JPH03161063A - Foam discharging opening - Google Patents

Foam discharging opening

Info

Publication number
JPH03161063A
JPH03161063A JP1304491A JP30449189A JPH03161063A JP H03161063 A JPH03161063 A JP H03161063A JP 1304491 A JP1304491 A JP 1304491A JP 30449189 A JP30449189 A JP 30449189A JP H03161063 A JPH03161063 A JP H03161063A
Authority
JP
Japan
Prior art keywords
water
chamber
flow
air
foaming
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
JP1304491A
Other languages
Japanese (ja)
Other versions
JPH0745017B2 (en
Inventor
Masahiko Imazono
今園 雅彦
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 JP1304491A priority Critical patent/JPH0745017B2/en
Priority to US07/614,905 priority patent/US5143295A/en
Priority to KR1019900018592A priority patent/KR970002860B1/en
Priority to CA002030677A priority patent/CA2030677A1/en
Priority to DE69028832T priority patent/DE69028832T2/en
Priority to AT90122199T priority patent/ATE144015T1/en
Priority to EP90122199A priority patent/EP0429068B1/en
Publication of JPH03161063A publication Critical patent/JPH03161063A/en
Publication of JPH0745017B2 publication Critical patent/JPH0745017B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To eliminate pressure loss and clogging of foreign matter by a method wherein a foaming chamber and an air passage in communication with a whirling stream chamber are provided and the foaming chamber is provided with a reverse flow prevention mechanism. CONSTITUTION:When water is supplied from a spout 50, the water runs into a downstream side chamber 8 from its outer periphery along the inner wall thereof and joins the water from a hole 6a and a stream thus formed starts a rotating movement therein while creating a swirl. In the downstream side chamber 8, the fluid energy of the water itself increases and a centrifugal action takes place due to a whirling stream to form the dropping water into a cone- shaped water screen F for discharging. Since a discharge opening 3a is located in the center of a foaming chamber 5 and since the water runs out at a high speed accompanied by centrifugal force, an inner spatial pressure inside the cone-shaped water screen F is decreased, whereby air is sucked in from an air stream 22a to produce foam. The foamed water runs into a water diffusing hole 21 and its stream is straightened by a current plate 23 for discharging.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、水栓のスパウトやシャワーヘッド等の先端に
取り付けられて給水を泡沫化するための泡沫吐水口に関
する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a foam spout that is attached to the tip of a faucet spout, shower head, etc., and is used to foam supplied water.

〔従来の技術〕[Conventional technology]

給水音やシンク等への落下音を小さくしたり水撥ねをな
くすために泡沫吐水口を設けた水栓が従来から利用され
ている。最も一般的に用いられているものとして、たと
えば特公昭63−31621号公報に記載されたものが
ある。
BACKGROUND ART Faucets equipped with a foam spout have been used in the past in order to reduce the sound of water being supplied, the sound of water falling into a sink, etc., and to eliminate water splashing. The most commonly used one is, for example, the one described in Japanese Patent Publication No. 31621/1983.

第9図はこの公報に記載のもの及びその他の一般的な泡
沫吐水口の概略を示す断面図である。図において、水栓
のスパウト50の先端に固定された吐水キャップ51の
中に多数の小孔52aを開けた減圧板52が収納されて
いる。そして、この減圧板52よりも下流の吐水キャッ
プ5lの周壁に外の空気を給水中に取り入れる空気孔5
3を開け、更に出口には流れを整流化するための複数の
整流wI54が配置されている。
FIG. 9 is a cross-sectional view schematically showing the one described in this publication and other general foam spouts. In the figure, a pressure reducing plate 52 having a large number of small holes 52a is housed in a water discharge cap 51 fixed to the tip of a spout 50 of a water faucet. There is an air hole 5 in the peripheral wall of the water discharge cap 5l downstream of the pressure reducing plate 52 to introduce outside air into the water supply.
3 is opened, and a plurality of rectifiers wI54 are arranged at the outlet for rectifying the flow.

