に開口するので、導入管10内に導入された液体は、後述する混合部40方向に送られる気体の気流に引っ張られて、効率よく混合部40の方向に進むようになる。
In the present embodiment, as shown in FIG. 3, the second cylindrical portion 34 b is formed so that the opening 33 is positioned near the shaft 15 b of the third member 15.
Accordingly, when the gas passes through the introduction pipe 10, the pressure around the liquid introduction portion 30 becomes negative due to the flow velocity, so that the liquid outside the introduction pipe 10 is introduced into the second member 14 (introduction from the hole 31. The air is drawn into the inner space of the pipe 10) and discharged from the opening 33 on the downstream side of the hole 31 into the inner space of the introduction pipe 10.
Further, in the present embodiment, the opening 33 is formed so as to be positioned near the shaft 15b of the third member 15, and the opening 33 opens near the shaft 15b, so that the liquid introduced into the introduction pipe 10 Is pulled by a gas stream sent in the direction of the mixing unit 40, which will be described later, and proceeds in the direction of the mixing unit 40 efficiently.

 なお、液体導入部30は、本実施形態で説明した構成になんら限定解釈されるものではなく、本発明の範囲内で設計変更可能である。
また、本実施形態では、穴31が液体中に没する第2部材14の所定位置に設けている実施の一形態を説明しているが、穴31が液体から外れた外方に位置している形態であってもよい。すなわち、液体中に配された図示しない外パイプが、液体よりも外に位置している穴31に接続されている形態であれば本発明と同様の作用効果を奏することができる。なお、外パイプは、導入管10内で生じる負圧によって液体が導入管10内に引き込めることが可能な長さとすることが条件となる。
The liquid introduction unit 30 is not construed as being limited to the configuration described in the present embodiment, and can be changed in design within the scope of the present invention.
Further, in the present embodiment, one embodiment in which the hole 31 is provided at a predetermined position of the second member 14 that is submerged in the liquid is described. However, the hole 31 is located outside the liquid. It may be a form. That is, as long as the outer pipe (not shown) arranged in the liquid is connected to the hole 31 located outside the liquid, the same effects as the present invention can be achieved. The outer pipe is required to have a length that allows the liquid to be drawn into the introduction pipe 10 by the negative pressure generated in the introduction pipe 10.

 混合部40は、図2に示すように、3枚の羽根部材42a,42b,42cでプロペラ状に形成されており、該羽根部材42a,42b,42cは、連結部材53によって、夫々連結されている。
 具体的には、図2及び図3に示すように、連結部材53は、一つの面(いわゆる三角錐形状の底面となる面)が三角形状の開口部53eとなった中空の内部領域53aを有する三角錐形状に形成されており、その開口部53eと、開口部53eに対向する三角錐の頂点55aとを結ぶ軸線が第3部材15の軸15bと同一の軸線となるように、導入管10の断面方向の中心部に配されている。
 なお、連結部材53の開口部53eは、混合部40の最も吐出部70寄りに位置している。
As shown in FIG. 2, the mixing unit 40 is formed in a propeller shape with three blade members 42 a, 42 b, 42 c, and the blade members 42 a, 42 b, 42 c are connected by a connecting member 53, respectively. Yes.
Specifically, as shown in FIGS. 2 and 3, the connecting member 53 includes a hollow inner region 53 a in which one surface (a surface that becomes a so-called triangular pyramid-shaped bottom surface) is a triangular opening 53 e. The introduction pipe is formed such that the axis connecting the opening 53e and the apex 55a of the triangular pyramid facing the opening 53e is the same as the axis 15b of the third member 15. 10 is arranged in the center of the cross-sectional direction.
The opening 53 e of the connecting member 53 is located closest to the discharge unit 70 of the mixing unit 40.

 羽根部材42a,42b,42cは、図2(a)及び図2(b)に示すように、連結部材53の前記開口部53eを除く各傾斜面(三角錐の頂点55aから底面となる開口部53eに向けて傾斜状に形成されている)53c,53d,53eと、第3部材15の内面との間にわたって架け渡されて配されたそれぞれが略扇形状に形成されている。
 羽根部材42aは、前記開口部53eの三角形の頂点55bから、該三角形の他の頂点55cと三角錐の頂点55aとを結ぶ辺43aにおける前記他の頂点55cから所定距離離れた位置45aにわたり面53cに一体に固着されている基端部44aと、該基端部44aと第3部材15の内面との間にわたり、拡開状に形成された立ち上がり部46aとで構成されている。立ち上がり部46aの上端は、第3部材15の内面と同一の円弧状に形成されるとともに、第3部材15の内面と一体に固着されている。すなわち、羽根部材42aは、第3部材15の径方向視で傾斜が加えられた傾斜羽根の形状となっている。
 羽根部材42bは、前記開口部53eの三角形の頂点55cから、該三角形の他の頂点55dと三角錐の頂点55aとを結ぶ辺43bにおける前記他の頂点55dから所定距離離れた位置45bにわたり面53dに一体に固着されている基端部44bと、該基端部44bと第3部材15の内面との間にわたり、拡開状に形成された立ち上がり部46bとで構成されている。立ち上がり部46bの上端は、第3部材15の内面と同一の円弧状に形成されるとともに、第3部材15の内面と一体に固着されている。すなわち、羽根部材42bは、第3部材15の径方向視で傾斜が加えられた傾斜羽根の形状となっている。
 羽根部材42cは、前記開口部53eの三角形の頂点55dから、該三角形の他の頂点55bと三角錐の頂点55aとを結ぶ辺43cにおける前記他の頂点55bから所定距離離れた位置45cにわたり面53eに一体に固着されている基端部44cと、該基端部44cと第3部材15の内面との間にわたり、拡開状に形成された立ち上がり部46cとで構成されている。立ち上がり部46cの上端は、第3部材15の内面と同一の円弧状に形成されるとともに、第3部材15の内面と一体に固着されている。すなわち、羽根部材42cは、第3部材15の径方向視で傾斜が加えられた傾斜羽根の形状となっている。
As shown in FIGS. 2A and 2B, the blade members 42a, 42b, and 42c are inclined surfaces (opening portions from the apex 55a of the triangular pyramid to the bottom surface) except for the opening 53e of the connecting member 53. 53c, 53d, and 53e (inclined toward 53e) and the inner surface of the third member 15 are arranged in a substantially fan shape.
The blade member 42a has a surface 53c extending from a triangular vertex 55b of the opening 53e to a position 45a that is a predetermined distance away from the other vertex 55c on the side 43a connecting the other vertex 55c of the triangle and the vertex 55a of the triangular pyramid. The base end portion 44a is integrally fixed to the base member 44, and the base end portion 44a and the inner surface of the third member 15 are formed with a rising portion 46a formed in an expanded shape. The upper end of the rising portion 46 a is formed in the same arc shape as the inner surface of the third member 15 and is fixed integrally with the inner surface of the third member 15. That is, the blade member 42 a has a shape of an inclined blade to which an inclination is added when viewed in the radial direction of the third member 15.
The blade member 42b has a surface 53d extending from a triangular vertex 55c of the opening 53e to a position 45b that is a predetermined distance away from the other vertex 55d on the side 43b connecting the other vertex 55d of the triangle and the vertex 55a of the triangular pyramid. A base end portion 44b fixed integrally with the base end portion 44b, and a rising portion 46b formed between the base end portion 44b and the inner surface of the third member 15 so as to expand. The upper end of the rising portion 46 b is formed in the same arc shape as the inner surface of the third member 15 and is fixed integrally with the inner surface of the third member 15. In other words, the blade member 42 b has a shape of an inclined blade to which an inclination is added as viewed in the radial direction of the third member 15.
The blade member 42c has a surface 53e extending from a triangular vertex 55d of the opening 53e to a position 45c at a predetermined distance from the other vertex 55b on the side 43c connecting the other vertex 55b of the triangle and the vertex 55a of the triangular pyramid. The base end portion 44c is integrally fixed to the base member 44, and the base end portion 44c and the inner surface of the third member 15 are provided with a rising portion 46c formed in an expanded shape. The upper end of the rising portion 46 c is formed in the same arc shape as the inner surface of the third member 15 and is fixed integrally with the inner surface of the third member 15. That is, the blade member 42c has a shape of an inclined blade to which an inclination is added in the radial view of the third member 15.

