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JP7329397B2 - Fine bubble generating nozzle body - Google Patents
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JP7329397B2 - Fine bubble generating nozzle body - Google Patents

Fine bubble generating nozzle body Download PDF

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JP7329397B2
JP7329397B2 JP2019166602A JP2019166602A JP7329397B2 JP 7329397 B2 JP7329397 B2 JP 7329397B2 JP 2019166602 A JP2019166602 A JP 2019166602A JP 2019166602 A JP2019166602 A JP 2019166602A JP 7329397 B2 JP7329397 B2 JP 7329397B2
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pressurized water
side opening
dissolved pressurized
inlet
air
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JP2021041361A (en
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拓也 岩▲崎▼
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Rinnai Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

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Description

本明細書で開示する技術は、微細気泡発生ノズル本体に関する。 The technology disclosed in this specification relates to a fine bubble generating nozzle body.

特許文献1には、微細気泡発生ノズルが開示されている。この微細気泡発生ノズルは、微細な噴出孔を有する筒状部材であるノズル本体と、ノズル本体の先端に取り付けられるノズルカバーとを備える。ノズルカバーは、噴出孔に対向する壁と、噴出孔よりも微細な流出孔とを有する。 Patent Literature 1 discloses a microbubble generating nozzle. This fine bubble generating nozzle includes a nozzle body, which is a cylindrical member having fine ejection holes, and a nozzle cover attached to the tip of the nozzle body. The nozzle cover has a wall facing the ejection hole and an outflow hole that is finer than the ejection hole.

特許文献1の微細気泡発生ノズルでは、気体(例えば空気、炭酸ガス、水素等)が水に溶解している気体溶解加圧水がノズル本体に供給されると、気体溶解加圧水は、ノズル本体を通って噴出孔から壁に向けて噴出される。噴出孔から噴出された気体溶解加圧水は、壁に衝突してノズルカバー内で迂回した後、流出孔から流出箇所(具体的には浴槽)に流出される。気体溶解加圧水は、微細な噴出孔、及び、さらに微細な流出孔を通過することにより、大気圧まで徐々に減圧される。気体溶解加圧水が減圧される過程において、気体溶解加圧水に溶解されていた気体が析出し、微細気泡が発生する。即ち、特許文献1の微細気泡発生ノズルでは、気体溶解加圧水の流通過程で気体溶解加圧水を減圧することにより、流出箇所(具体的には浴槽)に流出される気体溶解加圧水に微細気泡を含ませることができる。 In the fine bubble generating nozzle of Patent Document 1, when gas-dissolved pressurized water in which gas (for example, air, carbon dioxide, hydrogen, etc.) is dissolved in water is supplied to the nozzle body, the gas-dissolved pressurized water passes through the nozzle body. It is ejected from the ejection port toward the wall. The gas-dissolved pressurized water ejected from the ejection hole collides with the wall, detours within the nozzle cover, and then flows out from the outflow hole to an outflow location (specifically, a bathtub). The gas-dissolved pressurized water is gradually decompressed to atmospheric pressure by passing through fine jet holes and finer outflow holes. In the process of depressurizing the gas-dissolved pressurized water, the gas dissolved in the gas-dissolved pressurized water is precipitated to generate fine bubbles. That is, in the microbubble generating nozzle of Patent Document 1, the pressure of the gas-dissolved pressurized water is reduced in the flow process of the gas-dissolved pressurized water, so that the gas-dissolved pressurized water flowing out to the outflow location (specifically, the bathtub) contains microbubbles. be able to.

特開2007-167557号公報JP 2007-167557 A

しかしながら、特許文献1の微細気泡発生ノズルでは、流出箇所に流出される気体溶解加圧水に含まれる微細気泡の量が不十分であるという状況が発生する。 However, in the microbubble generating nozzle of Patent Document 1, a situation occurs in which the amount of microbubbles contained in the gas-dissolved pressurized water flowing out to the outflow location is insufficient.

本明細書では、流出箇所に流出される気体溶解加圧水に微細気泡を大量に含ませることができる技術を提供する。 The present specification provides a technique that allows a large amount of microbubbles to be included in the gas-dissolved pressurized water that flows out to the outflow location.

本明細書によって開示される微細気泡発生ノズル本体は、上流側端部から下流側端部に向けて、気体が水に溶解している気体溶解加圧水を通過させる減圧管と、前記上流側端部に開口され、前記気体溶解加圧水を供給するための給水手段から前記減圧管内に前記気体溶解加圧水を導入する導入口と、前記減圧管のうち前記導入口よりも下流側に設けられ、前記減圧管内に導入された前記気体溶解加圧水を通過させる入口側開口部と、前記入口側開口部よりも下流側である前記下流側端部に開口された出口側開口部と、を備えている。前記入口側開口部の開口面積は前記導入口の開口面積よりも小さく、前記出口側開口部の開口面積は前記入口側開口部の開口面積よりも大きく、前記減圧管のうち、前記入口側開口部よりも下流側であって前記入口側開口部近傍の特定部分に、前記減圧管の外周壁と内周壁とを連通する少なくとも1個の連通孔が開口されている。前記導入口および前記少なくとも1個の連通孔が、前記給水手段から前記気体溶解加圧水が供給される給水空間内に配置されている。 The fine bubble generating nozzle body disclosed by the present specification includes a decompression pipe for passing gas-dissolved pressurized water in which gas is dissolved in water from an upstream end to a downstream end, and the upstream end an inlet for introducing the gas-dissolved pressurized water into the decompression pipe from a water supply means for supplying the gas-dissolved pressurized water; an inlet-side opening through which the gas-dissolved pressurized water introduced into the inlet-side opening passes; and an outlet-side opening opened at the downstream end located downstream of the inlet-side opening. The opening area of the inlet-side opening is smaller than the opening area of the inlet, the opening area of the outlet-side opening is larger than the opening area of the inlet-side opening, and the inlet-side opening of the decompression tube is At least one communication hole communicating between the outer peripheral wall and the inner peripheral wall of the decompression tube is opened in a specific portion in the vicinity of the inlet side opening on the downstream side of the pressure reducing tube. The introduction port and the at least one communication hole are arranged in a water supply space into which the gas-dissolved pressurized water is supplied from the water supply means.

上記の構成によると、気体溶解加圧水は、外部から減圧管内に導入される際に入口側開口部を通過することによって流速が上昇し、その結果減圧される(ベンチュリー効果)。気体溶解加圧水が減圧されることにより、気体溶解加圧水に溶解していた気体が析出し、微細気泡の元になる気泡(気泡核とも言う)が発生する。その後、減圧管の出口側開口部から排出された気体溶解加圧水は、流出箇所に流出されるまでの間、所定の流通経路を流通されながら増圧される。減圧によって気泡が析出させられた後の気体溶解加圧水が増圧されると、気体溶解加圧水に含まれる気泡が分裂して微細気泡になる。 According to the above configuration, when the gas-dissolved pressurized water is introduced into the decompression tube from the outside, the flow rate increases by passing through the inlet side opening, resulting in decompression (Venturi effect). When the pressure of the gas-dissolved pressurized water is reduced, the gas dissolved in the gas-dissolved pressurized water is precipitated, and bubbles (also called bubble nuclei) that form fine bubbles are generated. After that, the gas-dissolved pressurized water discharged from the outlet side opening of the decompression pipe is increased in pressure while being circulated through a predetermined flow path until it flows out to the outflow point. When the pressure of the gas-dissolved pressurized water after bubbles are precipitated by depressurization is increased, the bubbles contained in the gas-dissolved pressurized water are split and become fine bubbles.

