WO2013012069A1 - 気泡発生機構及び気泡発生機構付シャワーヘッド - Google Patents

気泡発生機構及び気泡発生機構付シャワーヘッド Download PDF

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Publication number
WO2013012069A1
WO2013012069A1 PCT/JP2012/068480 JP2012068480W WO2013012069A1 WO 2013012069 A1 WO2013012069 A1 WO 2013012069A1 JP 2012068480 W JP2012068480 W JP 2012068480W WO 2013012069 A1 WO2013012069 A1 WO 2013012069A1
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WO
WIPO (PCT)
Prior art keywords
collision
flow
cross
throttle
generating mechanism
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/JP2012/068480
Other languages
English (en)
French (fr)
Japanese (ja)
Inventor
啓雄 加藤
芳樹 柴田
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.)
Shibata Corp
Original Assignee
Shibata Corp
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 Shibata Corp filed Critical Shibata Corp
Priority to JP2013524754A priority Critical patent/JP5712292B2/ja
Priority to KR1020147001715A priority patent/KR20140048940A/ko
Priority to EP12814186.8A priority patent/EP2735363A4/en
Priority to CN201280036169.1A priority patent/CN103747858B/zh
Priority to US14/234,032 priority patent/US9370784B2/en
Publication of WO2013012069A1 publication Critical patent/WO2013012069A1/ja
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/14—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with multiple outlet openings; with strainers in or outside the outlet opening
    • B05B1/18—Roses; Shower heads
    • B05B1/185—Roses; Shower heads characterised by their outlet element; Mounting arrangements therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2373—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media for obtaining fine bubbles, i.e. bubbles with a size below 100 µm
    • B01F23/2375—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media for obtaining fine bubbles, i.e. bubbles with a size below 100 µm for obtaining bubbles with a size below 1 µm
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/441—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits
    • B01F25/4412—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits the slits being formed between opposed planar surfaces, e.g. pushed again each other by springs
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/441—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits
    • B01F25/4416—Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits the opposed surfaces being provided with grooves
    • B01F25/44163—Helical grooves formed on opposed surfaces, e.g. on cylinders or cones
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40—Static mixers
    • B01F25/44—Mixers in which the components are pressed through slits
    • B01F25/442—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation
    • B01F25/4422—Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation the surfaces being maintained in a fixed but adjustable position, spaced from each other, therefore allowing the slit spacing to be varied
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/14—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with multiple outlet openings; with strainers in or outside the outlet opening
    • B05B1/18—Roses; Shower heads

Definitions

  • the present invention relates to a bubble generation mechanism, particularly a mechanism suitable for generating fine bubbles such as microbubbles and nanobubbles, and a shower head using the mechanism.
  • Bubbles formed in the water are classified into millibubbles or microbubbles (further, micro / nano bubbles, nano bubbles, etc.) depending on their sizes. Millibubbles are huge bubbles to some extent, which rise rapidly in water and eventually rupture and disappear at the surface of the water. On the other hand, bubbles with a diameter of 50 ⁇ m or less are fine, so they have a long residence time in water and are excellent in gas dissolving ability, so they further shrink in water, and finally disappear in water ( It has a special property of completely dissolving), and it is becoming common to call this microbubble (Non-patent Document 1).
  • fine bubbles refers to a concept that collectively refers to micro-nano bubbles (diameter: 10 nm or more and less than 1 ⁇ m) and nano bubbles (diameter: less than 10 nm) having a smaller diameter in addition to the micro bubbles.
  • Patent Documents 1 to 5 various shower devices incorporating a bubble generation mechanism have been proposed for use in bathrooms.
  • the bubble generating mechanism incorporated in the shower apparatus disclosed in these patent documents is formed in the wing body shaft portion in the swirl flow generating wing body incorporated in the head portion for ejecting the shower water flow and the vortex formed by the wing body.
  • a method of entraining outside air sucked in from the fine pores into a gas-liquid mixture referred to as Patent Document 1: Two-phase flow swirl method
  • a venturi in the shower body the handle portion extending from the head portion.
  • a cavitation system that incorporates a throttle mechanism such as a pipe and deposits air dissolved in water as fine bubbles due to the pressure reduction effect caused by Bernoulli's principle when water passes through the throttle mechanism at a high flow rate ( It is roughly classified into Patent Documents 2 to 5).
  • JP 2008-229516 A JP 2008-73432 A JP 2007-209509 A JP 2007-50341 A JP 2006-116518 A Internet homepage (http://unit.aist.go.jp/emtech-ri/26env-fluid/takahashi.pdf#search 'Research on microbubbles and nanobubbles')
  • the shower apparatus disclosed in Patent Documents 2 to 4 adopting the cavitation method has only one closed throttle hole around the venturi pipe or orifice, and the flow path portion is provided at the throttle hole position. Has a structure that does not exist. For this reason, the flow velocity does not increase as expected when the fluid resistance when passing through the throttle hole is increased, and the radial pressure from the inner wall surface of the hole is easily received in the throttle hole, so that the cavitation (decompression) effect is achieved. There is a drawback that the amount of bubble deposition tends to be insufficient.
  • An object of the present invention is to generate a sufficient amount of bubbles without using a complicated gas-liquid mixing mechanism. As a result, the amount of bubbles generated in the microbubble region or the micro / nanobubble region can be reduced to a level that could not be achieved conventionally.
  • An object of the present invention is to provide a bubble generation mechanism that can be enhanced and a shower head using the same.
  • the bubble generation mechanism of the present invention is: A flow path connecting the inlet opening at the inflow end and the outlet opening at the outflow end is formed in a penetrating form with respect to the member body in which the inflow end on the liquid inflow side and the outflow end on the liquid outflow side are defined.