 このように形成された各羽根部材42a,42b,42cは、図2(b)に示すように、それぞれ隣り合う羽根部材42aと42b,42bと42c,42cと42a同士が、管の軸方向視で、所定距離はなれた、重なり合う領域が形成されるとともに、それぞれの重なり合った領域には、それぞれ前記液体導入部30側の領域と吐出部70側の領域とを連通する混合経路41a,41b,41cが形成されている。
 従って、上述した構成により、混合部40に到達した混合液は、混合経路41a,41b,41cのみを通過して混合部40の上流側の領域(混合部40を境にした液体導入部30側の領域)から下流側の領域(混合部40を境にした吐出部70側の領域)へと流れ込む。
As shown in FIG. 2 (b), the blade members 42a, 42b, 42c formed in this way are adjacent to each other between the blade members 42a and 42b, 42b and 42c, and 42c and 42a, respectively. Thus, overlapping regions that are separated from each other by a predetermined distance are formed, and in each of the overlapping regions, the mixing paths 41a, 41b, and 41c that respectively connect the region on the liquid introduction unit 30 side and the region on the discharge unit 70 side. Is formed.
Accordingly, with the above-described configuration, the liquid mixture that has reached the mixing unit 40 passes only through the mixing paths 41a, 41b, and 41c, and is located upstream of the mixing unit 40 (on the liquid introduction unit 30 side with the mixing unit 40 as a boundary). ) And the downstream area (area on the discharge section 70 side of the mixing section 40).

 この混合経路41a,41b,41cは、液体導入部30側の導入管10の断面積よりも狭い断面積を有している。これにより、気体導入部20から導入された気体と、液体導入部30から導入された液体とが混在した混合液が、連結部材53の3つの面53c,面53d,面53eの傾斜に沿って、徐々に第3部材15の内面側に向けた方向へと案内されるとともに、上記混合経路41a,41b,41cを通過する際に流速が速くなり、効率よく混合されながら、さらに第3部材15の軸線に沿った螺旋状の旋回運動をするようになる。 The mixing paths 41a, 41b, and 41c have a cross-sectional area that is narrower than the cross-sectional area of the introduction pipe 10 on the liquid introduction part 30 side. Thereby, the liquid mixture in which the gas introduced from the gas introduction part 20 and the liquid introduced from the liquid introduction part 30 coexist along the inclination of the three surfaces 53c, 53d, and 53e of the connecting member 53. The third member 15 is gradually guided in the direction toward the inner surface side of the third member 15, and the flow rate becomes faster when passing through the mixing paths 41a, 41b, 41c. A spiral turning motion along the axis of.

 なお、気体と液体が混在した混合液が旋回運動をする際には、混合液には、旋回の外周側(導入管10の内面のある側)へと向かった遠心力が作用し、このとき、混合液の圧力分布は、外周側の圧力が高くなり、中心側(第3部材15の軸線のある側)の圧力が低くなっている。
 このため、外周側では、圧力の高いので、気泡が液体に溶解され、中心側では、圧力が低いので、キャビテーションによる気泡が発生する。このように、気泡の溶解と発生を繰り返すことによって、気体が微細な気泡となる。
In addition, when the mixed liquid in which gas and liquid are mixed makes a swirling motion, centrifugal force directed to the outer peripheral side of the swirling (the side where the inner surface of the introduction pipe 10 is located) acts on the mixed liquid. In the pressure distribution of the mixed liquid, the pressure on the outer peripheral side is high, and the pressure on the center side (side where the axis of the third member 15 is located) is low.
For this reason, since the pressure is high on the outer peripheral side, the bubbles are dissolved in the liquid, and on the central side, the pressure is low, so that bubbles are generated by cavitation. In this way, by repeating the dissolution and generation of bubbles, the gas becomes fine bubbles.

 本実施例では、一例として、連結部材53が三角錐形状に形成された場合を説明したが、連結部材53の形状は、これに限定されることなく、導入管10の内側領域の流れの抵抗となりにくい形状が採用されていれば、他の形状であっても良い。例えば、砲弾型の円錐形状に形成され、該円錐形の底部が開口となっていても良い。
 また、本実施形態では、混合部40の構成として連結部材53を有しているもので説明したが、連結部材53は本発明において必須の構成要件ではなく、羽根部材42a,42b,42cのみで構成されているものであってもよい。
In the present embodiment, the case where the connecting member 53 is formed in a triangular pyramid shape has been described as an example. However, the shape of the connecting member 53 is not limited to this, and the flow resistance in the inner region of the introduction pipe 10 is not limited thereto. Other shapes may be used as long as a shape that is difficult to form is employed. For example, it may be formed in a shell-shaped conical shape, and the bottom of the conical shape may be an opening.
Further, in the present embodiment, the description has been given by using the connecting member 53 as the configuration of the mixing unit 40. However, the connecting member 53 is not an essential constituent element in the present invention, but only the blade members 42a, 42b, and 42c. It may be configured.

 なお、本実施形態では、上述した羽根部材構成としているが、これに限定解釈されず、本発明の範囲内で設計変更可能である。例えば、開口部53eの三角形の各頂点55b,55c,55dから基端部44a,44b,44cが設けられている実施の一形態を説明したが、各頂点55b,55c,55dから離れた位置から設けられている形態であっても本発明の範囲内である。また、基端部44a,44b,44cは、開口部53eの三角形の各辺と平行に設けるものであっても良い。すなわち、混合部40よりも上流側の気体と液体の混合液を、混合部の下流側である吐出部70へと送る際に、混合液が通過する混合経路41a,41b,41cが、導入管10の断面積よりも狭い断面積を有している構成が採用されるものであれば特にその形状に限定はされないものである。 In addition, in this embodiment, although it is set as the blade member structure mentioned above, it is not limited to this and a design change is possible within the scope of the present invention. For example, the embodiment in which the base end portions 44a, 44b, and 44c are provided from the respective triangular vertices 55b, 55c, and 55d of the opening 53e has been described, but from a position away from each of the vertices 55b, 55c, and 55d. Even the provided form is within the scope of the present invention. Further, the base end portions 44a, 44b, and 44c may be provided in parallel with the triangular sides of the opening 53e. That is, when the mixed liquid of gas and liquid upstream of the mixing unit 40 is sent to the discharge unit 70 downstream of the mixing unit, the mixing paths 41a, 41b, and 41c through which the mixed liquid passes are introduced pipes The configuration is not particularly limited as long as a configuration having a cross-sectional area narrower than 10 is adopted.

 気体取り込み部50は、図1乃至図3及び図5に示すように、導入管10の外部から気体を導入して、混合部40よりも吐出部70寄りに取り込む管52からなる。
 管52は、前記混合部40の連結部材53から、第3部材15の上部に設けられた貫通穴54を介して、該第3部材15の軸15bと直角に交差するとともに、管52の一端52aの開口52cが、液体の液体面Wよりも上側に位置するように配されている。
As shown in FIGS. 1 to 3 and 5, the gas intake unit 50 includes a tube 52 that introduces a gas from the outside of the introduction tube 10 and takes it closer to the discharge unit 70 than the mixing unit 40.
The tube 52 intersects the shaft 15b of the third member 15 at a right angle from the connecting member 53 of the mixing unit 40 through a through hole 54 provided in the upper portion of the third member 15, and one end of the tube 52 The opening 52c of 52a is arranged so as to be positioned above the liquid surface W of the liquid.

 また、管52の他端52bは、図2及び図3に示すように、前記貫通穴54を介して第3部材15の内部領域に挿し込まれるとともに、他端52bの開口52dが、羽根部材42a,42b,42cよりも上流側(液体導入部30側)で、連結部材53の中空の内部領域53aに連通している。
 なお、貫通穴54は、管52の外径よりも僅かに大径に形成されているが、貫通穴54と管52との隙間が塞がれているので、該貫通穴54から第3部材15の外部の液体が、第3部材15の内側領域に侵入することがない。
2 and 3, the other end 52b of the tube 52 is inserted into the internal region of the third member 15 through the through hole 54, and the opening 52d of the other end 52b is formed as a blade member. It communicates with the hollow inner region 53a of the connecting member 53 on the upstream side (the liquid introduction part 30 side) with respect to 42a, 42b, and 42c.
Although the through hole 54 is formed to have a diameter slightly larger than the outer diameter of the tube 52, the gap between the through hole 54 and the tube 52 is closed, so that the third member extends from the through hole 54. The liquid outside 15 does not enter the inner region of the third member 15.