そして、上記の構成によると、減圧管の特定部分に少なくとも1個の連通孔が開口されているため、気体溶解加圧水が入口側開口部を通過することに伴うベンチュリー効果によって減圧管内に負圧が生じる場合に、その負圧によって、外部から連通孔を通って気体溶解加圧水が減圧管内に引き込まれる。連通孔から減圧管内に引き込まれた気体溶解加圧水は、減圧管内を入口側開口部から出口側開口部に向けて流れる気体溶解加圧水のうちの減圧管内周壁付近の気体溶解加圧水の流れと衝突する。その結果、内周壁付近の流速が径方向中心付近の流速よりも遅くなる。内周壁付近と中心付近の流速差が大きくなることで、より多くの気泡核が生じる。その結果、上記の微細気泡発生ノズル本体を用いることで、気泡核を元にする微細気泡を大量に発生させることができる。 According to the above configuration, since at least one communication hole is opened in a specific portion of the decompression tube, a negative pressure is generated in the decompression tube by the Venturi effect associated with the gas-dissolved pressurized water passing through the inlet side opening. When this occurs, the negative pressure draws gas-dissolved pressurized water into the decompression tube from the outside through the communication hole. The gas-dissolved pressurized water drawn into the decompression tube through the communication hole collides with the flow of the gas-dissolved pressurized water near the inner peripheral wall of the decompression tube among the gas-dissolved pressurized water flowing in the decompression tube from the inlet side opening toward the outlet side opening. As a result, the flow velocity near the inner peripheral wall becomes slower than the flow velocity near the radial center. As the flow velocity difference between the vicinity of the inner peripheral wall and the vicinity of the center increases, more bubble nuclei are generated. As a result, it is possible to generate a large amount of microbubbles based on the bubble nuclei by using the fine bubble generating nozzle main body.

ここで言う「気体」は、空気、炭酸ガス、水素等、水に溶解可能な任意の気体を含む。 The term "gas" as used herein includes any gas that can be dissolved in water, such as air, carbon dioxide, and hydrogen.

前記少なくとも1個の連通孔の合計開口面積は、前記入口側開口部の開口面積よりも小さくてもよい。 A total opening area of the at least one communication hole may be smaller than an opening area of the inlet side opening.

この構成によると、少なくとも1個の連通孔の合計開口面積が、入口側開口部の開口面積以上である構成を採用する場合に比べて、減圧管内で発生する負圧によって外部から連通孔を通って減圧管内に気体溶解加圧水が引き込まれ易くなる。即ち、減圧管内で発生する負圧を有効に働かせることができる。 According to this configuration, compared to the case where the total opening area of at least one communicating hole is equal to or larger than the opening area of the inlet side opening, the negative pressure generated in the pressure reducing tube causes the outside to pass through the communicating hole. As a result, gas-dissolved pressurized water is easily drawn into the decompression tube. That is, the negative pressure generated in the decompression tube can be effectively used.

前記特定部分における前記減圧管の開口面積は、前記入口側開口部の開口面積以上であって110%以内であってもよい。 The opening area of the decompression tube at the specific portion may be equal to or greater than the opening area of the inlet-side opening and within 110%.

この構成によると、減圧管のうち、少なくとも1個の連通孔が形成されている特定部分における開口面積は、入口側開口部の開口面積の110%以内である。即ち、減圧管のうち、入口側開口部から見た開口面積の増分が10%以内である範囲内に連通孔が形成される。この範囲は、主に入口側開口部の通過直後の範囲であるため、この範囲を通過する気体溶解加圧水には比較的大きい負圧が生じる。そのため、上記の構成によると、連通孔を通って外部から減圧管内に気体溶解加圧水が引き込まれ易くなる。即ち、減圧管内で発生する負圧をより有効に働かせることができる。 According to this configuration, the opening area of the specific portion of the decompression tube where at least one communication hole is formed is within 110% of the opening area of the inlet side opening. That is, the communication hole is formed within a range in which the increase in the opening area of the decompression tube as viewed from the inlet side opening is within 10%. Since this range is mainly the range immediately after passing through the inlet side opening, a relatively large negative pressure is generated in the gas-dissolved pressurized water passing through this range. Therefore, according to the above configuration, the gas-dissolved pressurized water is easily drawn into the decompression tube from the outside through the communication hole. In other words, the negative pressure generated inside the pressure reducing tube can be made to work more effectively.

微細気泡発生ノズル10の斜視図。FIG. 2 is a perspective view of the microbubble generating nozzle 10. FIG. 図1のII-II線に沿った微細気泡発生ノズル10の断面図。FIG. 2 is a cross-sectional view of the microbubble generating nozzle 10 taken along line II-II in FIG. 1; ノズル本体20の斜視図。3 is a perspective view of the nozzle body 20; FIG. ノズル本体20の入口側開口部24近傍の拡大断面図。4 is an enlarged cross-sectional view of the vicinity of the inlet-side opening 24 of the nozzle body 20. FIG. ホルダ部40の斜視図。4 is a perspective view of the holder part 40. FIG.

(実施例)
(微細気泡発生ノズル10の構成)
図1~図5を参照して、第1実施例の微細気泡発生ノズル10について説明する。微細気泡発生ノズル10は、浴槽(図示省略)等の流出箇所に微細気泡を含む水を供給するためのノズルである。図1に示すように、微細気泡発生ノズル10は、ノズル本体20と、ホルダ部40と、を備える。図1、図2において、ノズル本体20は、ホルダ部40に支持されている。
(Example)
(Structure of fine bubble generating nozzle 10)
A microbubble generating nozzle 10 of a first embodiment will be described with reference to FIGS. 1 to 5. FIG. The microbubble generating nozzle 10 is a nozzle for supplying water containing microbubbles to an outflow location such as a bathtub (not shown). As shown in FIG. 1 , the microbubble generating nozzle 10 includes a nozzle body 20 and a holder portion 40 . 1 and 2, the nozzle body 20 is supported by the holder portion 40. As shown in FIG.

(ノズル本体20の構成)
図1~図4を参照して、ノズル本体20の構成について説明する。なお、以下の説明では、図2中のX軸方向を左右方向、Y軸方向を上下方向、Z軸方向を前後方向と呼ぶ場合がある。図3に示すように、ノズル本体20は、減圧管22と鍔部28とを備える。
(Structure of Nozzle Body 20)
The configuration of the nozzle body 20 will be described with reference to FIGS. 1 to 4. FIG. In the following description, the X-axis direction in FIG. 2 may be referred to as the left-right direction, the Y-axis direction as the up-down direction, and the Z-axis direction as the front-rear direction. As shown in FIG. 3 , the nozzle body 20 includes a decompression tube 22 and a collar portion 28 .

