JP2012072594A - Foamy water discharge device - Google Patents

Foamy water discharge device Download PDF

Info

Publication number
JP2012072594A
JP2012072594A JP2010217993A JP2010217993A JP2012072594A JP 2012072594 A JP2012072594 A JP 2012072594A JP 2010217993 A JP2010217993 A JP 2010217993A JP 2010217993 A JP2010217993 A JP 2010217993A JP 2012072594 A JP2012072594 A JP 2012072594A
Authority
JP
Japan
Prior art keywords
water
rectifying
bubble
flow path
diameter side
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.)
Granted
Application number
JP2010217993A
Other languages
Japanese (ja)
Other versions
JP5854365B2 (en
Inventor
Ryohei Yasaka
遼平 八板
Koji Takeda
宏二 武田
Hidekazu Kitaura
秀和 北浦
Tomohiro Kudo
智博 工藤
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.)
Toto Ltd
Original Assignee
Toto Ltd
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 Toto Ltd filed Critical Toto Ltd
Priority to JP2010217993A priority Critical patent/JP5854365B2/en
Publication of JP2012072594A publication Critical patent/JP2012072594A/en
Application granted granted Critical
Publication of JP5854365B2 publication Critical patent/JP5854365B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Domestic Plumbing Installations (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a foamy water discharge device which can discharge bubble-mixed water with an increased bubble-mixing rate in a low flow rate stage, and even in a high flow rate stage, suppresses increase in the flow velocity and prevents water splash and appearance deterioration or the like during its usage.SOLUTION: A foamy water discharge device comprises: an orifice part which jets the water that has flowed into a main body part towards the downstream side of an inner flow path while increasing flow velocity of the water; a bubble-mixing part 300 that mixes the water with air to make bubble-mixed water; and a rectifying part 400 that rectifies the bubble-mixed water and discharge the water through a discharge port 113. The orifice is placed so as to block the inner flow path and has a pressure-reducing plate with a number of holes. The bubble-mixing part 300 includes a slope part 320 of which the diameter reduces downward like a funnel so that the water jetted from the number of holes is directed to the center of the inner flow path. The rectifying part 400 includes a rectifying grid to rectify the bubble-mixed water, and among annular rectifying ribs 411, the most outside annular rectifying ribs 411 are placed in the inner diameter side of the line extended from the slope surface of the slope part 320.

Description

本発明は、気泡混入水を吐出することが可能な泡沫吐水装置に関する。   The present invention relates to a foam water spouting device capable of discharging bubble-containing water.

従来、シンクへの着水音を低減させたり、水跳ねを抑制したりするために、吐水中に気泡を混入させた気泡混入水を吐出する泡沫吐水装置が利用されてきた。また、近年では節水志向の高まりによって、吐水する水の流量が2L/min程度の低流量段階から気泡の混入率を高めることで、吐水の量感や流速を上げ、節水しつつも使用時の快適性を向上させるような泡沫吐水装置も提案されている(特許文献1および2)。   Conventionally, in order to reduce the sound of water landing on the sink or to suppress water splashing, a foam water spouting device that discharges water containing air bubbles mixed with air bubbles in water discharge has been used. Also, in recent years, due to the increasing tendency to conserve water, by increasing the bubble mixing rate from the low flow rate stage where the flow rate of discharged water is about 2 L / min, the amount of water discharged and the flow rate are increased, and the user can comfortably use while saving water. Also proposed is a foam water spouting device that improves the performance (Patent Documents 1 and 2).

特許文献1に記載の泡沫吐水装置は、洗浄水流入口と、気泡流吐出口の間で延在する流路の途上に空気混入機構と整流機構とを上流側よりこの順に備えた泡沫吐水口が、継手を介して水栓の先端に設けられる。空気混入機構は、気泡流吐出口と同心の円であり且つ気泡流吐出口よりも大径の円の周上に配設された複数の小孔を有し流路を塞いで配設された減圧板と、減圧板の下流の流路囲壁に形成された空気孔と、空気孔の下流に配設された逆流防止部を有し、整流機構は、逆流防止部の下流で漏斗状に縮径する流路の傾斜部と、傾斜部の下流端から気泡流吐出口へ向けて延在する気泡流吐出口と同心の流路の整流部と、傾斜部と整流部とを連結する流路のR部と、流路の整流部を塞いで配設された整流格子と、整流格子の下流で整流部に接続する整流路とを有し、減圧板より上流に、継手の流路断面積よりも小さな通水流路断面を有する絞り部を設けたことを特徴とする泡沫吐水装置である。   The foam water spouting device described in Patent Document 1 includes a foam water spouting port provided with an air mixing mechanism and a rectifying mechanism in this order from the upstream side in the course of a flow path extending between the washing water flow inlet and the bubble flow discharge port. , Provided at the tip of the faucet through a joint. The air mixing mechanism is a circle concentric with the bubble flow outlet and has a plurality of small holes arranged on the circumference of the circle having a diameter larger than that of the bubble flow outlet, and is arranged to block the flow path. It has a pressure reducing plate, an air hole formed in the flow passage wall downstream of the pressure reducing plate, and a backflow prevention unit disposed downstream of the air hole, and the rectifying mechanism is contracted in a funnel shape downstream of the backflow prevention unit. An inclined portion of a diameter channel, a rectifying portion of a flow channel concentric with the bubble flow discharge port extending from the downstream end of the inclined portion toward the bubble flow discharge port, and a flow channel connecting the inclined portion and the rectification portion R section, a rectifying grid disposed to block the rectifying section of the flow path, and a rectifying path connected to the rectifying section downstream of the rectifying grid, and the flow path cross-sectional area of the joint upstream of the decompression plate It is a foam water discharging apparatus characterized by providing the throttle part which has a smaller water flow path cross section.

特許文献2に記載の泡沫吐水口は、洗浄水流入口と、気泡流吐出口と、洗浄水流入口と気泡流吐出口の間で延在する洗浄水流路の途上に配設された空気混入機構と、空気混入機構の下流に配設された整流機構とを備え、空気混入機構は、複数の小孔が形成され洗浄水流路を塞いで配設された減圧板と、減圧板の下流の洗浄水流路囲壁に形成された空気孔と、減圧板の下流で下流へ向けて漏斗状に縮径する洗浄水流路のテーパ部とを有し、整流機構は、テーパ部に接続しテーパ部の下流端と気泡流吐出口との間で延在する洗浄水流路の整流部と、整流部に配設された整流格子とを有し、減圧板の小孔はテーパ部周壁へ差し向けられていることを特徴とする泡沫吐水口である。   The foam spout described in Patent Document 2 includes a cleaning water inlet, a bubble flow outlet, and an air mixing mechanism disposed in the middle of the cleaning water passage extending between the cleaning water inlet and the bubble outlet. A rectifying mechanism disposed downstream of the air mixing mechanism, the air mixing mechanism including a decompression plate formed with a plurality of small holes and closing the cleaning water flow path, and a cleaning water flow downstream of the decompression plate An air hole formed in the passage wall and a taper portion of the washing water flow path having a diameter reduced in a funnel shape downstream from the decompression plate, and the rectifying mechanism is connected to the taper portion and connected to the downstream end of the taper portion And a rectifying part of the washing water flow channel extending between the bubble flow outlet and the rectifying grid disposed in the rectifying part, and the small hole of the decompression plate is directed to the peripheral wall of the tapered part It is a foam spout characterized by.

特許文献1に記載の泡沫吐水装置は、洗浄水が減圧板の小孔を通過する際、圧力エネルギーが運動エネルギーに変換され小孔からの噴流は流速を高め、この噴流が粘性により周囲の空気を巻き込むエジェクタ効果を空気混入に利用しており、前記複数の小孔から洗浄水を高速で吐出させることで、低流量段階から気泡の混入率を高めることを可能としている。   In the foam spouting device described in Patent Document 1, when washing water passes through the small hole of the decompression plate, the pressure energy is converted into kinetic energy, and the jet flow from the small hole increases the flow velocity. The ejector effect of entraining the air is used for air mixing, and by allowing the washing water to be discharged from the plurality of small holes at a high speed, the bubble mixing rate can be increased from the low flow rate stage.