  • a throttle part having a smaller flow cross-sectional area than the inlet is formed in the middle of the flow path, and the throttle part is configured to divide the axial cross section of the flow path into three or more segment regions at the throttle part.
  • the collision part is further arranged to further reduce the flow path cross-sectional area of After the gas-dissolved liquid flow supplied to the inflow end of the member body collides with the collision part, it is passed through the segment area while increasing the speed, and the dissolved gas is precipitated by the decompression effect to contain bubbles. It is characterized by being made out of liquid and flowing out from the outlet.
  • the liquid supplied to the flow path is squeezed by the throttle portion and the flow velocity is increased.
  • a negative pressure region is formed in the throttle portion (and its downstream side), and dissolved gas (for example, air) in the water flow is precipitated due to the cavitation (decompression) effect, and bubbles are generated.
  • bubbles in water are likely to coalesce even if they collide with each other.
  • the flow velocity of the passing water flow is insufficient just by passing through a well-known throttle mechanism such as a venturi tube.
  • the pressure reduction level is small and the degree of vortex generation is small.
  • such a throttle mechanism has a structure in which the flow path cross-section is reduced in a similar manner at the throttle, so if the cross-section of the throttle is reduced excessively to increase the flow velocity, the fluid passage resistance increases. Therefore, the increase in the flow rate corresponding to the cross-sectional reduction ratio cannot be expected, and the bubble generation efficiency is decreased. Therefore, the amount of bubble deposition due to cavitation is small, and the collision to the extent that the bubbles are crushed cannot be caused sufficiently, so that the fine bubbles cannot be sufficiently formed.
  • a colliding portion that further reduces the flow passage cross-sectional area of the restriction portion is arranged in a form in which the axial cross section of the flow passage is partitioned into three or more segment regions at the restriction portion.
  • the area where the liquid can flow can be In other words, the cross section of the flow path is reduced in a direction that is thinned out.
  • the fluid resistance at the throttle portion does not increase excessively, and the effect of increasing the flow velocity and thus the effect of generating negative pressure can be greatly increased.
  • region (and its downstream) is improved significantly, for example, even if it is a water flow with the same dissolved air density
  • the fluid flowing into the segment area mainly flows around the tip of the collision portion, and the flow near the center of the cross section where the flow velocity becomes the highest tends to be decelerated due to the bypass. .
  • a cross-sectional central flow that is relatively high speed with respect to the cross-sectional peripheral flow is passed between the tip portions of two or more of the plurality of collision portions that protrude toward the central cross-section of the throttle portion. It is effective to form a high-speed flow gap.
  • the flow near the center of the cross section can be passed through the high-speed flow gap without greatly decelerating, and the high-speed flow can be used particularly effectively for the generation of fine bubbles.
  • the high-speed flow gap can be formed in various forms. For example, a cone-shaped portion that reduces the axial cross section toward the tip of the collision portion is formed at the tip of the collision portion, and a high-speed flow gap is formed between the outer peripheral surfaces of the cone-shaped portions in the two collision portions adjacent to each other across the segment region A slit portion to be formed can be formed. Since the slit portion is formed in the direction of the outer peripheral surface bus of the conical portion, the flow toward the slit portion is squeezed and compressed so as to overcome the bulge along the bus of the conical portion.
  • the cavitation generation region is formed in a point shape in the vicinity of the center of the throttle, but in the above configuration, the cavitation generation region is formed in a linear shape along the slit portion. The area is greatly expanded, and a large amount of fine bubbles can be deposited.
  • At least one pair of a plurality of collision parts is arranged in a shape facing the inner diameter direction across the center of the cross section of the throttle part, and a central gap constituting a high-speed flow gap is formed between the tips of the collision parts
  • the flow at the center of the cross section is further narrowed down by the passage of the center gap to increase the speed, but the flow detour to the segment area side is allowed, so the increase in fluid resistance is effectively suppressed, and cavitation (decompression) Since the effect is greatly enhanced and the flow velocity at the center of the cross section can be greatly increased, a larger amount of fine bubbles can be deposited.
  • the collision parts can be provided in a cross shape in which the projecting directions are orthogonal to each other in the axial section of the diaphragm part, and the diaphragm part can be divided into four diaphragm segment regions by these collision parts.
  • the collision parts By arranging the collision parts in directions perpendicular to each other and dividing them into four diaphragm segment areas, the object of placement of the collision parts and the diaphragm segment areas with respect to the center of the cross section is also improved, and the individual diaphragm segment areas are more homogeneous. Fine bubbles can be deposited.
  • a cross-sectional central flow that is relatively high speed with respect to the cross-sectional peripheral flow is passed between the tip portions of two or more of the plurality of collision portions that protrude toward the central cross-section of the throttle portion.
  • a high-speed flow gap can be formed.
  • the four collision portions can be provided so as to protrude from the inner peripheral surface of the flow channel toward the central portion of the flow channel.
  • a high-speed flow is generated between the outer peripheral surfaces of the cone-shaped portions in the collision portions adjacent to each other across the segment region.
  • the slit part which comprises a gap can be formed.
  • a central gap that constitutes a part of the high-speed flow gap is formed between the tips of the collision portions that are arranged opposite to each other in the inner diameter direction across the center of the cross section of the throttle portion.
  • the part is formed in a cross shape integrated through a central gap.
  • the flow at the center of the cross section at the highest flow velocity is effectively restricted by the four conical portions arranged so as to surround the center of the cross section, and flows into the center gap while being accelerated.
  • the surrounding four slit portions communicate with the center gap, and the flow that is squeezed and compressed in the center gap is extremely effectively suppressed from increasing the fluid resistance by detouring to the slit portion, and Since it is squeezed by the slit, the decrease in the flow velocity at the detour destination can be kept low.