 これにより、導入管10の外部の気体が、管52の一端52aから導入され、他端53bから、連結部材53の内部領域53aに取り込まれる。この場合、連結部材53の開口部53eが混合部40の最も吐出部70寄りに位置していることにより、導入管10の外部の気体は、混合部40よりも吐出部70寄りに取り込まれることになる。
 本実施例1では、気体取り込み部50の管52の一端52aには、図示しない空気ポンプが接続されており、該空気ポンプから強制的に外気が導入されている。従って、気体取り込み部50の連結部材53から排出される気体の量は、空気ポンプの稼動量に応じて変化させることができる。
Thereby, the gas outside the introduction pipe 10 is introduced from one end 52a of the pipe 52, and taken into the internal region 53a of the connecting member 53 from the other end 53b. In this case, since the opening 53 e of the connecting member 53 is positioned closest to the discharge unit 70 of the mixing unit 40, the gas outside the introduction pipe 10 is taken closer to the discharge unit 70 than the mixing unit 40. become.
In the first embodiment, an air pump (not shown) is connected to one end 52a of the pipe 52 of the gas intake unit 50, and outside air is forcibly introduced from the air pump. Therefore, the amount of gas discharged from the connecting member 53 of the gas intake unit 50 can be changed according to the operating amount of the air pump.

 本実施例の管52の外径は6mmに設定され、内径は4mmに設定されている。なお、管52の外径や内径は、これに限定されず、導入管10の外部の気体を導入する量の要望に応じて、自由に設定されれば良い。 The outer diameter of the pipe 52 of this embodiment is set to 6 mm, and the inner diameter is set to 4 mm. The outer diameter and inner diameter of the pipe 52 are not limited to this, and may be set freely according to the demand for the amount of gas introduced outside the introduction pipe 10.

 混合部40の下流側では、前記混合部40によって第3部材15の軸15bに沿った混合液の渦巻きが形成されており、その渦巻きの略中心部分には、前記気体取り込み部50から取り込まれ、連結部材53の開口53bから排出された気体が合流する。
 このとき、渦巻きの略中心部分は、渦巻きの外径側部分と比べて圧力が低くなっており、気体導入部20の気体は大気圧よりも高圧であるので、連結部材53の内部領域53aに混合液が逆流することなく、気体取り込み部50からの気体が効率よく導入管10に吸い込まれる。そして、気体取り込み部50からの気体は、前記気体と液体が混在した混合液と一緒に旋回運動を繰り返すことによって、微細な気泡となる。
On the downstream side of the mixing unit 40, a swirl of the mixed liquid is formed by the mixing unit 40 along the shaft 15 b of the third member 15, and is taken in from the gas intake unit 50 at a substantially central portion of the swirl. The gas discharged from the opening 53b of the connecting member 53 joins.
At this time, the pressure in the substantially central portion of the spiral is lower than that in the outer diameter side portion of the spiral, and the gas in the gas introduction unit 20 is higher than the atmospheric pressure. The gas from the gas intake unit 50 is efficiently sucked into the introduction pipe 10 without the mixed liquid flowing backward. And the gas from the gas taking-in part 50 becomes a fine bubble by repeating a turning motion with the liquid mixture in which the gas and the liquid were mixed.

 衝突板60は、図2及び図3に示すように、混合部40と吐出部70との間に配された板であって、導入管10の内面から第3部材15の軸15bに沿って延設されている。
 本実施例では、衝突板60は、第3部材15の下側内面から軸15bに向かって、導入管10の内径の半分の高さまで、立ち上げられているとともに、該衝突板60の上流側が円弧状に形成されている。
 前記旋回した混合液は、気体取り込み部50からの気体を取り込んで、旋回を続けながら渦巻きとなって衝突板60に衝突する。このとき、混合部40を通過した際に微細な気泡とならなかった比較的大きな気泡や、気体取り込み部50からの気体がせん断されて、微細な気泡となる。それに加えて、混合液の旋回方向の流れは、衝突板60によって、吐出部70から液体中への放出される方向の流れに整流される。
2 and 3, the collision plate 60 is a plate disposed between the mixing unit 40 and the discharge unit 70, and extends from the inner surface of the introduction tube 10 along the axis 15 b of the third member 15. It is extended.
In the present embodiment, the collision plate 60 is raised from the lower inner surface of the third member 15 toward the shaft 15b to a height that is half the inner diameter of the introduction tube 10, and the upstream side of the collision plate 60 is It is formed in an arc shape.
The swirled mixed liquid takes in the gas from the gas take-in portion 50 and collides with the collision plate 60 as a swirl while continuing swirling. At this time, relatively large bubbles that did not become fine bubbles when passing through the mixing unit 40 and gas from the gas intake unit 50 are sheared to become fine bubbles. In addition, the flow in the swirling direction of the mixed liquid is rectified by the collision plate 60 into a flow in a direction in which the mixed liquid is discharged into the liquid.

 本実施例1によれば、気体導入部20から導入管10内に導入された気体が、液体導入部30を通過する際の負圧によって、導入管10の外部の液体が導入管10内に導入されるとともに、該導入管10内に導入された気体と、液体導入部30から導入された液体とが、混合部40の混合経路41a,41b,41cを通過する際に効率よく混合される。混合部40を通過して混合された気体と液体は、微細な気泡となりながら、衝突板60に衝突することによって、微細な気泡(マイクロバブル)を大量に発生させて、液体中に放出される。さらに、気体取り込み部50から追加して外気を導入することによって、微細な気泡の量を増加させることができる。 According to the first embodiment, the gas introduced into the introduction pipe 10 from the gas introduction part 20 causes the liquid outside the introduction pipe 10 to enter the introduction pipe 10 due to the negative pressure when passing through the liquid introduction part 30. While being introduced, the gas introduced into the introduction pipe 10 and the liquid introduced from the liquid introduction part 30 are efficiently mixed when passing through the mixing paths 41a, 41b, 41c of the mixing part 40. . The gas and the liquid mixed through the mixing unit 40 collide with the collision plate 60 while forming fine bubbles, thereby generating a large amount of fine bubbles (microbubbles) and releasing them into the liquid. . Furthermore, the amount of fine bubbles can be increased by additionally introducing outside air from the gas intake unit 50.

 このように、本実施例1による微細気泡発生装置1は、微細な気泡を発生させる際に、ケーシング内(装置内)に液体を圧送する必要がなく、経済的である。また、導入される外気の量に応じて微細な気泡を発生されることができるので、工場や内燃機関からの排気を液体に溶解させて浄化させる場合や、気体と液体の生物学的あるいは化学的な反応を促進させる場合などに好適である。 Thus, the fine bubble generating device 1 according to the first embodiment is economical because it does not need to pump the liquid into the casing (inside the device) when generating fine bubbles. In addition, since fine bubbles can be generated according to the amount of outside air introduced, the exhaust from a factory or internal combustion engine can be dissolved in liquid and purified, or the biological or chemical of gas and liquid This is suitable for promoting a typical reaction.

 また、本実施例では、液体導入部30を液体中に没する位置に配した構成を説明したが、液体導入部30が液体中に没さずに、液体の液体面Wよりも上側に位置するように配した構成とすることもできる。
 この場合には、導入管10の外面において、液体導入部30の穴31から隙間無く延出するとともに、先端側が液体中に没した導入管を設けるなど、穴31に液体が供給される構成とすれば良い。
Further, in the present embodiment, the configuration in which the liquid introduction unit 30 is disposed at a position where the liquid introduction unit 30 is submerged in the liquid has been described, but the liquid introduction unit 30 is not submerged in the liquid and is positioned above the liquid surface W of the liquid. It can also be set as the structure arranged so.
In this case, on the outer surface of the introduction tube 10, the liquid is supplied to the hole 31, such as providing an introduction tube that extends from the hole 31 of the liquid introduction part 30 without a gap and whose tip side is submerged in the liquid. Just do it.