特開2002−275969JP 2002-275969 A 国際公開第01/068995号パンフレットInternational Publication No. 01/068995 Pamphlet

気泡混入水は、低流量段階においては、気泡の混入率を高めることで、シンクへの着水音を低減させたり、水跳ねを抑制したりするという基本的な目的を損なわずに、節水しながらも吐水の量感や流速を上げ、快適性を向上させることができる。したがって、特許文献1及び特許文献2に記載の泡沫吐水装置においては、低流量段階での気泡混入率を高めるような設計上の工夫がなされている。   In the low-flow stage, the water containing bubbles is saved without increasing the mixing rate of bubbles, thereby reducing the sound of landing on the sink and suppressing water splashing. However, it is possible to increase the feeling of water discharge and the flow velocity, and to improve comfort. Therefore, in the foam water spouting device described in Patent Literature 1 and Patent Literature 2, a design contrivance is made to increase the bubble mixing rate in the low flow rate stage.

しかし、実際には、このような低流量段階だけではなく、高流量段階で使用する場合も考えられる。水流量が増え、減圧板の小孔からの噴流の流速が高まり過ぎると、気泡流吐出口からの吐水が縮流し、それにより気泡流吐出口から吐出される気泡混入水の流速も高まり、水跳ね等の問題を生じる他、見た目も悪化してしまう。特に、低流量段階における気泡混入率を高めるような設計上の工夫をすればするほど、高流量段階において、この現象も顕著に現れる。   However, actually, not only such a low flow rate stage but also a high flow rate stage may be used. If the water flow rate increases and the flow velocity of the jet from the small hole in the decompression plate increases too much, the water discharged from the bubble flow discharge port contracts, thereby increasing the flow rate of the bubble-containing water discharged from the bubble flow discharge port. In addition to causing problems such as splashing, the appearance also deteriorates. In particular, this phenomenon becomes more prominent at the high flow rate stage as the design is devised to increase the bubble mixing rate at the low flow rate stage.

本発明はこのような課題に鑑みてなされたものであり、低流量段階では気泡混入率を高めた気泡混入水を吐出することが可能でありつつ、高流量段階でも流速の高まりを抑制し、使用時の水跳ねや見た目の悪化等の問題を防ぐことが可能な泡沫吐水装置を提供することを目的とする。   The present invention has been made in view of such a problem, while it is possible to discharge the bubble mixed water with an increased bubble mixing rate in the low flow rate stage, while suppressing an increase in the flow rate even in the high flow rate stage, An object of the present invention is to provide a foam water spouting device capable of preventing problems such as water splashing during use and deterioration of appearance.

上記課題を解決するためになされた本発明は、流入口から流入した水を気泡混入水として吐出口から吐出することができる泡沫吐水装置であって、流入口から吐出口に至るまでの内部流路が形成された本体部と、流入口から流入した水を内部流路の下流側に向けて流速を大きくして噴射するオリフィス部と、内部流路内に空気を導入する空気孔が形成され、空気孔から導入された空気をオリフィス部から噴射された水に混入して気泡混入水とする気泡混入部と、気泡混入部の下流に配設され、吐出口から気泡混入水を整流させて吐出する整流部と、を備え、オリフィス部は、内部流路を遮るように設けられ、複数の孔が形成された減圧板を有し、気泡混入部は、複数の孔から噴射された水が、内部流路の中心方向に向かうように、下流側に向けて漏斗状に縮径した傾斜部を有し、整流部は、気泡混入部で生成した気泡混入水を整流するための整流格子を有し、整流格子は、環状の整流リブと、放射状の整流リブと、を有し、環状の整流リブのうち、最も外径側に配設される環状の整流リブは、傾斜部の斜面の延長線よりも内径側に配設されたことを特徴とする。   The present invention made to solve the above problems is a foam water spouting device capable of discharging water flowing in from an inflow port from a discharge port as bubble-mixed water, and an internal flow from the inflow port to the discharge port. A main body portion in which a passage is formed, an orifice portion for injecting water flowing in from the inlet toward the downstream side of the internal flow path at a higher flow velocity, and an air hole for introducing air into the internal flow path are formed. The air introduced from the air hole is mixed with the water jetted from the orifice part to make the air bubble mixed water, and the air bubble mixed part is disposed downstream of the air bubble mixed part, and the air bubble mixed water is rectified from the discharge port. The orifice portion is provided so as to block the internal flow path, and has a decompression plate in which a plurality of holes are formed, and the bubble mixing portion has water jetted from the plurality of holes. Towards the center of the internal flow path And the rectifying unit has a rectifying grid for rectifying the bubble mixed water generated in the bubble mixing unit, and the rectifying grid includes an annular rectifying rib and a radial rectifying unit. The annular rectifying rib disposed on the outermost diameter side among the annular rectifying ribs is disposed on the inner diameter side of the extended line of the inclined surface of the inclined portion. .

この発明によれば、気泡混入部において、低流量段階でも効果的に細かい気泡を含む気泡混入水を生成することができるエジェクタ効果を利用して気泡混入水を生成する。そのため、シンクへの着水音を低減させたり、水跳ねを抑制したりするという基本的な目的を損なわずに、節水しながらも吐水の量感や流速を上げ、快適性を向上させることができる。   According to this invention, in the bubble mixing part, the bubble mixed water is generated by utilizing the ejector effect that can effectively generate the bubble mixed water including fine bubbles even at the low flow rate stage. Therefore, without sacrificing the basic purpose of reducing the sound of landing on the sink or suppressing water splash, it is possible to improve the comfort by increasing the amount of water discharged and the flow velocity while saving water. .

この発明によれば、傾斜部は、気泡混入を効率的に行うために、複数の孔から噴射された水が、内部流路の中心方向に向かうように、下流側に向けて漏斗状に縮径している。したがって、低流量段階でも量感のある吐水が可能となり、気泡が混入していない吐水と比較して少ない水量で食器洗いや手洗いをすることができるため、節水に寄与できると共に水跳ねを抑制することもできる。   According to the present invention, the inclined portion contracts in a funnel shape toward the downstream side so that water sprayed from the plurality of holes is directed toward the center of the internal flow path in order to efficiently mix bubbles. It has a diameter. Therefore, it is possible to discharge water with a sense of volume even at a low flow rate stage, and it is possible to do dishwashing and hand washing with a small amount of water compared to water discharged without bubbles, which can contribute to water saving and suppress water splashing. it can.

また、環状の整流リブのうち、最も外径側に配設される環状の整流リブが、傾斜部の斜面の延長線より内径側に配設されたことによって、傾斜部を経て整流部の径内方向へ向かう流れに対向し、流れの抵抗となる。そのため、気泡混入水の流れを減速させつつ径外方向の吐出口へ誘導させることができる。したがって、高流量段階でも吐出口から吐出される気泡混入水の縮流を防ぐと共に、流速の高まりを抑制することができる。そのため、高流量段階での使用時において、水跳ねや見た目の悪化等の問題を防ぐことが可能となっている。   Further, among the annular rectifying ribs, the annular rectifying rib disposed on the outermost diameter side is disposed closer to the inner diameter side than the extended line of the inclined surface of the inclined portion, so that the diameter of the rectifying portion passes through the inclined portion. Opposes the inward flow and acts as a flow resistance. Therefore, it is possible to guide to the discharge port in the radially outward direction while decelerating the flow of the bubble mixed water. Therefore, it is possible to prevent the bubbling water discharged from the discharge port from contracting even at a high flow rate stage and to suppress an increase in the flow velocity. Therefore, it is possible to prevent problems such as water splashing and appearance deterioration during use at the high flow rate stage.