  • the cavitation (decompression) effect is extremely active not only in the center gap but also in the slit portion, and nanobubble-level fine bubbles can be generated at a high concentration.
  • the tip of the collision part facing the center gap, the flow passing through the vicinity can be particularly speeded up, and the bubble miniaturization becomes more remarkable.
  • the tip of the collision part can be formed flat, and in this case, the expansion of the central gap and the uniform flow contribute to an improvement in the generation density of the fine bubbles as a whole.
  • the collision part is disposed so as to face the inner diameter direction across the center of the cross section of the throttle part in a form orthogonal to the main collision part and a main collision part arranged so as to cross the cross section of the throttle part along the inner diameter.
  • a pair of opposing collision portions that form an outer peripheral gap that forms a high-speed flow gap may be provided between the front end surface and the outer peripheral surface of the main collision portion.
  • the outer peripheral gap can be formed in a slit shape, and the cavitation region can be expanded in the slit longitudinal direction.
  • fine bubbles can be generated at a higher concentration.
  • the main collision part is opposed to the pair of collision parts each having a flat tip surface in the inner diameter direction of the throttle part by forming a central gap including the cross-sectional center of the throttle part between the tip surfaces. It is also possible to arrange them.
  • the flow that is compressed is diverted to the slit-shaped outer peripheral gap, so that an increase in fluid resistance is extremely effectively suppressed. Further, since the outer peripheral gap is also narrowed in a slit shape, a decrease in flow velocity at the detour destination can be suppressed to a low level. As a result, the cavitation (decompression) effect is extremely active even in the center gap and the slit portion, and nanobubble-level fine bubbles can be generated at a high concentration.
  • each of the main collision portions has a flat tip surface and a pair of impact portions each having a chamfered portion formed along the outer periphery of the tip surface. It can be configured to be arranged and formed facing the direction.
  • the outer periphery gap is formed so that the tip of the opposing collision portion faces the groove portion of the V-shaped cross section formed by the chamfered portions of the two collision portions forming the main collision portion, the above-described opposing collision portion It is possible to further enhance the bubble refinement effect by increasing the flow velocity near the tip.
  • a plurality of circumferential throttle ribs can be formed on the outer peripheral surface of the collision part along the protruding direction of the collision part.
  • the gas-dissolved liquid flowing in the tangential direction of the outer peripheral surface of the collision portion is further squeezed in the groove portion (or valley-like portion) between the restricting ribs, and the pressure reduction effect is enhanced.
  • the flow on the valley opening side is relatively slow, and the pressure is particularly high with respect to the high-speed flow on the valley bottom side.
  • the gas saturation dissolution amount of the liquid on the valley opening side increases, the saturation dissolution amount on the valley bottom side decreases, and the dissolution liquid flows to the valley bottom side, so that bubbles can be precipitated extremely actively.
  • the valley-shaped part has a shape that decreases in width toward the valley, it is desirable to enhance the flow restricting effect in the valley-like part and the bubble precipitation effect.
  • the plurality of throttle ribs in the valley portion are formed adjacent to each other with the apex portion having an acute angle.
  • the apex angle of the aperture rib is preferably set to 60 ° or less and 20 ° or more from the viewpoint of optimizing the above effect.
  • Multiple winding ribs can be integrally formed in a spiral. In this way, formation of the throttle rib is facilitated, and the throttle rib is inclined with respect to the flow, so that the flow component crossing the ridge line portion of the throttle rib increases, and the turbulent flow generation effect accompanying flow separation becomes remarkable. Therefore, the bubbles can be further miniaturized.
  • the collision part is formed with a screw member whose leg end side protrudes into the flow path, the thread formed on the outer peripheral surface of the leg part of the screw member can be used as a throttle rib, and manufactured. Is easy.
  • the member body can be coaxially mounted inside the tube member by forming the outer peripheral surface into a cylindrical surface.
  • a portion of the pipe member positioned upstream of the inflow end of the member main body forms a liquid supply conduit
  • a portion of the tube member positioned downstream of the outflow end forms a liquid recovery conduit.
  • the liquid supply conduit and the liquid recovery conduit can be formed collectively with a single tube member, so that the number of parts can be reduced.
  • a ring-shaped seal member is provided between the outer peripheral surface of the member main body and the inner peripheral surface of the pipe member to seal the space between the outer peripheral surface and the inner peripheral surface.
  • the member main body is formed as a columnar member in which the end surfaces of the inflow end side and the outflow end side are flat surfaces orthogonal to the axis of the outer peripheral surface, it is easy to manufacture and can be attached to the tube member. It is convenient because it is simple.
  • an inflow side taper portion that expands toward the inflow port can be formed on the inflow side of the flow path.
  • the flow velocity at the throttle portion can be further increased, and the bubble generation effect can be enhanced.
  • the outflow side taper part which diameter-expands toward this outflow port can also be formed in the outflow side of a flow path with a collision part.
  • a constant cross-sectional portion having a constant flow cross-sectional area is formed as a throttle portion between the inflow side taper portion and the outflow side taper portion of the flow path with a collision portion, and the collision portion is disposed in the constant cross-section portion. If this is done, the flow accelerated by the inflow side taper can be stabilized at the constant cross-section, and can be led to the collision portion and thus the flow passage cross-sectional area reduction portion, so that bubbles can be generated more stably. .
  • the present invention also provides a shower head using the bubble generating mechanism of the present invention.
  • the shower head includes the bubble generating mechanism of the present invention.
  • a water flow supply unit for supplying a water flow to the inflow end of the member body of the bubble generating mechanism;
  • a water jet unit that jets the bubble-containing liquid collected at the outflow end of the member main body as a shower water flow.