このような泡沫吐水口では、スバウト50からの給水が
減圧板52の小孔52aを通過するときに流れが増達さ
れる。このため、減圧板52の下流側の吐水キャップ5
1の中が減圧されて空気口53から外部の空気が吸い込
まれ、この空気が給水の中に混入することによって流れ
が泡沫化される。また、整流網54の網目が細かいため
、給水がこれに衝き当たって流れ去るときにも給水が激
しく撹拌されるため、更に泡沫化が促進される。
In such a foam spout, when the water supplied from the spout 50 passes through the small holes 52a of the pressure reducing plate 52, the flow is increased. For this reason, the water discharge cap 5 on the downstream side of the pressure reducing plate 52
1 is reduced in pressure, outside air is sucked in through the air port 53, and this air mixes into the water supply, thereby turning the flow into foam. Furthermore, since the mesh of the straightening net 54 is fine, the supplied water is vigorously agitated even when it collides with the straightening net 54 and flows away, so that foaming is further promoted.

また、このような構造に代えて、吐出端に設ける散水板
に減圧板の小孔からの流速の速い流れを衝突させ、混入
した空気と共に更に撹拌することによって泡沫化を促進
するものもある。
In addition, instead of such a structure, there is also a structure in which a high-velocity flow from small holes in a pressure reducing plate impinges on a water sprinkling plate provided at the discharge end, and further agitates together with the mixed air to promote foaming.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

ところが、スパウト50からの給水は減圧板52の小孔
52aを通過するため、流れの圧力損失がかなり大きい
。このため、水栓の弁開度を或る一定以上に設定しない
と適切な吐水圧が得られない、また、流量を小さくした
場合には、泡沫にならなかったり泡沫感のない吐水とな
ってしまう。
However, since the water supplied from the spout 50 passes through the small holes 52a of the pressure reducing plate 52, the pressure loss of the flow is quite large. For this reason, appropriate water discharge pressure cannot be obtained unless the valve opening of the faucet is set above a certain level, and if the flow rate is reduced, the water does not foam or have a foamy feel. Put it away.

更に、減圧板52及び整流i54を2段に備えているの
で、給水中の異物が詰まったリスケールが付着しやすい
。このため、流路面積が小さくなって吐水量不足を生じ
たり、特に減圧板52の小孔52aが閉じてしまうと適
切な泡沫化もできなくなる。
Furthermore, since the pressure reducing plate 52 and the rectifier i54 are provided in two stages, rescale clogged with foreign matter in the water supply is likely to adhere. For this reason, the flow path area becomes small, resulting in an insufficient amount of water to be discharged, and in particular, if the small holes 52a of the pressure reducing plate 52 are closed, appropriate foaming cannot be achieved.

このように、従来の泡沫吐水口では、減圧板を利用した
給水の増速及びこれに基づく内部流路の減圧による外気
の吸引を利用しているので、給水の圧力損失が大きくて
流路の閉塞等の障害があるほか、低流量では適切に使え
ない等の問題があった。
In this way, the conventional foam spout uses a pressure reducing plate to increase the speed of the water supply and to reduce the pressure in the internal flow path to suck in outside air, so the pressure loss of the water supply is large and the flow path In addition to problems such as blockage, there were other problems such as the inability to use the system properly at low flow rates.

そこで、本発明は、圧力損失や異物の詰まり等を生じる
ことなく流量を確保し且つ常に適切な泡沫化が得られる
ようにすることを目的とする。
Therefore, an object of the present invention is to ensure a flow rate without causing pressure loss or clogging with foreign matter, and to always obtain appropriate foaming.