さらに、吐出口の径を傾斜部の内径に比べて大きく設計するほど、径外方向の吐水口へ気泡混入水が供給されにくくなるため、吐水の縮流現象は発生しやすい。しかし、設計やデザイン上の都合によって、吐出口の径を傾斜部の内径に比べて大きくしなくてはならない場合も多い。したがって、この発明のように、傾斜部の斜面の延長線より内径側に、環状の整流リブのうち、最も外径側に配設された整流リブが配設されたことによって、流れを減速させつつ径外方向へ誘導すれば、高流量段階でも吐出口から吐出される気泡混入水の縮流を防ぐと共に、流速の高まりを抑制することができるため、水跳ねや見た目の悪化等の問題を防ぐ効果は大きい。   Furthermore, as the diameter of the discharge port is designed to be larger than the inner diameter of the inclined portion, the bubble-mixed water is less likely to be supplied to the water discharge port in the radially outward direction, so that the water discharge phenomenon tends to occur. However, there are many cases where the diameter of the discharge port has to be made larger than the inner diameter of the inclined portion due to the design or design reasons. Therefore, as in the present invention, the flow is slowed down by arranging the flow straightening rib disposed on the outermost diameter side among the circular flow straightening ribs on the inner diameter side from the extended line of the inclined surface of the inclined portion. However, if guided to the outer diameter direction, it is possible to prevent the bubbling water discharged from the discharge port from constricting even at a high flow rate stage and to suppress the increase of the flow velocity. The effect to prevent is great.

上述したように、本発明によれば、低流量段階では気泡混入率を高めた気泡混入水を吐出することが可能でありつつ、高流量段階でも吐出される気泡混入水の縮流を防ぐと共に、流速の高まりを抑制し、使用時の水跳ねや見た目の悪化等の問題を防ぐことが可能な吐水装置を提供することができる。   As described above, according to the present invention, it is possible to discharge the bubble-containing water with an increased bubble mixing rate at the low flow rate stage, while preventing the contraction of the bubble-containing water discharged even at the high flow rate stage. In addition, it is possible to provide a water discharging device that can suppress an increase in flow velocity and prevent problems such as water splashing during use and deterioration of appearance.

また、本発明に係る泡沫吐水装置において、整流格子は、環状の整流リブと、放射状の整流リブと、により区画化された複数の開口部を有し、最も外径側に配設される環状リブよりも径外方向に配設される複数の開口部は、径外方向に扁平状に形成されたことを特徴とする。   Further, in the foam spouting device according to the present invention, the rectifying grid has a plurality of openings partitioned by an annular rectifying rib and a radial rectifying rib, and is arranged on the outermost diameter side. The plurality of openings disposed in the radially outward direction from the rib are formed in a flat shape in the radially outward direction.

この発明によれば、最も外径側に配設される環状リブよりも径外方向に配設される複数の開口部が、径外方向に扁平状に形成されたことによって、径方向における流れの速度分布の均一化がより促進されるとともに、整流効果が高まり、より吐水の見た目が改善される。この作用により、気泡混入水が吐出口の内径側に偏って吐出する現象を抑制することができるため、高流量段階でも吐出口からの気泡混入水の縮流を防ぐと共に、流速の高まりをより抑制することができる。   According to the present invention, the plurality of openings disposed in the radially outer direction than the annular rib disposed on the outermost diameter side are formed in a flat shape in the radially outward direction, thereby causing a flow in the radial direction. The speed distribution is more uniform, the rectifying effect is increased, and the appearance of water discharge is further improved. This action can suppress the phenomenon in which bubble-containing water is discharged toward the inner diameter side of the discharge port, thereby preventing the bubble-containing water from constricting from the discharge port even at a high flow rate stage and further increasing the flow velocity. Can be suppressed.

また、本発明に係る泡沫吐水装置において、最も外径側に配設される環状の整流リブより径外方向の開口比率は、径内方向の開口比率より大きくしたことを特徴とする。   Moreover, the foam spouting device according to the present invention is characterized in that the opening ratio in the radially outer direction is larger than the opening ratio in the radially inner direction than the annular rectifying rib disposed on the outermost diameter side.

この発明によれば、最も外径側に配設される環状の整流リブより径内方向の開口部の圧力損失を径外方向に比べて大きくし、気泡混入水が外径側の開口部に流れやすくすることによって、気泡混入水が吐出口の内径側に偏って吐出する現象を抑制することができるため、高流量段階でも吐出口からの気泡混入水の縮流を防ぐと共に、流速の高まりをより抑制することができる。   According to the present invention, the pressure loss of the opening portion in the radially inner direction is made larger than that in the radially outer direction than the annular rectifying rib disposed on the outermost diameter side, so that the bubble mixed water enters the opening portion on the outer diameter side. By facilitating the flow, it is possible to suppress the phenomenon in which bubble-containing water is discharged toward the inner diameter side of the discharge port, thereby preventing the bubble-containing water from constricting from the discharge port even at a high flow rate stage and increasing the flow velocity. Can be further suppressed.

本発明によれば、低流量段階では気泡混入率を高めた気泡混入水を吐出することが可能でありつつ、高流量段階でも吐出される気泡混入水の縮流を防ぐと共に、流速の高まりを抑制することができる。そのため、水跳ねや見た目の悪化等の問題を防ぐことが可能な吐水装置を提供することができる。   According to the present invention, it is possible to discharge the bubble-containing water with an increased bubble mixing rate at the low flow rate stage, while preventing the condensate of the bubble-containing water discharged even at the high flow rate stage and increasing the flow velocity. Can be suppressed. Therefore, it is possible to provide a water discharging device that can prevent problems such as water splashing and appearance deterioration.

本発明の実施の形態にかかる泡沫吐水装置を表す断面模式図である。It is a cross-sectional schematic diagram showing the foam water discharging apparatus concerning embodiment of this invention. 泡沫吐水の原理を説明するための断面模式図である。It is a cross-sectional schematic diagram for demonstrating the principle of foam water spouting. 本実施形態の気泡混入水の流れを表す断面模式図である。It is a cross-sectional schematic diagram showing the flow of the bubble mixed water of this embodiment. 本実施形態の気泡混入水の流れを表す断面模式図Cross-sectional schematic diagram showing the flow of bubble-containing water of this embodiment 本発明の泡沫吐水装置内における、水の流れの様子を説明するための断面模式図。The cross-sectional schematic diagram for demonstrating the mode of the flow of the water in the foam water spouting apparatus of this invention. 比較例の水の流れの様子を説明するための断面模式図である。It is a cross-sectional schematic diagram for demonstrating the mode of the flow of the water of a comparative example. 本発明の泡沫吐水装置の整流部の断面図である。It is sectional drawing of the rectification | straightening part of the foam spouting apparatus of this invention. 本発明の泡沫吐水装置の整流部の断面図である。It is sectional drawing of the rectification | straightening part of the foam spouting apparatus of this invention.

以下、添付図面を参照しながら、本発明の実施の形態について説明する。なお、各図面中、同様の構成要素には同一の符号を付して詳細な説明は適宜省略する。   Hereinafter, embodiments of the present invention will be described with reference to the accompanying drawings. In addition, in each drawing, the same code | symbol is attached | subjected to the same component and detailed description is abbreviate | omitted suitably.