  • a shower water flow containing a larger amount of bubbles can be easily formed even with a water flow having the same dissolved air concentration.
  • dissolved air is bubbled by precipitation under reduced pressure, the dissolved oxygen concentration of bulk water (or dissolved chlorine concentration in the case of tap water, etc.) is reduced, and oxygen (or chlorine) for the skin and hair in contact with the shower water flow Can be effectively reduced.
  • the figure which shows the 6th modification of a collision part The figure which shows the 7th modification of a collision part.
  • the figure which shows the 9th modification of a collision part The figure which shows the 10th modification of a collision part.
  • the figure which shows the 14th modification of a collision part The schematic diagram which shows another utilization form of the bubble generation mechanism of this invention.
  • the second figure. The third figure.
  • the sixth figure. The seventh figure.
  • FIG. 1 shows the appearance of a shower device with a bubble generating mechanism (hereinafter also simply referred to as “shower device”) 100 according to an embodiment of the present invention, along with its internal structure cross section.
  • the shower apparatus 100 includes a hand grip portion 101, a shower main body 100M having a head portion 100H integrated at the tip thereof, and a bubble generation engine (bubble generation mechanism) 1 incorporated in the shower main body 100M.
  • the shower main body 100M is configured as an integral plastic molded product.
  • the bubble generation engine 1 is accommodated in the cylindrical grip 101. Specifically, the cylindrical bubble generating engine 1 is inserted coaxially from the rear end side opening of the grip portion 101, and the outer peripheral edge of the front end surface is formed on the front end side of the inner peripheral surface of the grip portion 101. It is stopped by the part 101a.
  • the member body 6 is made of resin (may be made of metal), has an outer peripheral surface formed in a cylindrical shape, and is coaxially mounted on the inside of the grip portion (tube member) 101. More specifically, the member main body 6 is formed as a columnar member in which the end surfaces on the inflow end side and the outflow end side are flat surfaces orthogonal to the axis of the outer peripheral surface.
  • a portion of the grip portion 101 located upstream from the inflow end of the member main body 6 is a liquid supply conduit, and a portion located downstream of the outflow end is a liquid recovery conduit (injection restricting portion 101b). ) Is formed. Between the outer peripheral surface of the member main body 6 and the inner peripheral surface of the grip portion (tube member) 101, a ring-shaped seal member 8 that seals between the outer peripheral surface and the inner peripheral surface in a liquid-tight manner may be disposed. The flow leaking to the outer peripheral surface side of the member main body 6 is prevented.
  • a threaded portion 104 c is formed at the rear end of the gripping portion 101, and a hose connecting portion 103 is screwed and coupled thereto via a seal ring 104.
  • a shower hose (not shown) is screwed and attached to the screw portion 103t formed in the hose connection portion 103, and a water flow is supplied into the grip portion 101 via the shower hose.
  • the inner peripheral surface of the gripping portion 101 has a tapered throttle portion 101b at a portion located in front of the front end surface of the bubble generating engine 1 fixed by the step portion 101a.
  • the water flow that has passed through the bubble generating engine 1 is supplied to the shower main body 101M integrated in a communicating form with the tip end side of the gripping portion 101 while being accelerated by the throttle portion 101b. It is jetted as a shower water stream from (a plurality of water jet nozzles 109h are dispersedly formed).
  • the head portion 100H is screwed by a screw portion 108t via a seal ring 114 to a back body 107 integrated with the gripping hand portion 101 and a screw portion 107t formed on the opening periphery of the back body 108.
  • a water jet unit 102 The passing water flow of the bubble generating engine 1 enters the head portion 100H through the throttle portion 101b and is jetted from the water spray plate 109.
  • FIG. 2 is an enlarged view showing the bubble generation engine 1 taken out.
  • the member body 6 is formed with a passage 2 connecting the inlet 2n opening at the inflow end and the outlet 2x opening at the outflow end in a penetrating form, and flows in the middle of the channel 2 from the inlet 2n.
  • a narrowed portion 2c having a small cross-sectional area is formed.
  • the throttle section 2c further reduces the channel cross-sectional area of the throttle section 2c by dividing the axial section of the flow path 3 into three or more, in this embodiment, four segment regions 2e.
  • the collision part 3 to be made is arranged.
  • Each collision portion 3 is configured as a screw member, and as shown in FIG.
  • Each segment region 2e is formed such that the flow path cross-sectional areas are equal to each other.
  • the water (hot water) supplied to the shower device is a gas-dissolved liquid in which air is dissolved.
  • the flow of the gas-dissolved liquid supplied to the inflow end of the member main body 6 collides with the collision portion 3 and then passes while being distributed to each segment region 2 e. Then, due to the pressure reducing effect, the dissolved gas in the gas-dissolved liquid is deposited as bubbles, becomes a bubble-containing liquid, and is ejected as a shower water flow from the head portion 100H of FIG.
  • High-speed flow gaps 2g and 2k for passing the central flow are formed.
  • a conical portion 5t that reduces the axial cross section toward the distal end is formed at the distal end portion of the collision portion 3 (in this embodiment, it is conical, but other conical shapes such as a quadrangular pyramid and a hexagonal pyramid are formed.
  • a slit portion 2g constituting a high-speed flow gap is formed between the outer peripheral surfaces of the conical portions 5t.
  • a center gap 2k constituting a high-speed flow gap is formed between the tips of the four collision portions 3 facing each other in the inner diameter direction across the center of the section of the throttle portion 2c.
  • the collision portions 3 are provided in a cross shape in which the projecting directions are orthogonal to each other in the axial section of the restriction portion 2c.