〔課題を解決するための手段〕[Means to solve the problem]

本発明の泡沫吐水口は、以上の目的を達戊するために、
給水源に連通して流れを旋回させる旋回流チャンパと、
前記旋回流チャンバのほぼ中央に開けた放出口によって
該旋回流チャンバに連通ずる泡沫化チャンバと、前記放
出口からの水流入時の減圧降下によって前記泡沫化チャ
ンバに空気を吸引する空気流路とを備え、前記泡沫化チ
ャンバは、空気吸入部及び空気と給水の混合部とを区画
する逆流防止機構を備えていることを特徴とする。
In order to achieve the above objectives, the foam spout of the present invention has the following features:
a swirling flow chamber that communicates with a water supply source and swirls the flow;
a foaming chamber that communicates with the swirling flow chamber through a discharge port opened approximately in the center of the swirling flow chamber; and an air flow path that sucks air into the foaming chamber by a reduced pressure drop when water flows in from the discharge port. The foaming chamber is characterized in that it is equipped with a backflow prevention mechanism that partitions an air intake section and an air and water supply mixing section.

また、泡沫化チャンパの内壁を微小な凹凸面とすれば、
旋回流チャンバでの強制的な旋回化による脈流等を干渉
させることができ、安定流れに変えることができる。
In addition, if the inner wall of the foaming champer is made into a minutely uneven surface,
Pulsating flow caused by forced swirling in the swirling flow chamber can be interfered with, and can be changed to a stable flow.

〔作用〕[Effect]

旋回流チャンバに流入した水は、渦巻き状の旋回流とな
り、流れ自体には外側への遠心力が作用する。そして、
旋回流チャンバのほぼ中央に開けた放出口部分での流れ
も渦巻き状となっているため、放出口から流れ出る水は
遠心力によって外側へ吹き飛ばされ、放出口から円錐の
水腹状となって泡沫化チャンバに送り込まれる。これに
より、泡沫化チャンバに流れ込む水は既に飛散しやすい
状態となり、泡沫化チャンパを空気孔等によって大気開
放しておけば放出口から高速での流入する水による減圧
効果によって、空気が吸引される。
The water flowing into the swirling flow chamber becomes a swirling swirling flow, and an outward centrifugal force acts on the flow itself. and,
The flow at the outlet opening in the center of the swirling flow chamber also has a spiral shape, so the water flowing out from the outlet is blown outward by centrifugal force, forming a conical water belly from the outlet and forming foam. into the chemical chamber. As a result, the water flowing into the foaming chamber is already in a state where it is easy to scatter, and if the foaming chamber is opened to the atmosphere through air holes, air will be sucked in by the depressurizing effect of the water flowing in at high speed from the discharge port. .

そして、この吸引された空気は流れ込んでいろ水膜状の
給水中に速やかに混入され、泡沫吐水となって排出され
る。
Then, this sucked air flows in and is quickly mixed into the water film-like water supply, and is discharged as foamy water.

このように、多数の小孔を開けた減圧板を用いることな
く、給水を旋回させて飛散しやすい状態とした後に空気
を混入させることで泡沫吐水が得られ、圧力損失を低減
した泡沫化が可能となる。
In this way, without using a pressure reducing plate with many small holes, by swirling the supplied water to make it more likely to scatter, and then mixing in air, foamy water can be obtained, resulting in foaming with reduced pressure loss. It becomes possible.

〔実施例〕〔Example〕

以下、図面に示す実施例により本発明の特徴を具体的に
説明する。
Hereinafter, features of the present invention will be specifically explained with reference to embodiments shown in the drawings.

第1図は本発明の一実施例を示す吐水口の要部縦断面図
、第2図は第1図の1−1線矢視断面図である。
FIG. 1 is a longitudinal cross-sectional view of a main part of a spout showing an embodiment of the present invention, and FIG. 2 is a cross-sectional view taken along the line 1-1 in FIG.