 また、本実施例では、気体取り込み部50を備えた構成を説明したが、これに限定されず、気体取り込み部50を備えない構成であっても良い。気体取り込み部50を備えない構成の場合には、導入管10には、気体導入部20からの圧送気体のみが導入される構成となるので、吐出部70から放出される微細気泡には、気体導入部20からの圧送気体のみが含まれ、導入管10の外部の気体が含まれないので、気体導入部20からの圧送気体のみの微細な気泡を発生させる要望に応じて選択されれば良い。 In the present embodiment, the configuration including the gas intake unit 50 has been described. However, the configuration is not limited thereto, and a configuration without the gas intake unit 50 may be used. In the case of a configuration that does not include the gas intake unit 50, only the pressurized gas from the gas introduction unit 20 is introduced into the introduction pipe 10, and thus the fine bubbles released from the discharge unit 70 include gas. Since only the pressurized gas from the introduction part 20 is included and the gas outside the introduction pipe 10 is not included, it may be selected according to the demand for generating fine bubbles of only the pressurized gas from the gas introduction part 20. .

 微細気泡発生装置1は、他の構成とした場合であっても、前述した実施例1と同様の効果を得ることができる。以下に、実施例2による微細気泡発生装置1の構成を説明する。
 実施例2による微細気泡発生装置1は、圧送された気体を導入する気体導入部20が一端11側(上流側)に設けられるとともに、液体中に配され、前記気体導入部20で導入した気体を液体中に放出する吐出部70が他端12側(下流側)に設けられた筒状の導入管10と、前記液体を導入管10の内部に導入する液体導入部30と、前記導入管10内にて、液体導入部30と吐出部70の間に配された混合部40と、導入管10内に内装されて、気体導入部20側の気体を導入管10内の混合部40と吐出部70との間に取り込む気体導入筒80と、前記導入管10内の混合部30と吐出部70の間に配された衝突板60を備えている(図7~図14参照)。
Even if the microbubble generator 1 has a different configuration, the same effects as those of the first embodiment described above can be obtained. Below, the structure of the microbubble generator 1 by Example 2 is demonstrated.
In the fine bubble generating apparatus 1 according to the second embodiment, the gas introduction unit 20 for introducing the pumped gas is provided on the one end 11 side (upstream side), and the gas introduced into the liquid is introduced in the gas introduction unit 20. A cylindrical introduction pipe 10 provided with a discharge part 70 for discharging the liquid into the other end 12 (downstream side), a liquid introduction part 30 for introducing the liquid into the introduction pipe 10, and the introduction pipe 10, the mixing unit 40 disposed between the liquid introduction unit 30 and the discharge unit 70, and the mixing unit 40 in the introduction tube 10, which is incorporated in the introduction tube 10, is connected to the mixing unit 40 in the introduction tube 10. A gas introduction cylinder 80 to be taken in between the discharge section 70 and a collision plate 60 disposed between the mixing section 30 and the discharge section 70 in the introduction pipe 10 are provided (see FIGS. 7 to 14).

 また、本実施例では、導入管10の概略形状および、気体導入部20及び吐出部70の構成においては、実施例1と同様であるので、その説明を省略し、以下には、本実施例の特徴的な構成である、液体導入部30と、混合部40と、気体導入筒80と、衝突板60の構成について説明する。
 なお、本実施例では、導入管10は、第1部材13と第2部材14の上部が、液体の液体面Wよりも上側に位置するとともに、第2部材14の中部と第3部材15が、液体の液体面Wよりも下側に没するように設置され、これにより、第2部材14の中部に配された液体導入部30及び、第3部材15の端部に設けられた吐出部70が液体中に没している。
Further, in this embodiment, the schematic shape of the introduction pipe 10 and the configuration of the gas introduction section 20 and the discharge section 70 are the same as those in the first embodiment, so that the description thereof will be omitted. The configurations of the liquid introduction unit 30, the mixing unit 40, the gas introduction cylinder 80, and the collision plate 60, which are characteristic configurations of the above, will be described.
In the present embodiment, the introduction pipe 10 is configured such that the upper parts of the first member 13 and the second member 14 are located above the liquid surface W of the liquid, and the middle part of the second member 14 and the third member 15 are provided. The liquid introduction part 30 is disposed so as to be submerged below the liquid surface W of the liquid, and thereby the liquid introduction part 30 disposed in the middle part of the second member 14 and the discharge part provided at the end part of the third member 15. 70 is submerged in the liquid.

 本実施例の気体導入筒80は、図8及び図9に示すように、導入管10の気体導入部20から吐出部70にわたって内装されて配されている。
 前記気体導入筒80は、導入管10の気体導入部20側と同一の端部81aには、気体取り込み部81cを有するとともに、導入管10の吐出部70側と同一の端部81bに、第2の吐出部81dを有した細い筒状に形成されている。
 具体的には、気体導入筒80は、導入管10の第1部材13と第2部材14と第3部材15の各延設方向の軸13b,14b,15bに沿って形成され、気体取り込み部81cは、導入管10の気体導入部20と同一面に開口し、第2の吐出部81dは、混合部40と衝突板60との間に開口している。
As shown in FIGS. 8 and 9, the gas introduction cylinder 80 according to the present embodiment is disposed and arranged from the gas introduction part 20 to the discharge part 70 of the introduction pipe 10.
The gas introduction cylinder 80 has a gas intake part 81c at the same end 81a as the gas introduction part 20 side of the introduction pipe 10 and a second end 81b same as the discharge part 70 side of the introduction pipe 10 at the second end 81b. It is formed in a thin cylindrical shape having two discharge portions 81d.
Specifically, the gas introduction cylinder 80 is formed along the shafts 13b, 14b, and 15b in the extending directions of the first member 13, the second member 14, and the third member 15 of the introduction pipe 10, and is a gas intake portion. 81 c opens in the same plane as the gas introduction part 20 of the introduction pipe 10, and the second discharge part 81 d opens between the mixing part 40 and the collision plate 60.

 気体導入筒80がこのように配されることにより、気体導入部20から導入管10内に導入される気体の一部が、気体取り込み部81cから気体導入筒80内に導入されるとともに、第2の吐出部81dを介して混合部40と衝突板60との間に吐出される。
 なお、本実施例では、気体導入筒80の気体取り込み部81cが、導入管10の気体導入部20と同一面に開口しているため、第2の吐出部81dから吐出される気体の量は、気体導入部20に圧送されて導入される気体の量に応じて変化する。
By arranging the gas introduction cylinder 80 in this way, a part of the gas introduced into the introduction pipe 10 from the gas introduction part 20 is introduced into the gas introduction cylinder 80 from the gas intake part 81c, and the first It is discharged between the mixing part 40 and the collision plate 60 via the two discharge parts 81d.
In this embodiment, since the gas intake part 81c of the gas introduction cylinder 80 is open on the same surface as the gas introduction part 20 of the introduction pipe 10, the amount of gas discharged from the second discharge part 81d is , And changes depending on the amount of gas introduced by being pumped to the gas introduction unit 20.

 また、前記気体導入筒80の外面と導入管10の内面との間には、導入管10の気体導入部20から吐出部80にわたる気体導入空間10aを形成している。この気体導入空間10aには、気体導入部20から導入管10内に導入された気体を、導入管10に沿って、液体導入部30の周辺を通過して混合部40へと搬送する経路となる。
 従って、気体導入筒80の外径は、導入管10の内側領域に気体が十分に通過することが可能な気体導入空間10aを残すため、導入管10の内径よりも十分に小径に設定される必要がある。本実施例では、導入管10の径が60mmであるのに対して、気体導入筒80の外径は17mmに設定され、内径は15mmに設定されている。なお、気体導入筒80の外径は、上記数値設定に限定されず、気体導入筒80で導入する気体量の要望に応じて自由に設定されれば良い。
A gas introduction space 10 a extending from the gas introduction part 20 of the introduction pipe 10 to the discharge part 80 is formed between the outer surface of the gas introduction cylinder 80 and the inner surface of the introduction pipe 10. In this gas introduction space 10a, there is a path for conveying the gas introduced into the introduction pipe 10 from the gas introduction part 20 through the periphery of the liquid introduction part 30 along the introduction pipe 10 to the mixing part 40. Become.
Therefore, the outer diameter of the gas introduction cylinder 80 is set to a sufficiently smaller diameter than the inner diameter of the introduction pipe 10 in order to leave a gas introduction space 10a through which gas can sufficiently pass in the inner region of the introduction pipe 10. There is a need. In the present embodiment, the diameter of the introduction tube 10 is 60 mm, whereas the outer diameter of the gas introduction tube 80 is set to 17 mm and the inner diameter is set to 15 mm. The outer diameter of the gas introduction cylinder 80 is not limited to the above numerical setting, and may be set freely according to the demand for the amount of gas introduced by the gas introduction cylinder 80.