  • the collision portions 3 cause the restriction portions to be divided into four restriction segment regions 2e. It is divided.
  • the four collision portions 3 protrude from the inner peripheral surface of the flow channel 2 toward the central portion of the flow channel 2.
  • four slit parts 2g are formed between the outer peripheral surfaces of the cone-shaped part 5t, and the collision part 3 arranged opposite to the inner diameter direction is formed.
  • a central gap 2k is formed between the tips.
  • the high-speed flow gap is formed in a cross shape in which the four slit portions 2g are integrated via the center gap 2k.
  • a plurality of circumferential restriction ribs 5 r are formed on the outer peripheral surface of each collision portion 3 along the protruding direction of the collision portion 3.
  • the valley-shaped portion 21 has a shape in which the width is reduced toward the valley low.
  • the plurality of diaphragm ribs 5r are formed adjacent to each other with the apex being an acute angle.
  • the apex angle of the aperture rib 5r is set to 60 ° or less and 20 ° or more, for example.
  • the collision portion 3 is a screw member, and the plurality of winding ribs 5r are integrally formed in a spiral shape.
  • a shower hose (not shown) is attached to the hose connection part 103 of the shower head 100, and a water flow is supplied through the shower hose.
  • the water flow from the hose connection portion 103 passes through the bubble generation engine 1 in the grip portion 101, and is further supplied to the shower main body 101M via the throttle portion 101b.
  • the water flow is injected as a shower water flow from the water flow injection portion 102 having the water spray plate 109. Is done.
  • the bubble generation engine 1 does not reduce the cross-sectional area of the flow path 2 in the throttle portion 2 c in a similar manner in the radial direction toward the cross-sectional center O where the flow velocity is high, By using it as an obstacle, the region through which the liquid can flow is reduced in the form of thinning out in the circumferential direction with respect to the center of the cross section. As a result, the fluid resistance at the throttle portion 2c does not increase excessively, and the effect of increasing the flow velocity and thus the effect of generating negative pressure can be greatly increased.
  • a constricted portion 2c is formed as a constant cross section, and the collision portion 3 is disposed in the constant cross section 2c.
  • the stabilized flow can be guided to the collision portion 3 while being stabilized by the constant cross-section portion 2c, and bubbles can be generated more stably.
  • the flow in the vicinity of the center of the cross section where the flow velocity is the largest is distributed to each segment region 2e, bypassing the tip portion of the collision portion 3.
  • the high-speed flow gaps 2g and 2k are formed between the front end portions of the collision portion 3, the high flow velocity near the center of the cross section passes through the high-speed flow gaps 2g and 2k without significantly decelerating. it can.
  • the cavitation effect due to the passing water flow is remarkably enhanced, and the generation of the generated bubbles becomes extremely remarkable.
  • the slit portion 2g formed between the tip portions (cone portions) 5t and 5t of the collision portion 3 adjacent to each other across the segment region 2e is an outer peripheral surface bus of the conical portion 5t. Formed in the direction. Accordingly, the flow toward the slit portion 2g is squeezed and compressed so as to overcome the bulge along the generatrix of the cone-shaped portion 5t. At this time, since the flow allowance of the compressed liquid is given in the longitudinal direction of the slit portion 2g, the flow velocity is hardly lowered, and the cavitation (decompression) effect is further enhanced. Further, since the cavitation generation region is formed linearly along the slit portion 2g, the region where bubbles are deposited under reduced pressure is greatly expanded, and a large amount of fine bubbles can be deposited.
  • the center gap 2k is formed so as to include the center of the cross section, and the center flow having the maximum flow velocity can pass through the center gap 2k without being influenced by detours.
  • the center flow is further narrowed by the passage of the center gap 2k to increase the speed, but since the flow detour to the segment region 2e side is permitted, an increase in fluid resistance is effectively suppressed. Thereby, the cavitation (decompression) effect in the center of the cross section is further enhanced, and a larger amount of fine bubbles can be deposited.
  • Each flow distributed to the segment region 2e generates an eddy current or turbulent flow downstream of each collision part 3, and it can be expected that the generated bubbles are entrained in the eddy current or turbulent flow and refined.
  • the high-speed flow near the center of the cross section is effectively restricted by the four conical portions 5t arranged so as to surround the center of the cross section, and flows into the center gap 2k while being increased.
  • four slit portions 2g around the center gap 2k communicate with each other, and the flow compressed and compressed in the center gap 2k bypasses the slit portion 2g, so that the fluid resistance is extremely increased. Effectively suppressed.
  • the flow detouring to the slit portion 2g itself also has a degree of freedom in the slit longitudinal direction, a decrease in the flow velocity can be suppressed low.
  • the cavitation (decompression) effect is very active even in the center gap 2k and the slit portion 2g, and nanobubble-level fine bubbles can be generated at a high concentration.
  • the tip of the collision part 3 (conical part 5t) facing the center gap 2k is sharply formed, and the flow passing through the vicinity thereof can be made particularly fast, so that the bubble miniaturization becomes more remarkable.
  • a plurality of circumferentially drawn diaphragm ribs 5 r are formed on the outer peripheral surface of the collision part 3 along the protruding direction of the collision part 3.
  • the gas-dissolved liquid that flows in the tangential direction of the outer peripheral surface of the collision portion 3 is further increased in speed by being squeezed in the groove portion (or valley-like portion) 21 between the squeezing ribs 5r, and the pressure reduction effect is enhanced.
  • the flow on the valley opening side is relatively slow, and in particular, the pressure is higher than the high-speed flow on the valley bottom side.
  • a low-speed high-pressure area HPA is formed on the valley opening side
  • a high-speed low-pressure area LPA is formed on the valley low side, so that the gas saturation dissolution amount of the liquid on the valley opening side increases and the saturation dissolution amount on the valley bottom side decreases.