図において、スパウ}50の先端に泡沫化のための吐水
ヘッド1が取り付けられている。吐水ヘッド1は円形の
横断面を持ち、スパウト50からほぼ水平方向に向かう
流線は吐水ヘッドlの中心から下に直角に曲がり、下端
に設けた散水板2から吐出される内部流路が形戊されて
いる。
In the figure, a water discharging head 1 for foaming is attached to the tip of a spout 50. The water spouting head 1 has a circular cross section, and a streamline extending from the spout 50 in a substantially horizontal direction curves downward from the center of the water spouting head 1 at a right angle, forming an internal flow path through which water is discharged from the water sprinkling plate 2 provided at the lower end. It has been pierced.

吐水ヘッド1の内部は隔壁3によって上下に分割され、
この隔壁3の上方を旋回流チャンバ4及び下方を泡沫化
チャンバ5としている。旋回流チャンバ4は、隔壁3と
吐水ヘッド1の上端内壁との間を繋ぐ環状壁6によって
上流側室7及び下流側室8に区画されている。上流側室
7は環状の流路を持ち、下流側室8は隔壁3に開けた放
出口3aにより泡沫化チャンバ5に連通している。なお
、隔壁3及び環状壁6は一体戒形品としておき、これを
吐水ヘッドlの中に固定する組立て構造とする。
The inside of the water discharging head 1 is divided into upper and lower parts by a partition wall 3,
The upper part of this partition wall 3 is a swirling flow chamber 4, and the lower part is a foaming chamber 5. The swirling flow chamber 4 is divided into an upstream chamber 7 and a downstream chamber 8 by an annular wall 6 that connects the partition wall 3 and the upper inner wall of the water discharge head 1 . The upstream chamber 7 has an annular flow path, and the downstream chamber 8 communicates with the foaming chamber 5 through a discharge port 3a formed in the partition wall 3. In addition, the partition wall 3 and the annular wall 6 are made into an integral part, and the assembly structure is such that this is fixed in the water spouting head l.

環状壁6は吐水ヘッド1の流路断面と同軸配置され、第
2図に示すように4箇所に孔6aを開けている。これら
の孔6aは、環状壁6の内部の下流側室8の横断面に対
して流線がタンジェンシャル方向となるような姿勢とし
ている。一方、下流側室8の底部に開放している放出口
3aは下流側室8の中心に位置し、その内径は下流側室
8の内径よりも格段に小さい。
The annular wall 6 is arranged coaxially with the cross section of the flow path of the water discharging head 1, and has holes 6a at four locations as shown in FIG. These holes 6a are oriented such that streamlines are tangential to the cross section of the downstream chamber 8 inside the annular wall 6. On the other hand, the discharge port 3a open to the bottom of the downstream chamber 8 is located at the center of the downstream chamber 8, and its inner diameter is much smaller than the inner diameter of the downstream chamber 8.

散水板2は泡沫水を整流して吐出させると共に泡沫化の
ための空気吸引構造を備えたもので、第3図(a)にそ
の全体斜視図を示す。
The water sprinkling plate 2 rectifies and discharges foamy water and is equipped with an air suction structure for foaming the water. FIG. 3(a) shows an overall perspective view of the water spraying plate 2.

散水板2の一端には吐水ヘッド1の吐出端にネジ接合等
によって一体化されるベース20を備え、このベース2
0に合計6個の散水孔2lが設けられている(第4図参
照)。そして、ベース20の中心から上に向けて空気吸
入筒22を同軸上に形威し、その内部に空気流路22a
を設けている。
One end of the water sprinkling plate 2 is provided with a base 20 that is integrated with the discharge end of the water spouting head 1 by screwing or the like.
A total of six water sprinkling holes 2L are provided in the 0 (see FIG. 4). Then, an air suction tube 22 is formed coaxially upward from the center of the base 20, and an air flow path 22a is formed inside the tube.
has been established.