本発明の実施形態である吐水装置について図1を参照しながら説明する。
図1は、本発明の実施の形態にかかる泡沫吐水装置を表す断面模式図である。
また、必要に応じて図2および図3も参照しながら説明する。
図2は、泡沫吐水の原理を説明するための断面模式図である。
図3および4は、本実施形態の気泡混入水の流れを表す断面模式図である。
なお、図3および4は、図2に表した領域Aを拡大して眺めた拡大模式図である。
The water discharging apparatus which is embodiment of this invention is demonstrated referring FIG.
FIG. 1 is a schematic cross-sectional view showing a foam water spouting device according to an embodiment of the present invention.
Moreover, it demonstrates, referring also to FIG. 2 and FIG. 3 as needed.
FIG. 2 is a schematic cross-sectional view for explaining the principle of foam water discharge.
3 and 4 are schematic cross-sectional views showing the flow of bubble-containing water according to this embodiment.
3 and 4 are enlarged schematic views in which the area A shown in FIG. 2 is enlarged and viewed.

図1に表したように、本発明の泡沫吐水装置100は、流入口111および吐出口113を有する本体部110と、オリフィス部200と、気泡混入部300と、整流部400と、を備えている。オリフィス部200の上流側には、上絞径部150が設けられている。給水元から流入口111へ流入した水は、内部流路を通って気泡混入水となって吐出口113から吐出される。内部流路では、水は、上絞径部150と、オリフィス部200と、気泡混入部300と、整流部400と、をこの順に通水する。   As shown in FIG. 1, the foam spouting device 100 of the present invention includes a main body 110 having an inflow port 111 and a discharge port 113, an orifice unit 200, a bubble mixing unit 300, and a rectifying unit 400. Yes. An upper reduced diameter portion 150 is provided on the upstream side of the orifice portion 200. The water that has flowed into the inlet 111 from the water supply source passes through the internal flow path and becomes bubble mixed water and is discharged from the discharge port 113. In the internal flow path, water passes through the upper reduced diameter portion 150, the orifice portion 200, the bubble mixing portion 300, and the rectifying portion 400 in this order.

上絞径部150は、環状凸部151と鍔部153とを有し、環状凸部151は、鍔部153から上流側に突出するように形成されている。環状凸部151の中央を含む領域には、流入穴155が形成されている。流入口111から入った水は、上絞径部150に当たることで水圧が減衰され、流入穴155から下流側に流出される。流入穴155から下流側に流出した水は、オリフィス部200へと流入する。   The upper narrowed diameter portion 150 includes an annular convex portion 151 and a flange portion 153, and the annular convex portion 151 is formed so as to protrude upstream from the flange portion 153. An inflow hole 155 is formed in a region including the center of the annular convex portion 151. The water that has entered from the inflow port 111 hits the upper narrowed diameter portion 150 to attenuate the water pressure, and flows out from the inflow hole 155 to the downstream side. The water flowing out from the inflow hole 155 to the downstream side flows into the orifice unit 200.

オリフィス部200は、上絞径部150の下流側に配置されており、減圧板210を有する。   The orifice portion 200 is disposed on the downstream side of the upper reduced diameter portion 150 and has a pressure reducing plate 210.

減圧板210は円形板状の部材である。減圧板210には、複数の孔211が円環を描くように、かつ上絞径部150の鍔部153によって塞がれないように形成されている。   The decompression plate 210 is a circular plate member. The decompression plate 210 is formed so that the plurality of holes 211 draw an annular shape and are not blocked by the flange portion 153 of the upper reduced diameter portion 150.

図2に表したように、オリフィス部200へと流入した水は、外周方向に広がる角度で、複数の孔211から下流の気泡混入部300へと噴射される。   As shown in FIG. 2, the water that has flowed into the orifice unit 200 is jetted from the plurality of holes 211 to the downstream bubble mixing unit 300 at an angle that spreads in the outer circumferential direction.

気泡混入部300は、オリフィス部200の下流側に配置されており、空気導入路310と、傾斜部320と、を有する。空気導入路310の端部には、空気導入路310に導かれた空気を内部流路内に導入する空気孔311が形成されている。   The bubble mixing part 300 is disposed on the downstream side of the orifice part 200 and includes an air introduction path 310 and an inclined part 320. An air hole 311 is formed at the end of the air introduction path 310 to introduce the air guided to the air introduction path 310 into the internal flow path.

傾斜部320は、下流側に向けて漏斗状に縮径した円筒状の部材である。図2に表したように、複数の孔211から噴射された水は、傾斜部320の上流側の面に衝突し、拡径した傾斜部320の壁面に沿って外径側に導かれる水と、内部流路の中心方向に向かうように導かれる水に分かれながら、内部流路全体へ均一に分散される。   The inclined portion 320 is a cylindrical member having a diameter reduced to a funnel shape toward the downstream side. As shown in FIG. 2, the water sprayed from the plurality of holes 211 collides with the upstream surface of the inclined portion 320, and is guided to the outer diameter side along the wall surface of the inclined portion 320 whose diameter has been expanded. While being divided into water guided toward the center of the internal flow path, the water is uniformly dispersed throughout the internal flow path.

このとき、流入口111から水が流入したとき複数の孔211から噴射された水の作用によって、気泡混入部300内は負圧になるので、空気導入路310から内部流路内に空気が導かれる。   At this time, when the water flows in from the inlet 111, the inside of the bubble mixing part 300 becomes negative pressure due to the action of the water jetted from the plurality of holes 211, so that air is introduced from the air introduction path 310 into the internal flow path. It is burned.

図2に表したように、傾斜部320によって、内部流路全体へ均一に分散されるように導かれた水は、整流部400へ流れ込む。   As shown in FIG. 2, the water guided by the inclined portion 320 so as to be uniformly dispersed throughout the internal flow path flows into the rectifying unit 400.

整流部400は、傾斜部320の下流側に配置されており、整流格子を有している。   The rectifying unit 400 is disposed on the downstream side of the inclined unit 320 and has a rectifying grid.

整流格子は、環状の整流リブと、放射状の整流リブと、により区画化された複数の開口部410を有する部材である。この整流格子が流れの抵抗になり、上流側から流れ込んできた水は減速されるため、整流部400の上流面側には、見かけ上、水が溜まり、気液界面が形成される。   The rectifying grid is a member having a plurality of openings 410 divided by annular rectifying ribs and radial rectifying ribs. This rectifying grid serves as a flow resistance, and the water flowing from the upstream side is decelerated, so that the water is apparently accumulated on the upstream surface side of the rectifying unit 400 and a gas-liquid interface is formed.

傾斜部320によって、内部流路全体へ均一に分散されるように導かれ、整流部400へ流れ込んできた水は、気液界面に突入する。このとき、空気導入路310から内部流路内に導かれた空気が、粘性によって水中に気泡として引き込まれ、気泡混入水が生成される。   The water that has been guided by the inclined portion 320 so as to be uniformly dispersed throughout the internal flow path and has flowed into the rectifying portion 400 enters the gas-liquid interface. At this time, the air guided from the air introduction path 310 into the internal flow path is drawn into the water as bubbles due to viscosity, and bubble mixed water is generated.

気泡混入部300および整流部400の上流面側によって生成された気泡混入水は、整流部400の整流格子によって整流され、吐出口113から吐出される。   The bubble mixed water generated by the bubble mixing unit 300 and the upstream surface side of the rectifying unit 400 is rectified by the rectifying grid of the rectifying unit 400 and discharged from the discharge port 113.

次に、効率の良い気泡混入と効率の悪い気泡混入について、図面を参照しつつ説明する。
図3および図4は、オリフィス部200から内部流路に流入した水が、整流部400へ流れ込むときの様子を模式的に表している。図3は、効率の良い気泡混入が行える本実施形態の気泡混入水の流れを表す断面模式図である。また、図4は、効率の悪い気泡混入となってしまう比較例の気泡混入水の流れを表す断面模式図である。
Next, efficient bubble mixing and inefficient bubble mixing will be described with reference to the drawings.
3 and 4 schematically show a state in which water that has flowed into the internal flow path from the orifice unit 200 flows into the rectifying unit 400. FIG. 3 is a schematic cross-sectional view showing the flow of bubble-containing water according to this embodiment in which bubbles can be efficiently mixed. Moreover, FIG. 4 is a cross-sectional schematic diagram showing the flow of the bubble-containing water of the comparative example that results in inefficient bubble mixing.