  • the dissolved air (dissolved liquid) SGF in the water flow is changed from the low-speed flow region LF (high pressure region HPA: FIG. 4) on the valley opening side to the high-speed flow region FF (low pressure region LPA: 5), the bubbles MB are deposited very actively.
  • the collision portion 3 is formed by a screw member 5, and a plurality of winding ribs 5r are integrally formed in a spiral shape.
  • the flow component crossing the ridge portion of the throttle rib 5r increases, and the effect of generating turbulent flow accompanying flow separation becomes significant. Therefore, there is an advantage that the bubbles can be further miniaturized.
  • the shower head 100 by incorporating the bubble generation engine 1, it is possible to easily form a shower water flow containing a larger amount of bubbles even if the water flow has the same dissolved air concentration. Also, since dissolved air is bubbled by precipitation under reduced pressure, the dissolved oxygen concentration of bulk water (or dissolved chlorine concentration in the case of tap water, etc.) is reduced, and oxygen (or chlorine) for the skin and hair in contact with the shower water flow Can be effectively reduced. In particular, as shown in FIG.
  • the above-mentioned throttle ribs 5r are continuously formed on the outer peripheral surface of all the collision parts 3, so that the collision part 3 material contacting both sides of each segment region 2e A large number of cavitation points for bubble deposition are formed by 5r and the valley-like portion, and bubble deposition becomes extremely active, and the bubble concentration in the water stream can be significantly increased.
  • the shower head 100 it is possible to produce a visually impactful effect such that a large amount of bubbles can be introduced to the extent that the water flow can be clouded only by the precipitation effect by cavitation without taking in outside air.
  • FIG. 8 shows an example in which a part of the plurality of collision portions 3 is configured with a diaphragm rib 5r and the rest is configured without a diaphragm rib 5r.
  • the ones with the diaphragm ribs 5r and the ones without the diaphragm ribs 5r are alternately arranged in the circumferential direction, and the diaphragm ribs are formed on one side of the collision portion 3 in contact with each segment region 2e. The cavitation effect by 5r is sure to occur.
  • the narrowed rib 5r in the remaining region without forming the narrowed rib 5r at the tip of the collision portion 3 located at the center of the cross section of the high flow velocity that greatly contributes to the generation of the fine bubble. This is effective in preventing the loss due to bubble coalescence.
  • the diaphragm rib 5r was not formed on the outer peripheral surface of the conical portion 5t that forms the tip of the collision portion 3, but when the bubble generation is excessive, as shown in FIG. A configuration in which the formation of the diaphragm rib 5r is omitted in the tip side region of the cylindrical peripheral side surface portion following the conical portion 5t is also possible.
  • the configuration consists of ultrafine bubbles (especially nanobubbles of 10 nm to 800 nm or less) due to the high-speed flow gaps 2g and 2k in the central region of the cross section and fine bubbles (1 ⁇ m or more and 100 ⁇ m or less of microbubbles) due to the squeezing rib 5r in the peripheral region. It can be said that it is effective in generating the above in a balanced manner.
  • FIG. 10 shows an example in which the diaphragm rib 5r is intermittently formed in the axial direction on the cylindrical peripheral side surface portion. If it is desired to give priority to the generation of nanobubbles, it is possible to adopt a configuration in which no diaphragm rib is formed on the outer peripheral surface of the collision portion as shown in FIG.
  • independent diaphragm ribs 5s in close contact with each other in the axial direction so as to be closed in the circumferential direction around the axis of the collision portion 3 as shown in FIG.
  • independent individual restricting ribs 5 s are formed in a direction orthogonal to the axis of the collision portion 3, but it is also possible to form them by inclining with respect to a plane orthogonal to the axis. In this manner, as in FIG. 3, the squeezing rib is inclined, so that the effect of generating turbulent flow accompanying flow separation becomes significant, and the bubbles can be further miniaturized.
  • the tip angle of the cone-shaped portion 5t that forms the tip of the collision portion 3 is 90 ° (that is, the entire circumferential angle is 360 °) expressed by a cross section cut by a plane including the axis of the collision portion 3. (Value divided by the number (4) of the collision parts 3). Therefore, as shown in FIG. 12, if each collision part 3 is positioned so that the side surfaces of the adjacent cone-shaped parts 5t are in close contact with each other so that the tip of the collision part 3 is aligned with the center of the cross section of the throttle part 2c, It is also possible to have no flow gap.
  • the flow of the liquid is distributed to each segment region 2e, and bubbles can be generated by the cavitation effect mainly composed of the throttle rib 5r.
  • the tip of the cone-shaped part 5t is brought into contact with the pair of collision parts 3 and 3 opposed in the inner diameter direction, and the remaining pair of collision parts 3 and 3 are retracted in the axial direction. By doing so, the slit portion 2g can be formed.
  • the tip of the collision part 3 can be formed flat.
  • the flat tip surface 5u is formed by cutting out the tip portion of the conical portion 5t similar to FIG.
  • the center gap 2k can be expanded and the flow can be made uniform, which contributes to an improvement in the concentration of fine bubbles as a whole.
  • the side surfaces of the adjacent conical portions 5t are brought into close contact with each other, but the center gap 2k is formed in a closed shape by forming a flat front end surface 5u.
  • FIG. 15 shows an example in which the slit portion 2g is formed between the side surfaces of the adjacent conical portions 5t.
  • the main collision portion 130 is disposed so as to cross the cross section of the throttle portion 2c along the inner diameter, and further, the cross section center of the throttle portion 2c is sandwiched between the main collision portion 130 and the main collision portion 130.