図1~図4に示すように、減圧管22は、空気が水に溶解している空気溶解加圧水の圧力を減圧することができる管状部材である。図2に示すように、減圧管22の内部には、減圧管22内を2本の管部に区画する区画壁25が設けられている。減圧管22の後方側の上流側端部22a(図中Z軸の負方向側の端部)には、2個の導入口23が開口されている。導入口23には、空気が水に溶解している空気溶解加圧水を供給するための給水手段(図示しない)から、空気溶解加圧水が供給される。本実施例では、導入口23及び連通孔30(後述)を含む減圧管22の後方側の部分(即ち、鍔部28より後方側の部分)が、上記給水手段から水が供給される給水空間(図示しない)内に配置される。ここで、空気溶解加圧水は、流出箇所に供給される微細気泡を含む水の原料となる液体である。 As shown in FIGS. 1 to 4, the decompression pipe 22 is a tubular member capable of decompressing the air-dissolved pressurized water in which air is dissolved in water. As shown in FIG. 2, inside the decompression tube 22, a partition wall 25 is provided to partition the interior of the decompression tube 22 into two tube portions. Two introduction ports 23 are opened at the upstream end portion 22a on the rear side of the decompression tube 22 (the end portion on the negative direction side of the Z axis in the drawing). Air-dissolved pressurized water is supplied to the inlet 23 from a water supply means (not shown) for supplying air-dissolved pressurized water in which air is dissolved in water. In this embodiment, the rear side portion of the decompression tube 22 (that is, the rear side portion of the collar portion 28) including the introduction port 23 and the communication hole 30 (described later) is a water supply space to which water is supplied from the water supply means. (not shown). Here, the air-dissolved pressurized water is a liquid that serves as a raw material for water containing microbubbles that is supplied to the outflow location.

減圧管22のうち、上流側端部22aの近傍であって、2個の導入口23よりもやや前方寄り(即ち、下流側寄り。Z軸の正方向寄りとも言う)の位置には、2個の入口側開口部24が開口されている。入口側開口部24の開口面積は、導入口23の開口面積よりも小さい。言い換えると、減圧管22は、入口側開口部24において縮径されている。区画壁25は、減圧管22の後方側の上流側端部22a(図中Z軸の負方向側の端部)から、減圧管22の途中までの区間を2本の管部に区画している。そのため、減圧管22の前方側の下流側端部22b(図中Z軸の正方向側の端部)は、区画壁25によって2本の管部に区画されていない。下流側端部22bには、1個の出口側開口部26のみが開口されている。本実施例では、出口側開口部26の開口面積(即ちXY平面上の面積)は、2個の入口側開口部24の開口面積(即ちXY平面上の面積)の合計面積よりも大きい。言い換えると、減圧管22は、入口側開口部24から出口側開口部26に向かって拡径されている。 In the vicinity of the upstream end 22a of the decompression tube 22 and slightly forward (that is, downstream, also referred to as the positive direction of the Z axis) of the two introduction ports 23, two A single inlet side opening 24 is opened. The opening area of the inlet side opening 24 is smaller than the opening area of the introduction port 23 . In other words, the decompression tube 22 has a reduced diameter at the inlet-side opening 24 . The partition wall 25 divides the section from the rear upstream end 22a of the decompression tube 22 (the end on the negative direction side of the Z-axis in the drawing) to the middle of the decompression tube 22 into two pipe sections. there is Therefore, the front downstream end portion 22b of the decompression tube 22 (the end portion on the positive side of the Z axis in the drawing) is not divided into two pipe portions by the dividing wall 25 . Only one outlet side opening 26 is opened in the downstream end 22b. In this embodiment, the opening area of the outlet side opening 26 (that is, the area on the XY plane) is larger than the total area of the opening areas of the two inlet side openings 24 (that is, the area on the XY plane). In other words, the decompression tube 22 expands in diameter from the inlet side opening 24 toward the outlet side opening 26 .

とくに図2、図4に示すように、減圧管22のうち、各入口側開口部24よりも下流側であって、各入口側開口部24の通過直後の部分(即ち入口側開口部24の近傍の部分。以下では「特定部分」と呼ぶ場合がある)に、減圧管22の外周壁と内周壁とを連通する連通孔30が1個ずつ開口されている。各連通孔30の開口面積は、各入口側開口部24の開口面積よりも小さい。また、本実施例では、連通孔30が形成されている部分(即ち特定部分)における減圧管22の開口面積は、入口側開口部24の開口面積とほぼ等しい。即ち、本実施例では、入口側開口部24から見た開口面積の増分がほぼない範囲内に連通孔30が形成される。 In particular, as shown in FIGS. 2 and 4, the portion of the decompression tube 22 that is downstream of each inlet-side opening 24 and immediately after passing through each inlet-side opening 24 (that is, the inlet-side opening 24). Communicating holes 30 for communicating between the outer peripheral wall and the inner peripheral wall of the decompression tube 22 are opened one by one in a nearby portion (hereinafter sometimes referred to as a “specific portion”). The opening area of each communication hole 30 is smaller than the opening area of each inlet-side opening 24 . Further, in this embodiment, the opening area of the decompression tube 22 at the portion where the communication hole 30 is formed (that is, the specific portion) is substantially equal to the opening area of the inlet side opening 24 . That is, in this embodiment, the communication hole 30 is formed within a range where there is almost no increase in opening area when viewed from the inlet side opening 24 .

図2、図3に示すように、鍔部28は、減圧管22の前後方向中間部付近の外面に設けられている円板状部材である。図2に示すように、鍔部28の外径は、減圧管22の外径よりも大きい。 As shown in FIGS. 2 and 3, the collar portion 28 is a disk-shaped member provided on the outer surface of the decompression tube 22 near the middle portion in the front-rear direction. As shown in FIG. 2 , the outer diameter of the collar portion 28 is larger than the outer diameter of the pressure reducing tube 22 .

(ホルダ部40の構成)
続いて、図1、図2、図5を参照して、ホルダ部40の構成について説明する。図5に顕著に示されるように、ホルダ部40は、外側円筒部42と、内側円筒部44と、2個の連結部52と、を備える。外側円筒部42と2個の連結部52とは連続して一体に成形されている。内側円筒部44は、外側円筒部42の内側に収容されて形成されている。
(Configuration of holder portion 40)
Next, the configuration of the holder portion 40 will be described with reference to FIGS. 1, 2, and 5. FIG. As clearly shown in FIG. 5 , the holder portion 40 includes an outer cylindrical portion 42 , an inner cylindrical portion 44 and two connecting portions 52 . The outer cylindrical portion 42 and the two connecting portions 52 are continuously and integrally formed. The inner cylindrical portion 44 is formed inside the outer cylindrical portion 42 .

外側円筒部42は、円筒状の部材である。図2、図5に示すように、後方側の開口部には、上述のノズル本体20の鍔部28を収容するための段差43が形成されている。 The outer cylindrical portion 42 is a cylindrical member. As shown in FIGS. 2 and 5, a step 43 is formed in the opening on the rear side to accommodate the flange 28 of the nozzle body 20 described above.