本実施形態では、整流部400の上流面側全体に気液界面を形成することで、より効率的な空気混入を行うことができる。   In the present embodiment, more efficient air mixing can be performed by forming the gas-liquid interface on the entire upstream surface side of the rectifying unit 400.

図3に表したように、複数の孔211から下流の気泡混入部300へと噴射された水は、傾斜部320の上流側の面に衝突し、内部流路全体へ均一に分散されるように導かれることが望ましい。   As shown in FIG. 3, the water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 collides with the upstream surface of the inclined part 320 and is uniformly dispersed throughout the internal flow path. It is desirable to be guided to.

図3は、複数の孔211から下流の気泡混入部300へと噴射された水が、傾斜部320の上流側の面に衝突し、内部流路全体へ均一に分散されて整流部400へ流れ込んでいるため、整流部400の上流面側全体に気液界面が形成される。   FIG. 3 shows that water sprayed from the plurality of holes 211 to the downstream bubble mixing unit 300 collides with the upstream surface of the inclined unit 320, is uniformly dispersed throughout the internal flow path, and flows into the rectifying unit 400. Therefore, a gas-liquid interface is formed on the entire upstream surface side of the rectifying unit 400.

整流部400の上流面側全体に気液界面が形成されると、空気導入路310から内部流路内に導かれた空気は、水と共に吐出口113から吐出される以外に流路がないため、
空気が水に混入せずに、分離したまま流出するのを防ぐことができる。
そのため、空気導入路310から内部流路内に導かれた空気は確実に水中に気泡として引き込まれ、効率の良い気泡混入を行うことができる。
When the gas-liquid interface is formed on the entire upstream surface side of the rectifying unit 400, the air guided from the air introduction path 310 into the internal flow path has no flow path other than being discharged from the discharge port 113 together with water. ,
It is possible to prevent air from flowing out while being separated without being mixed into water.
Therefore, the air guided from the air introduction path 310 into the internal flow path is surely drawn into the water as bubbles, and efficient bubble mixing can be performed.

一方、図4に表したように、複数の孔211から下流の気泡混入部300へと噴射された水が、傾斜部320の上流側の面に衝突し、内部流路の内径側や外径側に偏ってしまうと効率の良い気泡混入は行えない。 On the other hand, as shown in FIG. 4, the water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 collides with the upstream surface of the inclined part 320, and the inner diameter side or outer diameter of the internal channel. If it is biased to the side, efficient bubble mixing cannot be performed.

図4(a)は、複数の孔211から下流の気泡混入部300へと噴射された水が、傾斜部320の上流側の面に衝突し、内部流路の内径側に偏って整流部400へ流れ込んでいるため、整流部400の上流面側の内径側にしか気液界面が形成されない。   FIG. 4A shows that the water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 collides with the upstream surface of the inclined part 320 and is biased toward the inner diameter side of the internal flow path 400. Therefore, the gas-liquid interface is formed only on the inner diameter side on the upstream surface side of the rectifying unit 400.

整流部400の上流面側の内径側にしか気液界面が形成されないと、空気導入路310から内部流路内に導かれた空気は、気液界面が形成されていない外径側が流路になるため、水に混入せずに、分離したまま流出してしまう。
そのため、空気導入路310から内部流路内に導かれた空気の一部しか水中に引き込むことができないため、気泡混入の効率は悪くなってしまう。
If the gas-liquid interface is formed only on the inner diameter side on the upstream surface side of the rectification unit 400, the air guided from the air introduction path 310 into the internal flow path is the outer diameter side where the gas-liquid interface is not formed in the flow path. Therefore, it flows out with separation without mixing in water.
For this reason, only part of the air guided from the air introduction path 310 into the internal flow path can be drawn into the water, so that the efficiency of mixing bubbles deteriorates.

また、図4(b)は、複数の孔211から下流の気泡混入部300へと噴射された水が、傾斜部320の上流側の面に衝突し、内部流路の外径側に偏って整流部400へ流れ込んでいるため、整流部400の上流面側の外径側にしか気液界面が形成されない。   FIG. 4B shows that water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 collides with the upstream surface of the inclined part 320 and is biased toward the outer diameter side of the internal channel. Since it flows into the rectifying unit 400, a gas-liquid interface is formed only on the outer diameter side on the upstream surface side of the rectifying unit 400.

整流部400の上流面側の外径側にしか気液界面が形成されないと、空気導入路310から内部流路内に導かれた空気は、気液界面が形成されていない上流面側の内径側が流路になるため、水に混入せずに、分離したまま流出してしまう。
そのため、空気導入路310から内部流路内に導かれた空気の一部しか水中に引き込むことができないため、気泡混入の効率は悪くなってしまう。
If the gas-liquid interface is formed only on the outer diameter side on the upstream surface side of the rectifying unit 400, the air guided from the air introduction path 310 into the internal flow path has the inner diameter on the upstream surface side where the gas-liquid interface is not formed. Since the side becomes a flow path, it flows out with separation without mixing in water.
For this reason, only part of the air guided from the air introduction path 310 into the internal flow path can be drawn into the water, so that the efficiency of mixing bubbles deteriorates.

次に、気泡混入水の縮流の発生と流速の高まりについて、図面を参照しつつ説明する。
図3および図4は、オリフィス部200から内部流路に流入した水が、整流部400へ流れ込むときの様子を模式的に表している。
図3は、気泡混入水の縮流の発生と流速の高まりを抑制できる本実施形態の気泡混入水の流れを表す断面模式図である。
また、図4は、気泡混入水の縮流の発生と流速の高まりが起こってしまう比較例の気泡混入水の流れを表す断面模式図である。
Next, generation | occurrence | production of the contraction flow of bubble mixing water and the raise of the flow velocity are demonstrated, referring drawings.
3 and 4 schematically show a state in which water that has flowed into the internal flow path from the orifice unit 200 flows into the rectifying unit 400.
FIG. 3 is a schematic cross-sectional view showing the flow of bubble-mixed water according to this embodiment that can suppress the occurrence of contracted flow of bubble-mixed water and the increase in flow velocity.
FIG. 4 is a schematic cross-sectional view showing the flow of bubble-containing water of a comparative example in which generation of contracted flow of bubble-containing water and increase in flow velocity occur.

図3に表したように、複数の孔211から下流の気泡混入部300へと噴射された水は、傾斜部320の上流側の面に衝突し、内部流路全体へ均一に分散されるように導かれることが望ましい。   As shown in FIG. 3, the water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 collides with the upstream surface of the inclined part 320 and is uniformly dispersed throughout the internal flow path. It is desirable to be guided to.

図3は、複数の孔211から下流の気泡混入部300へと噴射された水が、傾斜部320の上流側の面に衝突し、内部流路全体へ均一に分散されて整流部400へ流れ込んでいるため、整流部400の上流面側全体に気液界面が形成される。   FIG. 3 shows that water sprayed from the plurality of holes 211 to the downstream bubble mixing unit 300 collides with the upstream surface of the inclined unit 320, is uniformly dispersed throughout the internal flow path, and flows into the rectifying unit 400. Therefore, a gas-liquid interface is formed on the entire upstream surface side of the rectifying unit 400.

整流部400の上流面側全体に気液界面が形成されると、生成された気泡混入水は吐出口113全面から吐出されるため、吐水の縮流や流速の高まりが発生することがない。そのため、水跳ねや見た目の悪化等の問題を防ぐことが可能な吐水装置を提供することができる。   When the gas-liquid interface is formed on the entire upstream surface side of the rectifying unit 400, the generated bubble-mixed water is discharged from the entire surface of the discharge port 113, so that the condensate of the discharged water and the increase in the flow velocity do not occur. Therefore, it is possible to provide a water discharging device that can prevent problems such as water splashing and appearance deterioration.