 さらに、気体導入筒80は、図8乃至図10、図12乃至図13に示すように、導入管10の内壁面から気体導入筒80に向けて設けられた、細い棒状の支持部材80aによって、導入管10の断面視、略中央部に支持されている。本実施例では、支持部材80aは、第1部材13(導入管10)の気体導入部20の近傍と、第1部材13(導入管10)の下流側13a、第3部材15(導入管10)の上流側に備えられている。具体的には、各支持部材80aは、第1部材13の気体導入部20の近傍では、導入管10の断面視90°の間隔で4本の支持部材80aが備えられ、第1部材13の下流側13a及び第3部材15の上流側では、導入管10の断面視90°の間隔で3本の支持部材80aが備えられている。 Further, as shown in FIGS. 8 to 10 and 12 to 13, the gas introduction cylinder 80 is provided by a thin rod-shaped support member 80 a provided from the inner wall surface of the introduction pipe 10 toward the gas introduction cylinder 80. A cross-sectional view of the introduction tube 10 is supported at a substantially central portion. In the present embodiment, the support member 80a includes the vicinity of the gas introduction part 20 of the first member 13 (introduction pipe 10), the downstream side 13a of the first member 13 (introduction pipe 10), and the third member 15 (introduction pipe 10). ) On the upstream side. Specifically, each support member 80 a is provided with four support members 80 a at intervals of 90 ° in cross-sectional view of the introduction pipe 10 in the vicinity of the gas introduction part 20 of the first member 13. On the downstream side 13a and the upstream side of the third member 15, three support members 80a are provided at intervals of 90 ° in a sectional view of the introduction tube 10.

 液体導入部30は、図7乃至図13に示すように、導入管10の外面側の液体を内面側に吸入する穴31と、該穴31から吸入された液体を該穴31よりも混合部40寄りで第2部材14の内側領域に放出する導入部32とで構成されている。 As shown in FIGS. 7 to 13, the liquid introduction part 30 includes a hole 31 for sucking the liquid on the outer surface side of the introduction pipe 10 toward the inner surface side, and a mixing part for sucking the liquid sucked from the hole 31 through the hole 31. It is comprised with the introduction part 32 which discharge | releases to the inner side area | region of the 2nd member 14 near 40.

 穴31は、気体導入部20の下流側に位置付けられる第2部材14であって、微細気泡発生装置1を設置した場合、液体中に没する位置に、導入管10の外面から内面に貫通して形成されている。
 本実施例2では、穴31として、4つの穴31a,穴31b,穴31c,穴31dを備えている。
 この場合、2つの穴31a,穴31cは、図10乃至図14に示すように、導入管10の第2部材14の径方向に対向して形成されている。
 また、穴31bは、図10及び図11に示すように、前記穴31aと縦方向に配列されて形成されている。
 さらに、穴31dは、図10乃至図14に示すように、前記穴31bと縦方向に配列され、かつ、穴31bと第2部材14の径方向に対向して形成されている。
 なお、穴径は、穴31a,31bは、内径8mmに形成され、穴31c,31dは、内径10mmに形成されている。
 互いに、第2部材14の径方向に対向する穴31a,31bと穴31c,31dの縦方向の位置は、本実施例2では、同一の高さに位置付けられるのではなく、上から、穴31a,穴31c,穴31b,穴31dの順に交互に配されている。
The hole 31 is the second member 14 positioned on the downstream side of the gas introduction unit 20, and penetrates from the outer surface of the introduction tube 10 to the inner surface at a position where it is submerged in the liquid when the fine bubble generating device 1 is installed. Is formed.
In the second embodiment, the hole 31 includes four holes 31a, a hole 31b, a hole 31c, and a hole 31d.
In this case, the two holes 31a and 31c are formed so as to oppose each other in the radial direction of the second member 14 of the introduction tube 10 as shown in FIGS.
Further, as shown in FIGS. 10 and 11, the holes 31b are formed so as to be arranged in the vertical direction with the holes 31a.
Furthermore, as shown in FIGS. 10 to 14, the holes 31 d are arranged in the longitudinal direction with respect to the holes 31 b and are formed so as to face the radial direction of the holes 31 b and the second member 14.
The holes 31a and 31b have an inner diameter of 8 mm, and the holes 31c and 31d have an inner diameter of 10 mm.
The vertical positions of the holes 31a and 31b and the holes 31c and 31d facing each other in the radial direction of the second member 14 are not positioned at the same height in the second embodiment, but from the top, the holes 31a and 31d are positioned at the same height. , Holes 31c, holes 31b, and holes 31d are alternately arranged in this order.

 なお、本実施例2では、穴31a,31b及び穴31c,31dの内径を上述の内径としたが、穴径は、使用環境や微細な気泡を発生させる性能の要望に応じて自由に設定すれば良い。
 また、本実施例2では、液体導入部30の穴31として、4つの穴31a,穴31b,穴31c,穴31dを備えた場合を説明したが、穴31の数は、これに限定されず、気体導入部20から導入される気体の量や、導入管10の径などの条件に応じて自由に設定すれば良い。また、穴31a,穴31c,穴31b,穴31dの位置についても、限定されず、使用環境に応じて自由に設定すれば良い。
In the second embodiment, the inner diameters of the holes 31a and 31b and the holes 31c and 31d are the above-described inner diameters. However, the hole diameter can be freely set according to the use environment and the demand for performance to generate fine bubbles. It ’s fine.
In the second embodiment, the case where the four holes 31a, 31b, 31c, and 31d are provided as the holes 31 of the liquid introduction unit 30 has been described. However, the number of the holes 31 is not limited thereto. The amount of gas introduced from the gas introduction unit 20 and the diameter of the introduction tube 10 may be set freely. Further, the positions of the hole 31a, the hole 31c, the hole 31b, and the hole 31d are not limited and may be set freely according to the use environment.

 導入部32は、図8及び図12に示すように、第2部材14の内面と密着し、かつ、穴31を第2部材14の内側領域側から覆うように形成された箱状の部材であって、該穴31よりも下流側に開口33を有している。
 本実施例2による構成では、穴31として、4つの穴31a,穴31b,穴31c,穴31dを備えているので、各穴31aには導入部32aが、各穴31bには導入部32bが、各穴31cには導入部32cが、各穴31dには導入部32dが、それぞれ備えられている。
 具体的には、図8に示すように、導入部32a(導入部32b,導入部32c,導入部32d)は、それぞれ同形に形成されており、穴31a(穴31b,31c,31d)の上流側(図中上側)と両横側をカバーするとともに、下流側(図中下側)に向けた開口部33a(開口部33b,33c,33d)を有し、導入管10の内面から、第2部材14の軸14bに向けて突出して形成されている。これにより、各カバー32a(32b,32c,32d)は、穴31a(穴31b,31c,31d)、開口部33a(開口部33b,33c,33d)とが連通するとともに、導入管10の内面と一体に形成されている。
As shown in FIGS. 8 and 12, the introduction portion 32 is a box-shaped member formed so as to be in close contact with the inner surface of the second member 14 and to cover the hole 31 from the inner region side of the second member 14. In addition, an opening 33 is provided on the downstream side of the hole 31.
In the configuration according to the second embodiment, since the four holes 31a, 31b, 31c, and 31d are provided as the holes 31, an introduction portion 32a is provided in each hole 31a, and an introduction portion 32b is provided in each hole 31b. Each hole 31c is provided with an introduction portion 32c, and each hole 31d is provided with an introduction portion 32d.
Specifically, as shown in FIG. 8, the introduction part 32a (introduction part 32b, introduction part 32c, introduction part 32d) is formed in the same shape, and is upstream of the hole 31a (holes 31b, 31c, 31d). Side (upper side in the figure) and both lateral sides, and has an opening 33a (opening parts 33b, 33c, 33d) directed toward the downstream side (lower side in the figure). The two members 14 are formed so as to protrude toward the shaft 14b. Thereby, each cover 32a (32b, 32c, 32d) communicates with the hole 31a (holes 31b, 31c, 31d) and the opening 33a (openings 33b, 33c, 33d) and the inner surface of the introduction pipe 10 It is integrally formed.