2個の連結部52は、それぞれ、外側円筒部42の外周面から外側に突出して形成されている。連結部52には、ネジ穴Bが設けられている。連結部52のネジ穴Bは、ホルダ部40を浴槽接続具(図示省略)に取付けるためのネジ穴である。なお、浴槽接続具は、微細気泡発生ノズル10を浴槽に取付けるための機具である。ホルダ部40内に、ノズル本体20を挿入した後に、浴槽接続具の取付穴(図示省略)と連結部52のネジ穴Bを位置合わせし、ネジ部材(図示省略)をネジ穴Bに螺合させることで、微細気泡発生ノズル10と浴槽接続具が連結される。 The two connecting portions 52 are formed to protrude outward from the outer peripheral surface of the outer cylindrical portion 42 . A screw hole B is provided in the connecting portion 52 . A screw hole B of the connecting portion 52 is a screw hole for attaching the holder portion 40 to a bathtub connector (not shown). The bathtub connector is a device for attaching the microbubble generating nozzle 10 to the bathtub. After inserting the nozzle body 20 into the holder part 40, the mounting hole (not shown) of the bathtub connector and the screw hole B of the connecting part 52 are aligned, and the screw member (not shown) is screwed into the screw hole B. By doing so, the fine bubble generating nozzle 10 and the bathtub connector are connected.

内側円筒部44は、外側円筒部42の内側に収容されて形成されている筒状部材である。内側円筒部44は、4個の接続部48を介して外側円筒部42の内面と接続されている。内側円筒部44と外側円筒部42との間の隙間により、4個の流出口50が形成されている。 The inner cylindrical portion 44 is a cylindrical member that is accommodated inside the outer cylindrical portion 42 . The inner cylindrical portion 44 is connected to the inner surface of the outer cylindrical portion 42 via four connecting portions 48 . A gap between the inner cylindrical portion 44 and the outer cylindrical portion 42 forms four outlets 50 .

内側円筒部44の前方側端部には、円板部46が形成されている。円板部46は、内側円筒部44の前方側端部を閉塞している。円板部46のXY平面における中心部には、Y軸に沿って突出部49が形成されている。突出部49は、円板部46の後側の面から後方に向けて突出する略壁状の突起部材である。図5に顕著に示されるように、突出部49によって、円板部46の後側の面が左右に分断される。図2に示すように、突出部49の先端付近は、後方から前方に向かう方向(即ち、空気溶解加圧水の流れ方向(図2中矢印参照))に沿って見た場合に、当該方向に対してやや傾斜している。言い換えると、突出部49の先端付近は、後方に向かって丸く尖るように形成されている。 A disc portion 46 is formed at the front end portion of the inner cylindrical portion 44 . The disk portion 46 closes the front end of the inner cylindrical portion 44 . A projecting portion 49 is formed along the Y-axis at the central portion of the disk portion 46 in the XY plane. The protruding portion 49 is a substantially wall-shaped protruding member that protrudes rearward from the rear surface of the disk portion 46 . As clearly shown in FIG. 5 , the projecting portion 49 divides the rear surface of the disc portion 46 into right and left sides. As shown in FIG. 2, when viewed from the rear to the front (that is, the direction of flow of the air-dissolved pressurized water (see the arrow in FIG. 2)), the vicinity of the tip of the projecting portion 49 is It is slightly sloping. In other words, the vicinity of the tip of the projecting portion 49 is formed so as to be rounded and sharpened toward the rear.

(ノズル本体20がホルダ部40に支持される状態)
続いて、ノズル本体20がホルダ部40に支持される状態における各構成要素の位置関係について説明する。図1、図2に示すように、ノズル本体20がホルダ部40に支持されることにより、本実施例の微細気泡発生ノズル10が形成される。この状態では、ノズル本体20のうち、減圧管22の下流側端部22b及び鍔部28がホルダ部40内に差し込まれている。具体的には、減圧管22の下流側端部22bは、ホルダ部40の内側円筒部44(後述)内に差し込まれている。また、鍔部28は、外側円筒部42の開口部に形成されている段差43内に収容されている。この際、鍔部28の前面28aは、段差43と当接する。ノズル本体20がホルダ部40に支持されている状態では、減圧管22の上流側端部22aは、ホルダ部40の後方側に突出している。
(State in which the nozzle body 20 is supported by the holder portion 40)
Next, the positional relationship of each component when the nozzle body 20 is supported by the holder portion 40 will be described. As shown in FIGS. 1 and 2, the nozzle body 20 is supported by the holder portion 40 to form the microbubble generating nozzle 10 of this embodiment. In this state, the downstream end 22 b of the decompression tube 22 and the flange 28 of the nozzle body 20 are inserted into the holder 40 . Specifically, the downstream end portion 22b of the decompression tube 22 is inserted into an inner cylindrical portion 44 (described later) of the holder portion 40 . Also, the collar portion 28 is accommodated within a step 43 formed in the opening of the outer cylindrical portion 42 . At this time, the front surface 28 a of the flange 28 abuts on the step 43 . When the nozzle body 20 is supported by the holder portion 40 , the upstream end portion 22 a of the decompression tube 22 protrudes rearward from the holder portion 40 .

図2に示すように、ノズル本体20がホルダ部40に支持される状態では、突出部49の先端部分は、減圧管22の下流側端部22bに対向して配置される。さらに言うと、突出部49の先端部分は、区画壁25の前端部と対向している。そして、この状態では、減圧管22の下流側端部22bと円板部46とが対向するように配置される。 As shown in FIG. 2 , when the nozzle body 20 is supported by the holder portion 40 , the tip portion of the projecting portion 49 is arranged to face the downstream end portion 22 b of the decompression tube 22 . Furthermore, the tip portion of the projecting portion 49 faces the front end portion of the partition wall 25 . In this state, the downstream end 22b of the decompression tube 22 and the disc portion 46 are arranged to face each other.

ノズル本体20がホルダ部40に支持されることにより、ノズル本体20とホルダ部40とによって、流路空間62、通路64、流路空間66、及び、通路68が形成される。流路空間62、通路64、流路空間66、通路68は、いずれも、空気溶解加圧水をこの順で流通させるための空間及び通路である。 By supporting the nozzle body 20 on the holder portion 40 , a channel space 62 , a passage 64 , a channel space 66 and a passage 68 are formed by the nozzle body 20 and the holder portion 40 . The channel space 62, the passage 64, the channel space 66, and the passage 68 are spaces and passages for circulating the air-dissolved pressurized water in this order.