  • This is an example in which a pair of opposed collision portions 30 opposed in the inner diameter direction are provided.
  • An outer peripheral gap 2j constituting a high-speed flow gap is formed between each front end surface of the opposing collision unit 30 and the outer peripheral surface of the main collision unit 130.
  • the tip of the opposing collision part 30 is formed flat, and the outer peripheral gap 2j is formed in a slit shape. Since the cavitation region can be expanded in the slit longitudinal direction, fine bubbles can be generated at a higher concentration.
  • the main collision part 130 is an integral member in the inner diameter direction in which both end parts are embedded in the member main body 6, and a throttle rib 5 r is formed on the entire outer peripheral surface of the part exposed in the throttle part 2 c.
  • the outer peripheral surface of the main collision portion 130 facing the tip surface of the opposing collision portion 30 is uneven by the restriction rib 5r, and the gap interval is narrowed at the position of the restriction rib 5r (mountain) so that the high-speed flow region In the valley portion 21, the gap interval is increased and a low flow velocity region is generated.
  • a dissolved gas flow is generated from the low flow velocity region to the high flow velocity region in accordance with the pressure difference between the two adjacent regions, and further, the dissolved gas is generated in the valley portion 21 shown in FIGS.
  • the outer peripheral surface of the main collision part 130 is reduced in distance from the liquid inflow side to the position facing the front end surface of the opposing collision part 30, and the increase in flow velocity due to the throttling effect also enhances the bubble generation effect. This is advantageous. Note that, as indicated by broken lines in FIG. 16, the space of the valley-shaped portion 21 forms the outer peripheral gap 2j even if the front end surface of the opposing collision portion 30 is brought into contact with the diaphragm rib 5 on the outer peripheral surface of the main collision portion 130. It becomes a shape and active bubble deposition can be expected.
  • FIG. 17 shows an example in which the front ends of the opposed collision portions 3 and 3 are sharply formed.
  • the squeezing effect in the vicinity of the tip of the opposing collision portion 3 is enhanced, and the bubbles can be miniaturized by increasing the flow velocity.
  • Each of the main collision parts has a flat front end surface 5u and a pair of collision parts 30 and 30 each having a chamfered portion 3t formed along the outer periphery of the front end surface 5u are in contact with each other at the front end surfaces 5u and 5u. In this manner, it is arranged so as to face the inner diameter direction of the throttle portion 2c.
  • the front ends of the opposing collision portions 3 and 3 form an outer peripheral gap 2j so as to face a groove portion having a V-shaped cross section formed by the chamfered portion 3t of the two collision portions 30 and 30 forming the main collision portion.
  • tip is further heightened.
  • the main collision portion is indicated by a pair of collision portions 30 ′, 30 ′ (hereinafter referred to as main collision portions 30 ′, 30 ′) each having flat tip surfaces 5u, 5u. It is also possible to form a central gap 2k that includes the center of the cross section of the throttle portion 2c between the tip surfaces 5u and 5u, and to be disposed opposite to the inner diameter direction of the throttle portion 2c. .
  • FIG. 18 shows a configuration in which the distal end surfaces of the opposing collision portions 30 and 30 are brought into contact with the outer peripheral surfaces of the leading end portions of the main collision portions 30 ′ and 30 ′ (as a result, the diaphragm rib 5 r).
  • FIG. 19 shows a slit-like outer peripheral gap 2j in which the front end surfaces 5u and 5u of the opposing collision portions 30 and 30 are separated from the outer peripheral surface of the front end portion of the main collision portions 30 ′ and 30 ′ (and consequently the diaphragm rib 5r). An example in which is further formed will be shown.
  • the flow that is squeezed and compressed in the center gap 2k is diverted to the slit-shaped outer peripheral gap 2j, so that an increase in fluid resistance is extremely effectively suppressed. Further, since the outer peripheral gap 2j is also narrowed in a slit shape, a decrease in flow velocity at the detour destination can be suppressed to a low level. As a result, the cavitation (decompression) effect is very active even in the center gap 2k and the slit portion 2g, and nanobubble-level fine bubbles can be generated at a high concentration.
  • all four segment areas are formed.
  • the number of segment areas is not limited to four.
  • the number of segment regions formed can be made 5 or more by reducing the outer diameter of the collision part.
  • FIG. 21 is a schematic diagram of a circulation type bubble generation mechanism 200 using the bubble generation engine 1.
  • the bubble generating engine 1 is incorporated in a wall portion of the water tank 54 to be a water flow outlet for the water tank 54, while a water flow inlet 53 is formed at another position of the wall portion, and the water tank is formed by a pump 51 through pipes 50 and 52. Inside water W bubble generation engine 1 It is designed to circulate through. When the water flow pumped by the pump 51 passes through the bubble generation engine 1, the bubbles MB are deposited and discharged into the water tank 54 as a bubble-containing liquid.
  • a known ejector nozzle is mounted on the pipe 50 or the pipe 52, and the sucked gas is further finely pulverized into the water tank 54 while passing through the bubble generating engine 1 while sucking and taking in outside air through the ejector nozzle. It can also be configured to release.
  • Inner diameter 16 mm
  • flow path length L2 8 mm
  • Collision part 3 Screw outer diameter: M2, tip part has a tip angle of 90 ° in the cross section including the axis, and the size of the center gap 2k (length between the tip of the opposing collision part 3): 0 mm, 0. 3 conditions of 18mm and 0.36mm
  • a hose was connected to the bubble generation engine 2, 10 ° C. water was supplied to the inlet 2 n at a supply pressure of 0.12 MPa, and the injected water was discharged into a water tank having a volume of about 90 liters. At this time, the injection flow rate from the outlet 2x was about 10 liters / minute.