 また、液体導入部30の穴31a,穴31bと穴31c,穴31dは、液体中に没しているので、気体導入部20に勢い良く導入された気体が、導入管10の第2部材14を通過すると、導入部32a,32b,32c,32d付近が負圧になる。このとき、穴31a,穴31b,穴31c,穴31dから、第2部材14(導入管10)の外側の液体が、負圧となった導入管10の内側に引き込まれて導入される。
 なお、本実施形態では、導入部32a,32b,32c,32dの開口部33a,33b,33c,33dが下流側(図中下側)に向けて配された場合を説明したが、開口部33a,33b,33c,33dが開口する向きについては、これに限定されず、液体の導入時に導入管10の内側の気体が逆流することを避けるために、穴31a,穴31b,穴31c,穴31dよりも下流側で開口していれば、特に限定されない。例えば、開口部33a,33b,33c,33dが穴31a,31b,31c,31dよりも下流側で、導入管10の内側周面に沿った方向に配されていても良い。
Further, since the holes 31a, 31b, 31c, and 31d of the liquid introduction part 30 are submerged in the liquid, the gas that is vigorously introduced into the gas introduction part 20 is the second member 14 of the introduction pipe 10. When passing through, the vicinity of the introduction portions 32a, 32b, 32c, 32d becomes negative pressure. At this time, the liquid outside the second member 14 (introducing pipe 10) is drawn into and introduced into the introducing pipe 10 having a negative pressure from the holes 31a, 31b, 31c, and 31d.
In this embodiment, the case where the openings 33a, 33b, 33c, and 33d of the introduction portions 32a, 32b, 32c, and 32d are arranged toward the downstream side (the lower side in the figure) has been described. , 33b, 33c, and 33d are not limited to the opening directions, and the holes 31a, 31b, 31c, and 31d may be used in order to prevent the gas inside the introduction pipe 10 from flowing backward when the liquid is introduced. The opening is not particularly limited as long as the opening is further downstream. For example, the openings 33a, 33b, 33c, and 33d may be arranged in the direction along the inner peripheral surface of the introduction pipe 10 on the downstream side of the holes 31a, 31b, 31c, and 31d.

 混合部40は、図8及び図9に示すように、液体導入部30の下流側に位置付けられる第3部材15内の液体導入部30と吐出部70との間であって、気体導入筒80の外面と導入管10の内面との間の気体導入空間10aに配設されている。
 具体的には、図8に示すように、混合部40は、気体導入空間10aにおいて、液体導入部30側の領域と吐出部70側の領域とに区分けする螺旋状(つる巻き線状)に連続して配された壁41が、導入管10の内面と一体に形成されることによって、液体導入部30側の領域と吐出部70側の領域とを連通する螺旋状の混合経路41aを形成している。
As shown in FIGS. 8 and 9, the mixing unit 40 is between the liquid introduction unit 30 and the discharge unit 70 in the third member 15 positioned on the downstream side of the liquid introduction unit 30, and includes a gas introduction cylinder 80. Is disposed in the gas introduction space 10 a between the outer surface of the gas and the inner surface of the introduction pipe 10.
Specifically, as illustrated in FIG. 8, the mixing unit 40 has a spiral shape (spiral winding) that is divided into a region on the liquid introduction unit 30 side and a region on the discharge unit 70 side in the gas introduction space 10 a. The continuously arranged wall 41 is formed integrally with the inner surface of the introduction tube 10 to form a spiral mixing path 41a that connects the region on the liquid introduction unit 30 side and the region on the discharge unit 70 side. is doing.

 混合経路41aの断面積は、液体導入部30側の導入管10の断面積よりも狭く設定されている。これにより、気体導入部20から導入された気体と、液体導入部30から導入された液体とが混在した混合液が、上記混合経路41aを通過する際に流速が速くなり、効率よく混合されながら、さらに第3部材15の軸15bに沿った螺旋状の旋回運動をするようになる。 The cross-sectional area of the mixing path 41a is set to be narrower than the cross-sectional area of the introduction pipe 10 on the liquid introduction part 30 side. As a result, a mixed liquid in which the gas introduced from the gas introducing part 20 and the liquid introduced from the liquid introducing part 30 are mixed is increased in flow velocity when passing through the mixing path 41a, and is efficiently mixed. In addition, a spiral turning motion along the axis 15b of the third member 15 is performed.

 なお、気体と液体が混在した混合液が旋回運動をする際には、前記実施例1で説明したように、旋回の外周側(導入管10の内面のある側)へと向かった遠心力により、外周側の圧力が高くなり、中心側(第3部材15の軸15bのある側)の圧力が低くなる。このとき発生する気泡の溶解と、キャビテーションによる気泡が発生することによって、気体が微細な気泡となる。 When the mixed liquid in which the gas and the liquid are mixed makes a swivel motion, as described in the first embodiment, the centrifugal force toward the outer periphery side of the swirl (the side where the inner surface of the introduction pipe 10 is located). The pressure on the outer peripheral side increases, and the pressure on the center side (the side where the shaft 15b of the third member 15 is present) decreases. The bubbles become fine bubbles by dissolving bubbles generated at this time and generating bubbles due to cavitation.

 混合部40の下流側では、前記混合部40によって第3部材15の延設方向の軸15bに沿った、混合液の渦巻きが形成されており、その渦巻きの略中心部分に、前記気体取り込み部80の第2の吐出部81dから排出された気体が合流する。
 このとき、渦巻きの略中心部分は、渦巻きの外径側部分と比べて圧力が低くなっており、気体導入部20の気体は大気圧よりも高圧であるので、第2の吐出部81dに混合液が逆流することなく、気体取り込み部80を経由した気体が効率よく導入管1に吸い込まれる。
 気体取り込み部80から導入管1に吸い込まれた気体は、混合部40による渦巻きに取り込まれる。このとき、気体取り込み部80の管81は小径に形成されているので、気体取り込み部580の第2の吐出部81dから排出される気体は、比較的小さな気泡であって、この小さな気泡が渦巻きに取り込まれることにより、微細な気泡となる。
On the downstream side of the mixing unit 40, a spiral of the mixed liquid is formed by the mixing unit 40 along the axis 15 b in the extending direction of the third member 15, and the gas intake unit is formed at a substantially central portion of the spiral. The gas discharged from the 80 second discharge part 81d merges.
At this time, the pressure in the substantially central portion of the spiral is lower than that in the outer diameter side portion of the spiral, and the gas in the gas introduction unit 20 is higher in pressure than the atmospheric pressure, so that it is mixed into the second discharge unit 81d. The gas passing through the gas intake part 80 is efficiently sucked into the introduction pipe 1 without the liquid flowing backward.
The gas sucked into the introduction pipe 1 from the gas intake part 80 is taken into the spiral by the mixing part 40. At this time, since the tube 81 of the gas intake unit 80 is formed with a small diameter, the gas discharged from the second discharge unit 81d of the gas intake unit 580 is a relatively small bubble, and the small bubble is swirled. It becomes a fine bubble by being taken in.