流路空間62は、減圧管22の下流側端部22bと円板部46との間に形成される。流路空間62の流路面積は、どの部分においても、上述の出口側開口部26の流路面積の合計面積よりも大きい。詳しく言うと、減圧管22の下流側端部22bの前方における、下流側端部22bの延長線と突出部49との間の空間のXY平面上の面積、および、下流側端部22bと円板部46との間の空間の面積(より詳しくは、円板部46のXY平面上の中心から垂直に伸びる軸線を中心軸とし、かつ、XY平面上における上記中心軸と下流側端部22bの外側とを結ぶ線を半径とする仮想的な円柱のうち、下流側端部22bと円板部46との間の範囲の外側面部分の面積)のいずれもが、上述の出口側開口部26の流路面積の合計面積よりも大きい。 A channel space 62 is formed between the downstream end 22b of the decompression tube 22 and the disc portion 46 . The channel area of the channel space 62 is larger than the total area of the above-described outlet-side openings 26 at any portion. Specifically, in front of the downstream end 22b of the pressure reducing tube 22, the area on the XY plane of the space between the extension line of the downstream end 22b and the protrusion 49, and the downstream end 22b and the circle The area of the space between the plate portion 46 (more specifically, the axis extending perpendicularly from the center on the XY plane of the disk portion 46 is the central axis, and the above-mentioned central axis on the XY plane and the downstream end 22b of the virtual cylinder whose radius is the line connecting the outside of the outlet side opening larger than the total area of the 26 channel areas.

通路64は、流路空間62の下流側に形成される。通路64は、内側円筒部44の内面と、内側円筒部44内に配置された減圧管22の外面との間に形成される。ここで、通路64の流路面積(即ちXY平面上の面積)は、上述の流路空間62のどの部分の流路面積よりも大きい。 A passageway 64 is formed downstream of the channel space 62 . Passage 64 is formed between the inner surface of inner cylindrical portion 44 and the outer surface of vacuum tube 22 disposed within inner cylindrical portion 44 . Here, the channel area of the passage 64 (that is, the area on the XY plane) is larger than the channel area of any portion of the channel space 62 described above.

流路空間66は、通路64の下流側に形成される。流路空間66は、内側円筒部44の後端と鍔部28の前面28aとの間に形成される。流路空間66は、内側円筒部44の後端、外側円筒部42の内面、減圧管22の外面、及び、鍔部28の前面28aによって画定される空間である。流路空間66の流路面積は、どの部分においても、上述の通路64の流路面積よりも大きい。詳しく言うと、内側円筒部44の後端と減圧管22の外面の間の空間のXY平面上の面積、内側円筒部44の後端と鍔部28の前面28aとの間の空間の面積(より詳しくは、円板部46のXY平面上の中心から垂直に伸びる軸線を中心軸とし、かつ、XY平面上における上記中心軸と内側円筒部44の外側とを結ぶ線を半径とする仮想的な円柱のうち、内側円筒部44の後端と前面28aとの間の範囲の外側面部分の面積)、および、内側円筒部44の後端と外側円筒部42の内面との間の空間のXY平面上の面積、のいずれもが、上述の通路64の流路面積よりも大きい。 A channel space 66 is formed downstream of the passage 64 . A flow passage space 66 is formed between the rear end of the inner cylindrical portion 44 and the front surface 28 a of the collar portion 28 . The flow passage space 66 is a space defined by the rear end of the inner cylindrical portion 44 , the inner surface of the outer cylindrical portion 42 , the outer surface of the decompression tube 22 , and the front surface 28 a of the collar portion 28 . The flow area of the flow space 66 is larger than the flow area of the passage 64 described above at any portion. Specifically, the area on the XY plane of the space between the rear end of the inner cylindrical portion 44 and the outer surface of the decompression tube 22, the area of the space between the rear end of the inner cylindrical portion 44 and the front surface 28a of the collar portion 28 ( More specifically, the center axis is an axis extending perpendicularly from the center of the disk portion 46 on the XY plane, and the radius is a line connecting the center axis on the XY plane and the outside of the inner cylindrical portion 44. area of the outer surface portion of the range between the rear end of the inner cylindrical portion 44 and the front surface 28a), and the space between the rear end of the inner cylindrical portion 44 and the inner surface of the outer cylindrical portion 42 area on the XY plane is larger than the passage area of the passage 64 described above.

通路68は、流路空間66の下流側に形成される。通路68は、流路空間66と流出口50とを接続する通路である。通路68は、外側円筒部42の内面と内側円筒部44の外面との間の隙間によって形成される。ここで、通路68の流路面積(即ちXY平面上の面積)は、上述の流路空間66のどの部分の流路面積よりも大きい。 A passageway 68 is formed downstream of the channel space 66 . A passage 68 is a passage that connects the flow passage space 66 and the outlet 50 . Passage 68 is formed by a gap between the inner surface of outer cylindrical portion 42 and the outer surface of inner cylindrical portion 44 . Here, the channel area of the passage 68 (that is, the area on the XY plane) is larger than the channel area of any portion of the channel space 66 described above.

(空気溶解加圧水の流れ)
図2、図4を参照して、微細気泡発生ノズル10内における空気溶解加圧水の流れ、及び、それに伴って微細気泡が形成される過程について説明する。図2、図4において、実線矢印が空気溶解加圧水の流路を示している。
(Flow of air-dissolved pressurized water)
2 and 4, the flow of the air-dissolved pressurized water in the microbubble generating nozzle 10 and the accompanying process of forming microbubbles will be described. In FIGS. 2 and 4, solid arrows indicate the flow path of the air-dissolved pressurized water.

図2、図4に示すように、まず、ノズル本体20の導入口23を介して、外部から空気溶解加圧水が減圧管22内に導入される。この時点における空気溶解加圧水の圧力は、大気圧よりも大きい。 As shown in FIGS. 2 and 4 , first, air-dissolved pressurized water is introduced into the decompression pipe 22 from the outside through the inlet 23 of the nozzle body 20 . The pressure of the air-dissolved pressurized water at this point is greater than the atmospheric pressure.

導入口23から導入された空気溶解加圧水は、導入口23よりも開口面積が小さい入口側開口部24を通過する。これにより、空気溶解加圧水の流速が上昇し、空気溶解加圧水が大気圧よりも低い圧力まで減圧される(即ちベンチュリー効果による減圧)。空気溶解加圧水が減圧されることにより、空気溶解加圧水に溶解していた空気が析出し、微細気泡の元になる気泡(気泡核とも言う)が発生する。 The air-dissolved pressurized water introduced from the introduction port 23 passes through the inlet side opening 24 having an opening area smaller than that of the introduction port 23 . As a result, the flow velocity of the air-dissolved pressurized water increases, and the pressure of the air-dissolved pressurized water is reduced to a pressure lower than the atmospheric pressure (that is, decompression due to the Venturi effect). When the pressure of the air-dissolved pressurized water is reduced, the air dissolved in the air-dissolved pressurized water is precipitated, and air bubbles (also called bubble nuclei) that are the origin of fine air bubbles are generated.