  • the laser diffraction particle size distribution measuring device makes the laser light beam incident on the measurement cell at a certain angle, and uses the fact that the scattering angle varies depending on the particle size of the particle to be measured (here, bubble).
  • the scattered light intensity is detected by an individual photodetector, and information related to the particle size distribution is obtained from the detected intensity of each sensor.
  • the detection intensity of scattered light at the corresponding detector tends to increase as the volume of the bubble increases, so that multiple light detections with different particle size intervals are handled.
  • What is directly calculated using the output intensity ratio of the vessel is distribution information using the relative total volume (hereinafter also referred to as volume relative frequency) for each particle size interval as an index.
  • volume relative frequency the relative total volume
  • the recognition of the average diameter is high is the number average diameter obtained by dividing the total value of the particle diameter by the number of particles, but in the case of a laser diffraction particle size distribution measuring device, on the measurement principle, Only the volume average diameter weighted by the particle volume can be calculated directly. Therefore, the bubble diameter distribution was calculated by converting the volume relative frequency into the number relative frequency on the assumption that the bubble was spherical by using software installed as standard in the apparatus.
  • FIG. 22 shows a measurement result while water is flowing when the center gap 2k is 0 mm at a supply pressure of 0.12 MPa, that is, when the slit portion 2g is not formed.
  • the upper row shows the bubble diameter distribution by the number relative frequency
  • the lower row shows the scattered light intensity at each detector (that is, the scattering angle position) at that time.
  • the measurement result of the number average diameter at this time is 27.244 ⁇ m.
  • the water flow was stopped, and after leaving for about 1 minute until the coarse bubbles in the water tank rose on the water surface, the same measurement was performed.
  • the results are shown in FIG. Although the average diameter was 0.128 ⁇ m, it was found that very fine bubbles existed, but the absorbance of water (indicating the degree of laser light loss due to scattering) was greatly reduced, and the concentration of fine bubbles Is considered low.
  • FIG. 24 shows the measurement results when the supply pressure was lowered to 0.09 MPa, and after standing for about one minute after the water flow was stopped, the measurement was performed in exactly the same manner. Very fine bubbles having an average diameter of 0.113 ⁇ m are confirmed, the absorbance is as high as 0.012, and it can be seen that the fine bubbles are formed at a relatively high concentration. It can be seen that fine bubbles can be formed at a high concentration even in an engine without a central gap by setting the supply pressure somewhat low and moderately suppressing the coalescence of bubbles.
  • FIG. 25 shows the measurement results during water flow when the center gap 2k is 0.18 mm at a supply pressure of 0.12 MPa.
  • the inside of the water tank was cloudy, but the rising speed of the bubbles was clearly slower than that in the case where the center gap 2k was not formed, and the average diameter of the bubbles was reduced to 18.539 ⁇ m.
  • the measurement result after one minute progress after a water flow stop is FIG. It can be seen that the average diameter decreases to 2.63 ⁇ m while maintaining a relatively high absorbance (0.025).
  • FIG. 27 shows the result of measurement performed in the same manner by dropping the supply pressure to 0.09 MPa and stopping the water flow for about 1 minute. It can be seen that extremely fine bubbles having an average diameter of 0.024 ⁇ m are formed at a high concentration while maintaining the absorbance as high as 0.020.
  • FIG. 28 shows the measurement results during water flow when the center gap 2k is 0.36 mm at a supply pressure of 0.12 MPa. Compared to the case where the central gap 2k is not formed, the average bubble diameter is as small as 18.477 ⁇ m.
  • FIG. 29 shows the measurement result after one minute has elapsed after stopping the water flow, and the average diameter is reduced to 0.153 ⁇ m while maintaining a relatively high absorbance (0.017). It can be seen that even if the supply pressure is slightly high, fine bubbles in the nanometer range are formed at a high concentration.
  • FIG. 30 shows the measurement results obtained by reducing the supply pressure to 0.09 MPa and leaving it for about 1 minute after stopping water flow. It can be seen that extremely fine bubbles having an average diameter of 0.071 ⁇ m are formed at a high concentration while maintaining the absorbance as high as 0.015.
  • Bubble generation engine (bubble generation mechanism) 2 channel 2a inflow side taper part 2b outflow side taper part 2c throttle part 2e segment area 2n inflow port 2x outflow port 2g slit part (high-speed flow gap) 2k Center gap (High-speed flow gap) 3, 30, 30 ', 130 Colliding part 5t Conical part 5r Drawing rib 6 Member main body 100 shower device

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Nanotechnology (AREA)
  • Bathtubs, Showers, And Their Attachments (AREA)
  • Nozzles (AREA)
PCT/JP2012/068480 2011-07-21 2012-07-20 気泡発生機構及び気泡発生機構付シャワーヘッド Ceased WO2013012069A1 (ja)

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JP2013524754A JP5712292B2 (ja) 2011-07-21 2012-07-20 気泡発生機構及び気泡発生機構付シャワーヘッド
KR1020147001715A KR20140048940A (ko) 2011-07-21 2012-07-20 기포발생기구 및 기포발생기구 부착 샤워헤드
EP12814186.8A EP2735363A4 (en) 2011-07-21 2012-07-20 BUBBLE GENERATION MECHANISM AND SHOWERHEAD HAVING A BUBBLE GENERATION MECHANISM
CN201280036169.1A CN103747858B (zh) 2011-07-21 2012-07-20 气泡发生机构以及带气泡发生机构的喷头
US14/234,032 US9370784B2 (en) 2011-07-21 2012-07-20 Bubble generating mechanism and showerhead with bubble generating mechanism

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EP2735363A4 (en) 2015-08-05
EP2735363A1 (en) 2014-05-28
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