 衝突板60は、図7乃至図9及び図11に示すように、気体取り込み部80の第2の吐出部81dと吐出部70との間に配された板であって、導入管10の内面から第3部材15の軸15bに沿って延設されている。
 本実施例では、衝突板60は、第3部材15の横側内面から軸15bに向かって立ち上げられている。
 前記旋回した混合液は、気体取り込み部80からの気体を取り込んで、旋回を続けながら渦巻きとなって衝突板60に衝突する。このとき、微細な気泡とならなかった比較的大きな気泡や、気体取り込み部80からの気体がせん断されて、微細な気泡となる。それに加えて、混合液の旋回方向の流れは、衝突板60によって、吐出部70から液体中への放出される方向の流れに整流される。
As shown in FIGS. 7 to 9 and 11, the collision plate 60 is a plate disposed between the second discharge portion 81 d of the gas intake portion 80 and the discharge portion 70, and is an inner surface of the introduction pipe 10. To the third member 15 along the axis 15b.
In the present embodiment, the collision plate 60 is raised from the inner side surface of the third member 15 toward the shaft 15b.
The swirled mixed liquid takes in the gas from the gas intake unit 80 and collides with the collision plate 60 as a swirl while continuing swirling. At this time, a relatively large bubble that has not become a fine bubble or a gas from the gas intake unit 80 is sheared to become a fine bubble. In addition, the flow in the swirling direction of the mixed liquid is rectified by the collision plate 60 into a flow in a direction in which the mixed liquid is discharged into the liquid.

 また、本実施例では、気体取り込み部80を備えた構成を説明したが、これに限定されず、気体取り込み部80を備えない構成であっても良い。気体取り込み部80を備えない構成の場合には、導入管10には、気体導入部20からの圧送気体のみが導入される構成となるので、吐出部70から放出される微細気泡には、気体導入部20からの圧送気体のみが含まれ、導入管10の外部の気体が含まれないので、気体導入部20からの圧送気体のみの微細な気泡を発生させる要望に応じて選択されれば良い。 In the present embodiment, the configuration including the gas intake unit 80 has been described. However, the configuration is not limited thereto, and a configuration without the gas intake unit 80 may be used. In the case of a configuration that does not include the gas intake unit 80, only the pressure-feed gas from the gas introduction unit 20 is introduced into the introduction pipe 10, so that the fine bubbles released from the discharge unit 70 include gas Since only the pressurized gas from the introduction part 20 is included and the gas outside the introduction pipe 10 is not included, it may be selected according to the demand for generating fine bubbles of only the pressurized gas from the gas introduction part 20. .

(変形例1)
 微細気泡発生装置1は、実施例1の混合部40に、実施例2の気体導入筒80が組み合わされていても良い。このような構成であっても、上述した実施例1及び実施例2と同様の効果を得ることができる。
 すなわち、導入管10の気体導入部20から吐出部70にわたって内装されて気体導入筒80が配されており、さらに、その気体導入筒80の外面と導入管10の内面との間に形成された気体導入空間10aに、プロペラ状の羽根部材42a,42b,42cが形成されることにより、その羽根部材42a,42b,42c間に混合経路41aを有するものであっても良い。
 その他の構成については、上述した実施例1及び実施例2と同様であるので、その説明を省略する。
(Modification 1)
In the microbubble generator 1, the gas introduction tube 80 of the second embodiment may be combined with the mixing unit 40 of the first embodiment. Even with such a configuration, the same effects as those of the first and second embodiments can be obtained.
That is, the gas introduction cylinder 80 is arranged from the gas introduction part 20 to the discharge part 70 of the introduction pipe 10, and is further formed between the outer surface of the gas introduction cylinder 80 and the inner surface of the introduction pipe 10. Propeller-like blade members 42a, 42b, and 42c may be formed in the gas introduction space 10a to have a mixing path 41a between the blade members 42a, 42b, and 42c.
Since other configurations are the same as those of the first and second embodiments, the description thereof is omitted.

(変形例2)
 微細気泡発生装置1は、実施例2の混合部40に、実施例1の気体取り込み部50が組み合わされていても良い。このような構成であっても、上述した実施例1及び実施例2と同様の効果を得ることができる。
 すなわち、液体導入部30側の領域と吐出部70側の領域とに区分けする螺旋状(つる巻き線状)に連続して配された壁41が、導入管10の内面と一体に形成されることによって、液体導入部30側の領域と吐出部70側の領域とを連通する螺旋状の混合経路41aを形成し、そのような構成の混合部40と吐出部70との間に、該導入管10の外部の気体を取り込む気体取り込み部50の管52の他端52bの開口52dが連通していても良い。
 その他の構成については、上述した実施例1及び実施例2と同様であるので、その説明を省略する。
(Modification 2)
In the microbubble generator 1, the gas intake section 50 of the first embodiment may be combined with the mixing section 40 of the second embodiment. Even with such a configuration, the same effects as those of the first and second embodiments can be obtained.
That is, the wall 41 continuously arranged in a spiral shape (spiral winding) divided into a region on the liquid introduction unit 30 side and a region on the discharge unit 70 side is formed integrally with the inner surface of the introduction tube 10. Thus, a spiral mixing path 41a that connects the region on the liquid introduction unit 30 side and the region on the discharge unit 70 side is formed, and the introduction is performed between the mixing unit 40 and the discharge unit 70 having such a configuration. The opening 52d of the other end 52b of the pipe 52 of the gas intake part 50 for taking in the gas outside the pipe 10 may be communicated.
Since other configurations are the same as those of the first and second embodiments, the description thereof is omitted.

実施例1による微細気泡発生装置の外観斜視図である。1 is an external perspective view of a fine bubble generator according to Embodiment 1. FIG. (a)は、実施例1による微細気泡発生装置の内部構造を示す斜視図であって、(b)は、羽根部材と連結部材の構成を示す斜視図である。(A) is a perspective view which shows the internal structure of the microbubble generator by Example 1, (b) is a perspective view which shows the structure of a blade member and a connection member. 第1図A-A線による縦断面図である。FIG. 1 is a longitudinal sectional view taken along line AA in FIG. 第3図B-B線による端面図である。FIG. 3 is an end view taken along line BB in FIG. 第3図C-C線による端面図である。FIG. 3 is an end view taken along the line CC in FIG. 第3図D-D線による縦断面図である。FIG. 3 is a longitudinal sectional view taken along line DD in FIG. 実施例2による微細気泡発生装置の外観斜視図である。It is an external appearance perspective view of the microbubble generator by Example 2. FIG. 実施例2による微細気泡発生装置の内部構造を示す斜視図である。It is a perspective view which shows the internal structure of the microbubble generator by Example 2. FIG. 第7図E-E線による縦断面図である。FIG. 7 is a longitudinal sectional view taken along line EE. 第9図F-F線による端面図である。FIG. 9 is an end view taken along line FF. 第9図G-G線による端面図である。FIG. 9 is an end view taken along line GG. 第9図H-H線による縦断面図である。FIG. 9 is a longitudinal sectional view taken along line HH. 第9図I-I線による縦断面図である。FIG. 9 is a longitudinal sectional view taken along line II. 第9図J-J線による断面図である。FIG. 9 is a sectional view taken along line JJ.

符号の説明Explanation of symbols

1 微細気泡発生装置
10 導入管
11 導入管の一端
12 導入管の他端
13 第1部材
13b 第1部材の軸
14 第2部材
14b 第2部材の軸
15 第3部材
15b 第3部材の軸
20 気体導入部
30 液体導入部
31 液体導入部の穴
32 導入部材
33 開口
40 混合部
41a,41b,41c 混合経路
42a 羽根部材
42b 羽根部材
42c 羽根部材
50 気体取り込み部
53 連結部材
53a 内部領域
53b 開口
53c 面
53d 面
53e 面
60 衝突板
70 吐出部
DESCRIPTION OF SYMBOLS 1 Fine bubble generator 10 Introducing pipe 11 One end 12 of introducing pipe 13 Other end 13 of introducing pipe First member 13b First member shaft 14 Second member 14b Second member shaft 15 Third member 15b Third member shaft 20 Gas introduction part 30 Liquid introduction part 31 Liquid introduction part hole 32 Introduction member 33 Opening 40 Mixing part 41a, 41b, 41c Mixing path 42a Blade member 42b Blade member 42c Blade member 50 Gas intake part 53 Connecting member 53a Internal region 53b Opening 53c Surface 53d Surface 53e Surface 60 Collision plate 70 Discharge part

Claims (8)