そして、本実施例では、減圧管22に連通孔30が開口されているため、空気溶解加圧水が入口側開口部24を通過することに伴うベンチュリー効果によって減圧管22内に負圧が生じる場合に、その負圧によって、外部から連通孔30を通って空気溶解加圧水が減圧管22内に引き込まれる。図4に示すように、連通孔30から減圧管22内に引き込まれた空気溶解加圧水は、減圧管22内を入口側開口部24から出口側開口部26に向けて流れる空気溶解加圧水のうちの減圧管22内周壁付近の空気溶解加圧水の流れと衝突する。その結果、内周壁付近の流速が径方向中心付近の流速よりも遅くなる。内周壁付近と中心付近の流速差が大きくなることで、微細気泡の元になる気泡核がより多く生じる。 In this embodiment, since the communication hole 30 is opened in the decompression tube 22, when a negative pressure is generated in the decompression tube 22 due to the Venturi effect associated with the passage of the air-dissolved pressurized water through the inlet side opening 24, , the air-dissolved pressurized water is drawn into the decompression tube 22 from the outside through the communication hole 30 by the negative pressure. As shown in FIG. 4, the air-dissolved pressurized water drawn into the decompression tube 22 through the communication hole 30 is part of the air-dissolved pressurized water that flows through the decompression tube 22 from the inlet side opening 24 toward the outlet side opening 26. It collides with the flow of air-dissolved pressurized water near the inner peripheral wall of the decompression pipe 22 . As a result, the flow velocity near the inner peripheral wall becomes slower than the flow velocity near the radial center. As the difference in flow velocity between the vicinity of the inner peripheral wall and the vicinity of the center increases, more bubble nuclei, which are sources of fine bubbles, are generated.

上記の通り、本実施例では、減圧管22は、入口側開口部24から出口側開口部26に向けて流路面積が増加するように形成されている。そのため、入口側開口部24を通過したことで減圧された減圧管22内の空気溶解加圧水が入口側開口部24から出口側開口部26に向かって減圧管22内を流れる間に、空気溶解加圧水の流速が低下する。流速が低下する結果、空気溶解加圧水が増圧される。空気溶解加圧水が増圧されることにより、空気溶解加圧水に含まれる気泡の一部が分裂して微細気泡になる。 As described above, in this embodiment, the decompression tube 22 is formed so that the passage area increases from the inlet-side opening 24 toward the outlet-side opening 26 . Therefore, while the air-dissolved pressurized water in the decompression pipe 22 decompressed by passing through the entrance-side opening 24 flows through the decompression pipe 22 from the entrance-side opening 24 toward the exit-side opening 26, the air-dissolved pressurized water flow velocity decreases. As a result of the decrease in flow velocity, the pressure of the air-dissolved pressurized water is increased. By increasing the pressure of the air-dissolved pressurized water, some of the air bubbles contained in the air-dissolved pressurized water split into fine air bubbles.

出口側開口部26に向かって減圧管22内を流れてきた空気溶解加圧水は、出口側開口部26から流路空間62内へと排出される。上記の通り、流路空間62の流路面積は、出口側開口部26の流路面積より大きい。そのため、出口側開口部26を通って流路空間62内へと排出された空気溶解加圧水の流速はさらに低下する。これにより、空気溶解加圧水はさらに増圧される。その結果、空気溶解加圧水に含まれる気泡の一部がさらに分裂して微細気泡になる。 The air-dissolved pressurized water that has flowed through the decompression tube 22 toward the outlet-side opening 26 is discharged from the outlet-side opening 26 into the channel space 62 . As described above, the channel area of the channel space 62 is larger than the channel area of the outlet opening 26 . Therefore, the flow velocity of the air-dissolved pressurized water discharged into the channel space 62 through the outlet-side opening 26 further decreases. This further increases the pressure of the air-dissolved pressurized water. As a result, some of the bubbles contained in the air-dissolved pressurized water are further divided into fine bubbles.

また、流路空間62内へと排出された空気溶解加圧水は、円板部46に衝突する。この際、流路空間62内へと排出された空気溶解加圧水の一部は、突出部49に衝突した後で円板部46に衝突する。これにより、空気溶解加圧水が流れる向きが変更されるとともに、空気溶解加圧水の流速がさらに低下する。空気溶解加圧水がさらに増圧され、結果として、空気溶解加圧水に含まれる気泡の一部がさらに分裂して微細気泡になる。 Also, the air-dissolved pressurized water discharged into the channel space 62 collides with the disk portion 46 . At this time, part of the air-dissolved pressurized water discharged into the channel space 62 collides with the disk portion 46 after colliding with the projecting portion 49 . As a result, the direction in which the air-dissolved pressurized water flows is changed, and the flow velocity of the air-dissolved pressurized water further decreases. The pressure of the air-dissolved pressurized water is further increased, and as a result, some of the bubbles contained in the air-dissolved pressurized water are further split into fine bubbles.

円板部46に衝突した後の空気溶解加圧水は、通路64を通過して流路空間66内へと排出される。上記の通り、通路64の流路面積は、流路空間62のどの部分の流路面積よりも大きい。そして、流路空間66の流路面積は、通路64の流路面積よりも大きい。そのため、通路64を通過して流路空間66内へと排出された空気溶解加圧水の流速はさらに低下する。空気溶解加圧水がさらに増圧され、結果として、空気溶解加圧水に含まれる気泡の一部がさらに分裂して微細気泡になる。 After colliding with the disk portion 46 , the air-dissolved pressurized water passes through the passage 64 and is discharged into the flow passage space 66 . As described above, the flow area of passage 64 is greater than the flow area of any portion of flow space 62 . The channel area of the channel space 66 is larger than the channel area of the passage 64 . Therefore, the flow velocity of the air-dissolved pressurized water discharged into the channel space 66 through the passage 64 further decreases. The pressure of the air-dissolved pressurized water is further increased, and as a result, some of the bubbles contained in the air-dissolved pressurized water are further split into fine bubbles.

そして、流路空間66内へと排出された空気溶解加圧水は、鍔部28の前面28aに衝突する。これにより、空気溶解加圧水が流れる向きが変更されるとともに、空気溶解加圧水の流速がさらに低下する。空気溶解加圧水もさらに増圧される。その結果、空気溶解加圧水に含まれる気泡の一部がさらに分裂して微細気泡になる。 Then, the air-dissolved pressurized water discharged into the flow path space 66 collides with the front surface 28 a of the collar portion 28 . As a result, the direction in which the air-dissolved pressurized water flows is changed, and the flow velocity of the air-dissolved pressurized water further decreases. The air-dissolved pressurized water is also further pressurized. As a result, some of the bubbles contained in the air-dissolved pressurized water are further divided into fine bubbles.

鍔部28の前面28aに衝突した後の空気溶解加圧水は、通路68を通過し、流出口50から流出箇所(浴槽等)に向けて流出する。上記の通り、通路68の流路面積は、流路空間66のどの部分の流路面積よりも大きい。通路68を通過する空気溶解加圧水の流速はさらに低下する。そして、流出箇所に空気溶解加圧水が流出されることにより、空気溶解加圧水の流速がさらに低下し、空気溶解加圧水はさらに増圧される。その結果、空気溶解加圧水に含まれる気泡の一部がさらに分裂して微細気泡になる。 After colliding with the front surface 28a of the flange 28, the air-dissolved pressurized water passes through the passage 68 and flows out from the outflow port 50 toward the outflow location (such as a bathtub). As described above, the flow area of passage 68 is greater than the flow area of any portion of flow space 66 . The flow rate of air-dissolved pressurized water through passageway 68 is further reduced. As the air-dissolved pressurized water flows out to the outflow location, the flow velocity of the air-dissolved pressurized water further decreases, and the pressure of the air-dissolved pressurized water is further increased. As a result, some of the bubbles contained in the air-dissolved pressurized water are further divided into fine bubbles.