ベース20は第1図に示すように散水孔21の軸線長さ
を或る程度大きくして、通過してゆく泡沫水を整流化で
きるようにしておく。そして、各散水孔21の内部には
十字状の整流板23が組み込まれ、これによって散水孔
21を流れる泡沫水の流れの乱れを無くすようにしてい
る。また、ベース20の上面には、図示のように空気吸
入筒22から放射状に伸びる6枚の整流羽根24を設け
る。これらの整流羽根24は、隣接する散水孔21の間
をぬってベース20の縁部に至り、その高さは敗水孔2
1の軸線長さの半分程度である。更に、ベース20の上
面にはペース20と同軸であって散水孔21の中心を通
る円形の環状整流板25が設けられる。この環状整流板
25は、第1図のように散水孔21に設けた十字状の整
流板23の交点の上を通過し、その高さは整流羽根24
のほぼ2倍程度である。
As shown in FIG. 1, the base 20 is designed so that the axial length of the water sprinkling holes 21 is increased to a certain extent so that the foamy water passing therethrough can be rectified. A cross-shaped rectifying plate 23 is installed inside each water sprinkling hole 21, thereby eliminating disturbances in the flow of foamy water flowing through the water sprinkling hole 21. Further, on the upper surface of the base 20, six rectifying blades 24 are provided which extend radially from the air suction tube 22 as shown in the figure. These rectifying blades 24 pass between adjacent water holes 21 to reach the edge of the base 20, and their height is higher than that of the water spray holes 21.
It is about half of the axis length of 1. Furthermore, a circular annular current plate 25 is provided on the upper surface of the base 20, which is coaxial with the pace 20 and passes through the center of the water sprinkling hole 21. This annular current plate 25 passes over the intersection of the cross-shaped current plate 23 provided in the water spray hole 21 as shown in FIG.
This is approximately twice as large as the previous year.

空気吸入簡22は、ペース20の上面から径を小さくし
た円錐台状に形或され、その外周の円錐面22bを泡沫
水のガイドとして利用する。また、円錐面22bの上端
部からは等径の筒状に形戊され、その上端を旋回流チャ
ンバ4の放出口3aに臨ませている。そして、空気吸入
筒22の上半分より高い位置には逆流防止板26が設け
られる。この逆流防止板26は円板状であって水平姿勢
に取り付けられ、その外径は環状整流板25よりも小さ
いか同じ程度の径を持つ。更に、第1図に示すように、
隔壁3の下面には泡沫化チャンバ5と同軸上に設けた環
状体の逆流防止板27が一体化されている。この逆流防
止板27の内径は下の逆流防止板26よりも大きいか同
じ程度であり環状整流板25にほぼ等しい。
The air suction tube 22 is shaped like a truncated cone with a diameter reduced from the upper surface of the pace 20, and uses a conical surface 22b on its outer periphery as a guide for foamy water. Further, the upper end of the conical surface 22b is formed into a cylindrical shape having an equal diameter, and the upper end thereof faces the discharge port 3a of the swirling flow chamber 4. A backflow prevention plate 26 is provided at a position higher than the upper half of the air intake cylinder 22. This backflow prevention plate 26 has a disk shape and is attached in a horizontal position, and has an outer diameter smaller than or about the same as that of the annular rectifier plate 25. Furthermore, as shown in Figure 1,
A backflow prevention plate 27 in the form of an annular body provided coaxially with the foaming chamber 5 is integrated with the lower surface of the partition wall 3 . The inner diameter of this backflow prevention plate 27 is larger than or about the same as that of the lower backflow prevention plate 26, and is approximately equal to that of the annular rectifying plate 25.

なお、環状の逆流防止板27は、隔壁3に一体に備える
のに代えて、第3図(ロ)のように散水板2側に設ける
ようにしてもよい。この場合、逆流防止板27は空気吸
入筒22の上端に4本のステ−27aによって一体化さ
れ、水及び空気の流れに障害を与えない構造とする。ま
た、ペース20の上面に設ける環状整流板25は、第5
図に示すように各敗水孔2lの間に頂角を持つ六角形状
としてもよい。
Note that instead of being provided integrally with the partition wall 3, the annular backflow prevention plate 27 may be provided on the water spray plate 2 side as shown in FIG. 3(b). In this case, the backflow prevention plate 27 is integrated with the upper end of the air suction cylinder 22 by four stays 27a, and has a structure that does not impede the flow of water and air. Further, the annular current plate 25 provided on the upper surface of the pace 20 has a fifth
As shown in the figure, it may have a hexagonal shape with an apex angle between each drainage hole 2l.