一方、図4(a)に表したように、複数の孔211から下流の気泡混入部300へと噴射された水が、内部流路の内径側に偏ってしまうと吐水の縮流や流速の高まりを抑制することができない。   On the other hand, as shown in FIG. 4A, if the water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 is biased toward the inner diameter side of the internal flow path, The increase cannot be suppressed.

図4(a)は、複数の孔211から下流の気泡混入部300へと噴射された水が、傾斜部320の上流側の面に衝突し、内部流路の内径側に偏って整流部400へ流れ込んでいるため、整流部400の上流面側の内径側にしか気液界面が形成されない。   FIG. 4A shows that the water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 collides with the upstream surface of the inclined part 320 and is biased toward the inner diameter side of the internal flow path 400. Therefore, the gas-liquid interface is formed only on the inner diameter side on the upstream surface side of the rectifying unit 400.

整流部400の上流面側の内径側にしか気液界面が形成されないと、生成された気泡混入水は吐出口113全面から吐出されないため、吐出口全面から吐出される場合に比べ、効率の良い気泡混入水の生成が行えない。さらに、高流量段階では、吐水の縮流や流速の高まりが発生しやすくなってしまう。そのため、水跳ねや見た目の悪化等の問題が出てきてしまう。   If the gas-liquid interface is formed only on the inner diameter side on the upstream surface side of the rectifying unit 400, the generated bubble-mixed water is not discharged from the entire surface of the discharge port 113, and therefore more efficient than when discharged from the entire surface of the discharge port Generation of water containing bubbles cannot be performed. Furthermore, at the high flow rate stage, the constricted flow of the discharged water and the increase in the flow velocity tend to occur. For this reason, problems such as water splashing and deterioration of appearance appear.

また、図4(b)に表したように、複数の孔211から下流の気泡混入部300へと噴射された水が、内部流路の外径側に偏ってしまうと吐水の流速の高まりを抑制することができない。   In addition, as shown in FIG. 4B, if the water jetted from the plurality of holes 211 to the downstream bubble mixing part 300 is biased toward the outer diameter side of the internal flow path, the flow rate of the discharged water increases. It cannot be suppressed.

図4(b)は、複数の孔211から下流の気泡混入部300へと噴射された水が、傾斜部320の上流側の面に衝突し、内部流路の外径側に偏って整流部400へ流れ込んでいるため、整流部400の上流面側の外径側にしか気液界面が形成されない。   FIG. 4B shows that the water jetted from the plurality of holes 211 to the downstream bubble mixing unit 300 collides with the upstream surface of the inclined unit 320 and is biased toward the outer diameter side of the internal flow path. Since it flows into 400, the gas-liquid interface is formed only on the outer diameter side on the upstream surface side of the rectifying unit 400.

整流部400の上流面側の外径側にしか気液界面が形成されないと、生成された気泡混入水は吐出口113全面から吐出されないため、吐出口全面から吐出される場合に比べ、効率の良い気泡混入水の生成が行えない。さらに、高流量段階では、吐出口全面から吐出される場合に比べ、吐水の流速の高まりが発生しやすくなってしまう。そのため、水跳ねや見た目の悪化等の問題が出てきてしまう。   If the gas-liquid interface is formed only on the outer diameter side on the upstream surface side of the rectifying unit 400, the generated bubble-mixed water is not discharged from the entire surface of the discharge port 113. It is not possible to produce good water with bubbles. Furthermore, in the high flow rate stage, compared to the case where the discharge is made from the entire discharge port, the flow rate of the discharged water is likely to increase. For this reason, problems such as water splashing and deterioration of appearance appear.

本実施形態では、整流部のリブの設け方により、整流部400の上流面側全体に気液界面が形成されやすくし、図3に表したような、より効率的な空気混入が行えると共に、気泡混入水の縮流や流速の高まりの発生を抑制できるようにした。   In the present embodiment, by providing the rib of the rectifying unit, a gas-liquid interface is easily formed on the entire upstream surface side of the rectifying unit 400, and more efficient air mixing as illustrated in FIG. 3 can be performed. It was made possible to suppress the occurrence of contraction of bubble-containing water and increase in flow velocity.

図5は、本発明の泡沫吐水装置内における、水の流れの様子を説明するための断面模式図である。また、図6は、比較例の水の流れの様子を説明するための断面模式図である。また、図7および8は、本発明の泡沫吐水装置の整流部の断面図である。   FIG. 5 is a schematic cross-sectional view for explaining the state of water flow in the foam water spouting device of the present invention. FIG. 6 is a schematic cross-sectional view for explaining the flow of water in the comparative example. 7 and 8 are cross-sectional views of the rectifying unit of the foam water spouting device of the present invention.

本実施形態では、図5(a)に表したように、気泡混入部300が有する傾斜部320の斜面の延長線よりも内径側に、環状の整流リブ411が配設されている。これにより、環状の整流リブ411が、傾斜部320によって流路の中心方向に向かうように導かれた水の流れの抵抗となり、気泡混入水の流れを減速させることができる。そのため、整流部400の上流面側全体に気液界面が形成されやすくなる。したがって、高流量段階でも、吐出される気泡混入水の縮流を防ぐと共に、流速の高まりを抑制することができる。   In the present embodiment, as illustrated in FIG. 5A, the annular rectifying rib 411 is disposed on the inner diameter side of the extended line of the inclined surface of the inclined portion 320 included in the bubble mixing portion 300. Thereby, the annular rectifying rib 411 becomes a resistance of the flow of water guided toward the center of the flow path by the inclined portion 320, and the flow of the bubble-containing water can be decelerated. Therefore, a gas-liquid interface is easily formed on the entire upstream surface side of the rectifying unit 400. Therefore, even at a high flow rate stage, it is possible to prevent contraction of the discharged bubble-containing water and to suppress an increase in flow velocity.

また、流路の中心方向に向かうように導かれた水の流れを減速させることで、整流部400の上流面側全体に気液界面を形成しやすくすることができるため、より効率的な空気混入を行うことができる。   In addition, by reducing the flow of water guided toward the center of the flow path, it is possible to easily form a gas-liquid interface on the entire upstream surface side of the rectifying unit 400, and thus more efficient air Mixing can be performed.

さらに、傾斜部320の斜面の延長線よりも外径側には、環状の整流リブ411は配設されていない。そのため、環状の整流リブ411は、傾斜部320によって内部流路の中心方向に向かうように導かれた水の流れを、内部流路の外径側へ方向付けることができる。その結果、整流部400の上流面側全体に気液界面が形成されやすくなる。
したがって、高流量段階でも吐出される気泡混入水の縮流を防ぐと共に、流速の高まりを抑制することができる。
Further, the annular rectification rib 411 is not disposed on the outer diameter side of the extended line of the inclined surface of the inclined portion 320. Therefore, the annular rectifying rib 411 can direct the flow of water guided by the inclined portion 320 toward the center of the internal flow path toward the outer diameter side of the internal flow path. As a result, a gas-liquid interface is easily formed on the entire upstream surface side of the rectifying unit 400.
Accordingly, it is possible to prevent the bubble-mixed water that is discharged even in the high flow rate stage from contracting and to suppress an increase in the flow velocity.

環状の整流リブ411は、完全な環状でなく、断片的に配設されていてもよい。   The annular rectifying ribs 411 may not be completely annular but may be arranged in pieces.

また、図5(b)には、本発明に係る別の実施形態の一つであり、整流部400に向かって拡径している傾斜部320を有さない例を示している。   FIG. 5B shows another example of the embodiment according to the present invention, which does not include the inclined portion 320 whose diameter increases toward the rectifying portion 400.