以上、本実施例の微細気泡発生ノズル10の構成及び作用について説明した。上記の通り、本実施例では、ノズル本体20の減圧管22に連通孔30が開口されているため、ベンチュリー効果によって減圧管22内に生じる負圧によって連通孔30を通って外部から空気溶解加圧水が減圧管22内に引き込まれる。その結果、連通孔30から引き込まれた空気溶解加圧水が、減圧管22内を入口側開口部24から出口側開口部26に向けて流れる内周壁付近の空気溶解加圧水の流れと衝突し、内周壁付近の流速が径方向中心付近の流速よりも遅くなる(図4参照)。内周壁付近と中心付近の流速差が大きくなることで、微細気泡の元になる気泡核がより多く生じる。その結果、本実施例の微細気泡発生ノズル10によると、流出箇所に流出される空気溶解加圧水には、微細気泡を大量に含ませることができる。 The configuration and operation of the microbubble generating nozzle 10 of this embodiment have been described above. As described above, in this embodiment, since the pressure reducing tube 22 of the nozzle body 20 has the communicating hole 30, the negative pressure generated in the pressure reducing tube 22 by the venturi effect causes the air-dissolved pressurized water to flow from the outside through the communicating hole 30. is drawn into the vacuum tube 22 . As a result, the air-dissolved pressurized water drawn from the communication hole 30 collides with the flow of the air-dissolved pressurized water near the inner peripheral wall flowing from the inlet-side opening 24 toward the outlet-side opening 26 in the decompression tube 22, The flow velocity in the vicinity becomes slower than the flow velocity in the vicinity of the radial center (see FIG. 4). As the difference in flow velocity between the vicinity of the inner peripheral wall and the vicinity of the center increases, more bubble nuclei, which are sources of fine bubbles, are generated. As a result, according to the microbubble generating nozzle 10 of the present embodiment, the air-dissolved pressurized water flowing out to the outflow location can contain a large amount of microbubbles.

また、本実施例では、連通孔30の開口面積は、入口側開口部24の開口面積よりも小さい。そのため、連通孔30の開口面積が入口側開口部24の開口面積以上である構成を採用する場合に比べて、減圧管22内で発生する負圧によって外部から連通孔30を通って減圧管22内に空気溶解加圧水が引き込まれ易くなる。即ち、減圧管22内で発生する負圧を有効に働かせることができる。 Further, in this embodiment, the opening area of the communication hole 30 is smaller than the opening area of the inlet side opening 24 . Therefore, compared to the case where the opening area of the communication hole 30 is equal to or larger than the opening area of the inlet side opening 24, the negative pressure generated in the pressure reduction tube 22 causes the pressure reduction tube 22 to pass through the communication hole 30 from the outside. Air-dissolved pressurized water is likely to be drawn inside. That is, the negative pressure generated within the decompression tube 22 can be effectively used.

また、本実施例では、連通孔30が形成されている部分(即ち特定部分)における減圧管22の開口面積は、入口側開口部24の開口面積とほぼ等しい。即ち、本実施例では、入口側開口部24から見た開口面積の増分がほぼない範囲内に連通孔30が形成される。このような特定部分を通過する空気溶解加圧水には比較的大きい負圧が生じる。そのため、連通孔30を通って外部から減圧管22内に空気溶解加圧水が引き込まれやすくなる。減圧管22内で発生する負圧をより有効に働かせることができる。 Further, in this embodiment, the opening area of the decompression tube 22 at the portion where the communication hole 30 is formed (that is, the specific portion) is substantially equal to the opening area of the inlet side opening 24 . That is, in this embodiment, the communication hole 30 is formed within a range where there is almost no increase in opening area when viewed from the inlet side opening 24 . A relatively large negative pressure is generated in the air-dissolved pressurized water passing through such a specific portion. Therefore, the air-dissolved pressurized water is easily drawn into the decompression tube 22 from the outside through the communication hole 30 . The negative pressure generated within the decompression tube 22 can be used more effectively.

以上、実施例について詳細に説明したが、これらは例示に過ぎず、特許請求の範囲を限定するものではない。特許請求の範囲に記載の技術には、以上に例示した具体例を様々に変形、変更したものが含まれる。 Although the embodiments have been described in detail above, these are merely examples and are not intended to limit the scope of the claims. The technology described in the claims includes various modifications and changes of the specific examples illustrated above.

(変形例1)上記の実施例では、連通孔30が形成されている部分(即ち特定部分)における減圧管22の開口面積は、入口側開口部24の開口面積とほぼ等しい。これに限られず、連通孔30が形成されている部分(即ち特定部分)における減圧管22の開口面積は、入口側開口部24の開口面積以上であって110%以内であればよい。即ち、減圧管22のうち、入口側開口部24から見た開口面積の増分が10%以内である範囲内に連通孔30が形成されればよい。この範囲も、依然として入口側開口部24の通過直後の範囲であるため、この範囲を通過する空気溶解加圧水には比較的大きい負圧が生じる。 (Modification 1) In the embodiment described above, the opening area of the decompression tube 22 at the portion where the communication hole 30 is formed (that is, the specific portion) is substantially equal to the opening area of the inlet side opening 24 . However, the opening area of the decompression tube 22 at the portion where the communication hole 30 is formed (that is, the specific portion) may be greater than or equal to the opening area of the inlet side opening 24 and within 110%. That is, the communication hole 30 may be formed within a range in which the increase in opening area of the decompression tube 22 as viewed from the inlet side opening 24 is within 10%. Since this range is also the range immediately after passing through the inlet side opening 24, a relatively large negative pressure is generated in the air-dissolved pressurized water passing through this range.

(変形例2)上記の実施例では、各入口側開口部24よりも下流側であって、各入口側開口部24の通過直後の部分(特定部分)に、減圧管22の外周壁と内周壁とを連通する連通孔30が1個ずつ開口されている。これに限られず、変形例では、特定部分において、減圧管22の径方向に沿って複数個の連通孔30が開口されていてもよい。その場合、複数個の連通孔30の合計開口面積が入口側開口部24の開口面積より小さければよい。 (Modification 2) In the above-described embodiment, the outer peripheral wall and the inner wall of the decompression tube 22 are provided downstream of each inlet-side opening 24 and immediately after passing through each inlet-side opening 24 (specific portion). A communication hole 30 communicating with the peripheral wall is opened one by one. Not limited to this, in a modification, a plurality of communication holes 30 may be opened along the radial direction of the decompression tube 22 in a specific portion. In that case, the total opening area of the plurality of communication holes 30 should be smaller than the opening area of the inlet side opening 24 .

(変形例3)さらに、変形例では、連通孔30の開口面積が入口側開口部24の開口面積以上であってもよい。 (Modification 3) Furthermore, in a modification, the opening area of the communication hole 30 may be equal to or larger than the opening area of the inlet-side opening 24 .