 圧送された気体を微細な気泡にして液体中に放出する微細気泡発生装置であって、
 圧送された気体を導入する気体導入部が一端側に設けられ、液体中に配されるとともに前記導入した気体を液体中に放出する吐出部が他端側に設けられた筒状の導入管と、
 前記液体を導入管の内部に導入する液体導入部と、
 前記導入管内にて、液体導入部と吐出部の間に配され、前記導入管内に導入された気体と液体とを混合させる混合部と、
 前記導入管内の混合部と吐出部の間に配され、混合部で混合された気体と液体が衝突する衝突板と
 を備えたことを特徴とする微細気泡発生装置。
A fine bubble generating device that discharges compressed gas into a liquid into fine bubbles,
A cylindrical introduction pipe provided with a gas introduction part for introducing the pumped gas on one end side, disposed in the liquid and having a discharge part for releasing the introduced gas into the liquid on the other end side; ,
A liquid introduction part for introducing the liquid into the introduction tube;
In the introduction tube, a mixing unit that is disposed between the liquid introduction unit and the discharge unit, and mixes the gas and the liquid introduced into the introduction tube;
A fine bubble generating apparatus, comprising: a collision plate disposed between a mixing unit and a discharge unit in the introduction pipe and colliding with a gas and a liquid mixed in the mixing unit.
 液体導入部は、
 導入管の外面から内面に貫通した穴と、該穴と連通して導入管内に配されるとともに前記穴よりも混合部寄りの位置で開口する導入部とからなり、
 前記導入管内を気体が通過する際に生じる負圧により、前記導入部から導入管内に液体が取り込まれる
 ことを特徴とする請求項1に記載の微細気泡発生装置。
The liquid inlet is
A hole penetrating from the outer surface to the inner surface of the introduction tube, and an introduction portion that is arranged in the introduction tube in communication with the hole and opens at a position closer to the mixing portion than the hole,
The fine bubble generating device according to claim 1, wherein a liquid is taken into the introduction pipe from the introduction section due to a negative pressure generated when a gas passes through the introduction pipe.
 混合部は、
 液体導入部側の領域と吐出部側の領域とに区分けする複数枚の羽根部材と、
 それぞれの羽根部材の間に設けられ、前記液体導入部側の領域と吐出部側の領域とを連通する混合経路とで構成され、
 該混合経路は、液体導入部側の導入管の断面積よりも狭い断面積を有し、
 導入管内に導入された気体と液体とが、断面積の狭い混合経路を通過する際に効率良く混合される
 ことを特徴とする請求項1に記載の微細気泡発生装置。
The mixing section
A plurality of blade members that are divided into a region on the liquid introduction unit side and a region on the discharge unit side;
It is provided between each blade member, and is composed of a mixing path that communicates the region on the liquid introduction part side and the region on the discharge part side,
The mixing path has a cross-sectional area narrower than the cross-sectional area of the introduction pipe on the liquid introduction part side,
The fine bubble generator according to claim 1, wherein the gas and the liquid introduced into the introduction pipe are efficiently mixed when passing through a mixing path having a narrow cross-sectional area.
 混合部は、
 液体導入部側の領域と吐出部側の領域とに区分けする螺旋状に連通するとともに、
 液体導入部側の導入管の断面積よりも狭い断面積を有し、
 導入管内に導入された気体と液体とが、断面積の狭い混合経路を通過する際に効率良く混合される
 ことを特徴とする請求項1に記載の微細気泡発生装置。
The mixing section
While communicating in a spiral shape divided into a region on the liquid introduction unit side and a region on the discharge unit side,
Having a cross-sectional area narrower than the cross-sectional area of the introduction pipe on the liquid introduction part side,
The fine bubble generator according to claim 1, wherein the gas and the liquid introduced into the introduction pipe are efficiently mixed when passing through a mixing path having a narrow cross-sectional area.
 混合部は、
 液体導入部側の領域と吐出部側の領域とに区分けする複数枚の羽根部材と、
 それぞれの羽根部材の間に設けられ、前記液体導入部側の領域と吐出部側領域とを連通する混合経路とで構成され、
 該混合経路は、液体導入部側の導入管の断面積よりも狭い断面積を有し、
 導入管内に導入された気体と液体とが、断面積の狭い混合経路を通過する際に効率良く混合される
 ことを特徴とする請求項2に記載の微細気泡発生装置。
The mixing section
A plurality of blade members that are divided into a region on the liquid introduction unit side and a region on the discharge unit side;
It is provided between each blade member, and is composed of a mixing path that communicates the region on the liquid introduction unit side and the region on the discharge unit side,
The mixing path has a cross-sectional area narrower than the cross-sectional area of the introduction pipe on the liquid introduction part side,
The fine bubble generator according to claim 2, wherein the gas and the liquid introduced into the introduction pipe are efficiently mixed when passing through a mixing path having a narrow cross-sectional area.
 混合部は、
 液体導入部側の領域と吐出部側の領域とに区分けする螺旋状に連通するとともに、
 液体導入部側の導入管の断面積よりも狭い断面積を有し、
 導入管内に導入された気体と液体とが、断面積の狭い混合経路を通過する際に効率良く混合される
 ことを特徴とする請求項2に記載の微細気泡発生装置。
The mixing section
While communicating in a spiral shape divided into a region on the liquid introduction unit side and a region on the discharge unit side,
Having a cross-sectional area narrower than the cross-sectional area of the introduction pipe on the liquid introduction part side,
The fine bubble generator according to claim 2, wherein the gas and the liquid introduced into the introduction pipe are efficiently mixed when passing through a mixing path having a narrow cross-sectional area.
 導入管外部の気体を導入管内の混合部と吐出部との間に取り込む気体取り込み部を備えた
 ことを特徴とする請求項1乃至請求項6のいずれかに記載の微細気泡発生装置。
The fine bubble generator according to any one of claims 1 to 6, further comprising a gas intake unit that takes in gas outside the introduction tube between the mixing unit and the discharge unit in the introduction tube.
 導入管内には、該導入管の気体導入部から吐出部にわたる長さの気体導入筒が内装されており、
 前記気体導入筒は、導入管の気体導入部側と同一の端部に気体取り込み部を有するとともに、導入管の吐出部側と同一の端部に第2の吐出部を有した細い筒状に形成され、
 前記気体導入筒の外面と導入管の内面との間に気体導入部から吐出部にわたる気体導入空間を形成し、
 混合部は、気体導入筒の外面と導入管の内面との間の気体導入空間に配設され、第2の吐出部は、混合部と衝突板との間に開口している
 ことを特徴とする請求項1乃至請求項6のいずれかに記載の微細気泡発生装置。

 
In the introduction pipe, a gas introduction cylinder having a length extending from the gas introduction part to the discharge part of the introduction pipe is internally provided,
The gas introduction cylinder has a gas intake part at the same end as the gas introduction part side of the introduction pipe, and a thin cylinder shape having a second discharge part at the same end as the discharge part side of the introduction pipe. Formed,
Forming a gas introduction space extending from the gas introduction part to the discharge part between the outer surface of the gas introduction cylinder and the inner surface of the introduction pipe;
The mixing portion is disposed in a gas introduction space between the outer surface of the gas introduction tube and the inner surface of the introduction tube, and the second discharge portion is opened between the mixing portion and the collision plate. The fine bubble generator according to any one of claims 1 to 6.

PCT/JP2008/073879 2008-12-30 2008-12-30 Microbubble generation device Ceased WO2010076843A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
PCT/JP2008/073879 WO2010076843A1 (en) 2008-12-30 2008-12-30 Microbubble generation device
PCT/US2009/069844 WO2010078442A2 (en) 2008-12-30 2009-12-30 Toxic substance removal method, toxic substance removal apparatus and mixing and/or bubble generating device adapted for use with the toxic substance removal apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/JP2008/073879 WO2010076843A1 (en) 2008-12-30 2008-12-30 Microbubble generation device

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Cited By (2)

* Cited by examiner, † Cited by third party
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JP2014155924A (en) * 2014-04-10 2014-08-28 Mitsubishi Electric Corp Fixed swirler, air bubble generation device using the same and bath hot water supply apparatus
JP2014168760A (en) * 2013-03-05 2014-09-18 Mitsubishi Electric Corp Fine bubble generation device and bath hot water supply device

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JP2014168760A (en) * 2013-03-05 2014-09-18 Mitsubishi Electric Corp Fine bubble generation device and bath hot water supply device
JP2014155924A (en) * 2014-04-10 2014-08-28 Mitsubishi Electric Corp Fixed swirler, air bubble generation device using the same and bath hot water supply apparatus

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