一方、図6(a)、(b)に表したように、気泡混入部300が有する傾斜部320の斜面の延長線よりも外径側に、環状の整流リブ411が配設されていると、傾斜部320によって流路の中心方向に向かうように導かれた水の流れは、環状の整流リブ411が流れの抵抗とならないので、そのまま減速することなく吐水される。   On the other hand, as shown in FIGS. 6A and 6B, when the annular rectifying rib 411 is disposed on the outer diameter side of the extended line of the inclined surface of the inclined portion 320 included in the bubble mixing portion 300. The water flow guided toward the center of the flow path by the inclined portion 320 is discharged without being decelerated as it is because the annular flow regulating rib 411 does not serve as a flow resistance.

また、内部流路の外径側へ方向付けられることもないため、整流部400の上流面側全体に気液界面が形成されにくくなる。したがって、吐出される気泡混入水の縮流や流速の高まりが発生しやすくなってしまう。   Moreover, since it is not directed to the outer diameter side of the internal flow path, a gas-liquid interface is hardly formed on the entire upstream surface side of the rectifying unit 400. Therefore, it becomes easy to generate | occur | produce the contraction flow of the bubble mixed water discharged, and the increase in the flow velocity.

本実施形態では、整流部400において、開口部410が径方向に扁平状になるように、放射状の整流リブ413が配設されている。これにより、径方向における流れの速度分布の均一化をより促進させることができる。この作用により、吐出口113における水量の偏りが抑制されるため、気泡混入水が吐出口113の内径側に偏って吐出する現象を防ぐことができる。そのため、高流量段階でも吐出口113からの気泡混入水の縮流を防ぐと共に、流速の高まりを抑制することができる。   In the present embodiment, radial rectifying ribs 413 are arranged in the rectifying unit 400 so that the opening 410 is flat in the radial direction. Thereby, the uniformization of the flow velocity distribution in the radial direction can be further promoted. Due to this action, the deviation of the amount of water at the discharge port 113 is suppressed, so that it is possible to prevent a phenomenon in which air bubbles mixed in are discharged toward the inner diameter side of the discharge port 113. Therefore, it is possible to prevent the bubbling water from contracting from the discharge port 113 even at a high flow rate stage and to suppress an increase in the flow velocity.

また、径方向における流れの速度分布の均一化をより促進させることで、整流部400の上流面側全体に気液界面を形成することができるため、より効率的な空気混入を行うことができる。   Further, by further promoting the uniformity of the flow velocity distribution in the radial direction, a gas-liquid interface can be formed on the entire upstream surface side of the rectifying unit 400, so that more efficient air mixing can be performed. .

さらに、放射状の整流リブ413は、径方向における流れの速度分布の均一化をより促進させることができるため、吐水の揺れを抑制することができる。   Furthermore, since the radial flow straightening ribs 413 can further promote the uniform flow velocity distribution in the radial direction, it is possible to suppress the shaking of the water discharge.

本実施形態では、図7に表したように、整流部400において、整流格子で区画化された開口部410は、整流部400の環状の整流リブ411のうち、最も外径側の整流リブの径内方向よりも径外方向の開口比率が大きくなるように、環状の整流リブ411および放射状の整流リブ413が配設されている。これにより、整流部400内径側への集中しがちな水の流入を抑制し、外径側への水の流入を促進されるため、高流量段階でも吐出口113からの気泡混入水の縮流を防ぐことができる。   In the present embodiment, as shown in FIG. 7, in the rectifying unit 400, the opening 410 partitioned by the rectifying grid is the outermost rectifying rib of the annular rectifying ribs 411 of the rectifying unit 400. An annular straightening rib 411 and a radial straightening rib 413 are arranged so that the opening ratio in the radial direction is larger than the radial direction. As a result, the inflow of water that tends to concentrate on the inner diameter side of the rectifying unit 400 is suppressed and the inflow of water to the outer diameter side is promoted. Can be prevented.

また、整流部400内径側への集中しがちな水の流入を抑制し、外径側への水の流入を促進することで、整流部400の上流面側全体に気液界面を形成することができるため、より効率的な空気混入を行うことができる。   In addition, by suppressing the inflow of water that tends to concentrate to the inner diameter side of the rectifying unit 400 and promoting the inflow of water to the outer diameter side, a gas-liquid interface is formed on the entire upstream surface side of the rectifying unit 400. Therefore, more efficient aeration can be performed.

さらに、整流部400内径側への集中しがちな水の流入を抑制し、外径側への水の流入を促進することで、径方向における流れの速度分布の均一化作用をもたらすので、吐水の揺れを抑制することができる。   Furthermore, since the inflow of water that tends to concentrate to the inner diameter side of the rectifying unit 400 is suppressed and the inflow of water to the outer diameter side is promoted, the flow velocity distribution in the radial direction can be made uniform. Can be suppressed.

図8に表したように、環状の整流リブ411のうち、最も外径側の整流リブの径内方向の開口比率が、径外方向の開口比率よりも大きくなるように、整流格子は、複数の環状の整流リブ411を備えたものであってもよい。   As shown in FIG. 8, a plurality of rectifying grids are provided so that the opening ratio in the radially inner direction of the rectifying rib on the outermost diameter side of the annular rectifying rib 411 is larger than the opening ratio in the radially outer direction. The annular rectifying rib 411 may be provided.

これまで、本発明の実施の形態について説明してきた。本発明はこれらの形態に限定されるものではなく、当業者が適宜設計変更を加えたものも、本発明の特徴を備えている限り、本発明の範囲に包含される。例えば、前述した各具体例が備える各要素およびその配置、材料、条件、形状、サイズなどは、例示したものに限定されず、適宜変更することが可能である。また、前述した実施の形態が備える各要素は、技術的に可能な限りにおいて組み合わせることができるため、これらを組み合わせたものも本発明の特徴を含む限り本発明の範囲に包含される。   The embodiments of the present invention have been described so far. The present invention is not limited to these embodiments, and those appropriately modified by those skilled in the art are also included in the scope of the present invention as long as they have the features of the present invention. For example, each element included in each of the specific examples described above and their arrangement, material, condition, shape, size, and the like are not limited to those illustrated, and can be changed as appropriate. In addition, since the elements included in the above-described embodiments can be combined as much as technically possible, combinations of these elements are also included in the scope of the present invention as long as they include the features of the present invention.

100…泡沫吐水装置
110…本体部
111…流入口
113…吐出口
150…上絞径部
151…環状凸部
153…鍔部
155…流入穴
200…オリフィス部
210…減圧板
211…複数の孔
300…気泡混入部
310…空気導入路
311…空気孔
320…傾斜部
400…整流部
410…開口部
411…環状の整流リブ
413…放射状の整流リブ
DESCRIPTION OF SYMBOLS 100 ... Foam spouting device 110 ... Main-body part 111 ... Inflow port 113 ... Ejection port 150 ... Upper diameter-reducing part 151 ... Annular convex part 153 ... Eaves part 155 ... Inflow hole 200 ... Orifice part 210 ... Pressure-reducing plate 211 ... Multiple holes 300 ... Bubble mixing part 310 ... Air introduction path 311 ... Air hole 320 ... Inclined part 400 ... Rectifying part 410 ... Opening part 411 ... Annular rectifying rib 413 ... Radial rectifying rib

Claims (3)