(変形例4)上記の各実施例では、微細気泡発生ノズルは、空気が水に溶解した空気溶解加圧水の供給を受け、空気溶解加圧水内の空気を析出させて微細気泡に変え、空気の微細気泡を含む水を流出箇所に供給する。これに限られず、微細気泡発生ノズルは、空気以外の他の気体(例えば、炭酸ガスや水素等)が水に溶解した気体溶解加圧水の供給を受け、当該気体溶解加圧水内の気体を析出させて微細気泡に変え、その期待の微細気泡を含む水を流出箇所に供給するようにしてもよい。即ち、「気体」は空気に限られず、炭酸ガスや水素等の任意の気体であってもよい。 (Modification 4) In each of the above embodiments, the microbubble generating nozzle receives supply of air-dissolved pressurized water in which air is dissolved in water, precipitates the air in the air-dissolved pressurized water, converts it into microbubbles, and converts the air into microbubbles. Water containing air bubbles is supplied to the outflow point. Not limited to this, the fine bubble generating nozzle is supplied with gas-dissolved pressurized water in which gas other than air (for example, carbon dioxide gas, hydrogen, etc.) is dissolved in water, and precipitates the gas in the gas-dissolved pressurized water. Instead of microbubbles, water containing the expected microbubbles may be supplied to the outflow location. That is, the "gas" is not limited to air, and may be any gas such as carbon dioxide or hydrogen.

本明細書または図面に説明した技術要素は、単独であるいは各種の組合せによって技術的有用性を発揮するものであり、出願時の請求項に記載の組合せに限定されるものではない。また、本明細書または図面に例示した技術は複数目的を同時に達成し得るものであり、そのうちの一つの目的を達成すること自体で技術的有用性を持つものである。 The technical elements described in this specification or in the drawings exhibit technical utility either singly or in various combinations, and are not limited to the combinations described in the claims as filed. In addition, the techniques exemplified in this specification or drawings can simultaneously achieve a plurality of purposes, and achieving one of them has technical utility in itself.

10:微細気泡発生ノズル
20:ノズル本体
22:減圧管
22a:上流側端部
22b:下流側端部
23:導入口
24:入口側開口部
25:区画壁
26:出口側開口部
28:鍔部
28a:前面
30:連通孔
40:ホルダ部
42:外側円筒部
43:段差
44:内側円筒部
46:円板部
48:接続部
49:突出部
50:流出口
52:連結部
62:流路空間
64:通路
66:流路空間
68:通路
B:ネジ穴
10: Microbubble generating nozzle 20: Nozzle body 22: Decompression tube 22a: Upstream end 22b: Downstream end 23: Inlet 24: Inlet side opening 25: Partition wall 26: Outlet side opening 28: Collar 28a: Front surface 30: Communication hole 40: Holder portion 42: Outer cylindrical portion 43: Step 44: Inner cylindrical portion 46: Disc portion 48: Connecting portion 49: Protruding portion 50: Outlet 52: Connecting portion 62: Channel space 64: Passage 66: Flow path space 68: Passage B: Screw hole

Claims (3)

上流側端部から下流側端部に向けて、気体が水に溶解している気体溶解加圧水を通過させる減圧管と、
前記上流側端部に開口され、前記気体溶解加圧水を供給するための給水手段から前記減圧管内に前記気体溶解加圧水を導入する導入口と、
前記減圧管のうち前記導入口よりも下流側に設けられ、前記減圧管内に導入された前記気体溶解加圧水を通過させる入口側開口部と、
前記入口側開口部よりも下流側である前記下流側端部に開口された出口側開口部と、
を備えており、
前記入口側開口部の開口面積は前記導入口の開口面積よりも小さく、
前記出口側開口部の開口面積は前記入口側開口部の開口面積よりも大きく、
前記減圧管のうち、前記入口側開口部よりも下流側であって前記入口側開口部近傍の特定部分に、前記減圧管の外周壁と内周壁とを連通する少なくとも1個の連通孔が開口されており、
前記導入口および前記少なくとも1個の連通孔が、前記給水手段から前記気体溶解加圧水が供給される給水空間内に配置されている
微細気泡発生ノズル本体。
a decompression pipe for passing gas-dissolved pressurized water in which gas is dissolved in water from the upstream end to the downstream end;
an inlet opening at the upstream end for introducing the gas-dissolved pressurized water into the decompression pipe from a water supply means for supplying the gas-dissolved pressurized water;
an inlet-side opening provided downstream of the introduction port in the decompression tube and allowing the gas-dissolved pressurized water introduced into the decompression tube to pass through;
an outlet-side opening opened at the downstream end that is downstream of the inlet-side opening;
and
The opening area of the inlet side opening is smaller than the opening area of the inlet,
The opening area of the outlet side opening is larger than the opening area of the inlet side opening,
At least one communication hole that communicates between an outer peripheral wall and an inner peripheral wall of the decompression tube is opened in a specific portion of the decompression tube that is downstream of the inlet side opening and in the vicinity of the inlet side opening. has been
The inlet and the at least one communication hole are arranged in a water supply space to which the gas-dissolved pressurized water is supplied from the water supply means,
Fine bubble generation nozzle body.
前記少なくとも1個の連通孔の合計開口面積は、前記入口側開口部の開口面積よりも小さい、請求項1に記載の微細気泡発生ノズル本体。 2. The fine bubble generating nozzle body according to claim 1, wherein a total opening area of said at least one communication hole is smaller than an opening area of said inlet side opening. 前記特定部分における前記減圧管の開口面積は、前記入口側開口部の開口面積以上であって110%以内である、請求項1又は2に記載の微細気泡発生ノズル本体。 3. The fine bubble generating nozzle body according to claim 1 or 2, wherein the opening area of the decompression tube in the specific portion is equal to or larger than the opening area of the inlet side opening and is within 110%.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012176335A (en) 2011-02-25 2012-09-13 Seiwa Kogyo Kk Microbubble generator
JP2014024012A (en) 2012-07-27 2014-02-06 Mitsubishi Electric Corp Ejector
JP2015100720A (en) 2013-11-21 2015-06-04 スプレーイングシステムスジャパン株式会社 Air-spraying microbubble nozzle
JP2019136648A (en) 2018-02-09 2019-08-22 リンナイ株式会社 Cleaning liquid generator

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Publication number Priority date Publication date Assignee Title
JPH06315654A (en) * 1993-04-30 1994-11-15 Nobuyuki Ishimatsu Water saving device for shower head
JPH1190275A (en) * 1997-09-17 1999-04-06 Hiroshi Saito Negative pressure air fine bubble generator

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012176335A (en) 2011-02-25 2012-09-13 Seiwa Kogyo Kk Microbubble generator
JP2014024012A (en) 2012-07-27 2014-02-06 Mitsubishi Electric Corp Ejector
JP2015100720A (en) 2013-11-21 2015-06-04 スプレーイングシステムスジャパン株式会社 Air-spraying microbubble nozzle
JP2019136648A (en) 2018-02-09 2019-08-22 リンナイ株式会社 Cleaning liquid generator

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