流入口から流入した水を気泡混入水として吐出口から吐出することができる泡沫吐水装置であって、
前記流入口から前記吐出口に至るまでの内部流路が形成された本体部と、
前記流入口から流入した水を前記内部流路の下流側に向けて流速を大きくして噴射するオリフィス部と、
前記内部流路内に空気を導入する空気孔が形成され、前記空気孔から導入された空気を前記オリフィス部から噴射された水に混入して前記気泡混入水とする気泡混入部と、
前記気泡混入部の下流に配設され、前記吐出口から前記気泡混入水を整流させて吐出する整流部と、
を備え、
前記オリフィス部は、前記内部流路を遮るように設けられ、複数の孔が形成された減圧板を有し、
前記気泡混入部は、前記複数の孔から噴射された水が、前記内部流路の中心方向に向かうように、下流側に向けて漏斗状に縮径した傾斜部を有し、
前記整流部は、前記気泡混入部で生成した気泡混入水を整流するための整流格子を有し、前記整流格子は、環状の整流リブと、放射状の整流リブと、を有し、前記環状の整流リブのうち、最も外径側に配設される環状の整流リブは、前記傾斜部の斜面の延長線よりも内径側に配設されたことを特徴とする泡沫吐水装置。
A foam water spouting device capable of discharging water flowing in from an inflow port as air bubble mixed water from a discharge port,
A main body portion in which an internal flow path from the inflow port to the discharge port is formed;
An orifice for injecting water flowing in from the inflow port toward the downstream side of the internal flow path at a higher flow velocity;
An air hole that introduces air into the internal flow path is formed, and a bubble mixing part that mixes the air introduced from the air hole into water jetted from the orifice part to form the bubble mixed water;
A rectifying unit that is disposed downstream of the bubble mixing unit and rectifies and discharges the bubble mixed water from the discharge port;
With
The orifice part is provided so as to block the internal flow path, and has a decompression plate formed with a plurality of holes,
The bubble mixing part has an inclined part whose diameter is reduced in a funnel shape toward the downstream side so that water sprayed from the plurality of holes is directed toward the center of the internal flow path.
The rectifying unit includes a rectifying grid for rectifying the bubble mixed water generated in the bubble mixing unit, and the rectifying grid includes an annular rectifying rib and a radial rectifying rib. The foam fountain apparatus according to claim 1, wherein an annular rectifying rib disposed on the outermost diameter side among the rectifying ribs is disposed on an inner diameter side with respect to an extended line of the inclined surface of the inclined portion.
前記整流格子は、前記環状の整流リブと、前記放射状の整流リブと、により区画化された複数の開口部を有し、前記最も外径側に配設される環状の整流リブよりも径外方向に配設される前記複数の開口部は、径方向に扁平状に形成されたことを特徴とする請求項1記載の泡沫吐水装置。
The rectifying grid has a plurality of openings partitioned by the annular rectifying ribs and the radial rectifying ribs, and has a diameter outside the annular rectifying rib disposed on the outermost diameter side. The foam water spouting device according to claim 1, wherein the plurality of openings disposed in the direction are formed in a flat shape in the radial direction.
前記最も外径側に配設される環状の整流リブより径外方向の開口比率は、径内方向の開口比率より大きくしたことを特徴とする請求項1記載の泡沫吐水装置。   The foam spouting device according to claim 1, wherein an opening ratio in the radially outward direction is larger than an opening ratio in the radially inward direction than the annular rectifying rib disposed on the outermost diameter side.
JP2010217993A 2010-09-29 2010-09-29 Foam spouting device Active JP5854365B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2010217993A JP5854365B2 (en) 2010-09-29 2010-09-29 Foam spouting device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2010217993A JP5854365B2 (en) 2010-09-29 2010-09-29 Foam spouting device

Publications (2)

Publication Number Publication Date
JP2012072594A true JP2012072594A (en) 2012-04-12
JP5854365B2 JP5854365B2 (en) 2016-02-09

Family

ID=46169042

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2010217993A Active JP5854365B2 (en) 2010-09-29 2010-09-29 Foam spouting device

Country Status (1)

Country Link
JP (1) JP5854365B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103306335A (en) * 2013-06-05 2013-09-18 邝锦汉 Plastic water discharging bent pipe of water faucet
CN104099977A (en) * 2013-04-15 2014-10-15 Toto株式会社 Water Spraying Device
JP2016097341A (en) * 2014-11-20 2016-05-30 Toto株式会社 Water discharge device
JP6044816B1 (en) * 2015-08-19 2016-12-14 株式会社 Toshin Foam water discharge device and foam water discharge unit
CN107075844A (en) * 2015-03-26 2017-08-18 Toto株式会社 Water discharge device
JP2017214763A (en) * 2016-05-31 2017-12-07 Toto株式会社 shower head
JP2019094756A (en) * 2017-11-24 2019-06-20 高木 茂 Water discharge device
JP6905290B1 (en) * 2020-12-15 2021-07-21 株式会社 Toshin shower head

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001068995A1 (en) * 2000-03-17 2001-09-20 Toto Ltd. Foam water delivery port
JP2001279746A (en) * 2000-03-29 2001-10-10 Toto Ltd Automatic faucet
JP2002070098A (en) * 2000-09-01 2002-03-08 Toto Ltd Bubble flow discharging apparatus
JP2002275969A (en) * 2001-03-21 2002-09-25 Toto Ltd Foamed water discharging device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001068995A1 (en) * 2000-03-17 2001-09-20 Toto Ltd. Foam water delivery port
JP2001279746A (en) * 2000-03-29 2001-10-10 Toto Ltd Automatic faucet
JP2002070098A (en) * 2000-09-01 2002-03-08 Toto Ltd Bubble flow discharging apparatus
JP2002275969A (en) * 2001-03-21 2002-09-25 Toto Ltd Foamed water discharging device

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104099977A (en) * 2013-04-15 2014-10-15 Toto株式会社 Water Spraying Device
CN103306335A (en) * 2013-06-05 2013-09-18 邝锦汉 Plastic water discharging bent pipe of water faucet
JP2016097341A (en) * 2014-11-20 2016-05-30 Toto株式会社 Water discharge device
CN107075844A (en) * 2015-03-26 2017-08-18 Toto株式会社 Water discharge device
CN107075844B (en) * 2015-03-26 2019-05-17 Toto株式会社 Water discharge device
JP6044816B1 (en) * 2015-08-19 2016-12-14 株式会社 Toshin Foam water discharge device and foam water discharge unit
WO2017029835A1 (en) * 2015-08-19 2017-02-23 株式会社Toshin Foamy water discharging device and foamy water discharging unit
US10654053B2 (en) 2015-08-19 2020-05-19 Toshin Inc. Foamed water discharging device and foamed water discharging unit
JP2017214763A (en) * 2016-05-31 2017-12-07 Toto株式会社 shower head
JP2019094756A (en) * 2017-11-24 2019-06-20 高木 茂 Water discharge device
JP6905290B1 (en) * 2020-12-15 2021-07-21 株式会社 Toshin shower head
JP2022094418A (en) * 2020-12-15 2022-06-27 株式会社 Toshin shower head

Also Published As

Publication number Publication date
JP5854365B2 (en) 2016-02-09

Similar Documents

Publication Publication Date Title
JP5854365B2 (en) Foam spouting device
CN108571037B (en) Sanitary insert unit
US11248368B2 (en) Faucet aerator with center stream
US9328491B2 (en) Water spouting device
JP2012082591A (en) Shower head
JP5802959B2 (en) Flush toilet
JP6044816B1 (en) Foam water discharge device and foam water discharge unit
JP5573879B2 (en) Microbubble generator
CN108543430B (en) Water outlet device
JP2010188046A (en) Shower device
JP5800276B2 (en) Water discharge device
JP3837744B1 (en) shower head
JP6727538B2 (en) Water discharge device
JP5660281B2 (en) Water discharge device
JP6315248B2 (en) Water discharge device
JP2010142336A (en) Shower device
JP5800278B2 (en) Water discharge device
WO2009130812A1 (en) Water saving device
CN207740545U (en) A kind of Anti-blockage water-saving sparger
JP6394314B2 (en) Water discharge device
JP2011214301A (en) Water discharge device
JPH03161063A (en) Foam discharging opening
JP6315247B2 (en) Water discharge device
JP5532312B2 (en) Water discharge device
WO2019119644A1 (en) Water saving and noise reduction device and water outlet device

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20130725

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20140307

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20140421

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20140526

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20141125

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20150122

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150609

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20150710

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20151116

R150 Certificate of patent or registration of utility model

Ref document number: 5854365

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20151129