更に、泡沫化チャンバ5の内周壁には雌ネジ5aが干渉
面として形戊されている。この雌ネジ5aは放出口3a
から水腹状となって流れ込む給水が当たったときに、給
水に脈動があるような場合にこれに干渉して脈動を減衰
させる機能を持つ。なお、干渉面として雌ネジ5aを刻
んだのは、加工が簡単であることが一つの理由であり、
これに代えて泡沫化チャンバ5の内周壁に微小な凹凸を
持たせるようにしてもよい。
Furthermore, a female thread 5a is formed on the inner circumferential wall of the foaming chamber 5 as an interference surface. This female screw 5a is the discharge port 3a.
If there is pulsation in the water supply when it hits the water supply flowing in a water belly shape, it has the function of interfering with this and damping the pulsation. One of the reasons why the female thread 5a was carved as an interference surface is that it is easy to process.
Alternatively, the inner circumferential wall of the foaming chamber 5 may have minute irregularities.

ここで、スパウト50から水を送り込むと、上流側室7
から環状壁6の孔6aを通って下流側室8に水が流れ込
む。このとき、孔6aの軸線は円形断面の下流側室8に
対してタンジェンシャル方向を向いているので、下流側
室8内では水が旋回流となる。すなわち、第2図に示す
ように、水は下流側室8の外周部から内壁に沿って流れ
込み、4箇所の孔6aからの水が合流して渦を形威しな
がら下流側室8の中で旋回し始める。このとき、孔6a
の全体の流路面積が放出口3aのそれより大きければ、
下流側室s内で水が滞留する現象を生じ、内圧も幾分か
上昇する。したがって、下流側室8の内部では水自体の
流動エネルギが増加し、旋回流による遠心力が作用する
。このため、放出口3aから下に流れ落ちる水は、遠心
力の影響を受けて外に広がる挙動をし、第1図の矢印で
示すように円錐状の水MPとなって吐出される。
Here, when water is sent from the spout 50, the upstream chamber 7
From there, water flows into the downstream chamber 8 through the hole 6a of the annular wall 6. At this time, since the axis of the hole 6a faces in the tangential direction with respect to the downstream chamber 8 having a circular cross section, the water forms a swirling flow within the downstream chamber 8. That is, as shown in FIG. 2, water flows from the outer periphery of the downstream chamber 8 along the inner wall, and the water from the four holes 6a joins and swirls inside the downstream chamber 8 forming a vortex. Begin to. At this time, hole 6a
If the entire flow path area of is larger than that of the discharge port 3a,
A phenomenon occurs in which water accumulates in the downstream chamber s, and the internal pressure also rises to some extent. Therefore, inside the downstream chamber 8, the flow energy of the water itself increases, and a centrifugal force due to the swirling flow acts. Therefore, the water flowing downward from the discharge port 3a behaves to spread outward under the influence of centrifugal force, and is discharged as conical water MP as shown by the arrow in FIG.

一方、放出口3aは泡沫化チャンバ5のほぼ中央に位置
し、遠心力を伴った水が大きな流速で流れ出すため、円
錐状の水膜Fの内側の空間の内圧が低下する。このため
、空気流路22aから空気が吸い込まれ、放出口3aか
らの水膜Fが泡沫化チャンパ5の雌ネジ5aに衝き当た
って砕けた水に空気が混ざり込んで給水が泡沫化される
。そして、泡沫化された水は敗水孔21に流れ込み、整
流板23により流れが整えられて吐出される。
On the other hand, the discharge port 3a is located approximately at the center of the foaming chamber 5, and since water accompanied by centrifugal force flows out at a high flow rate, the internal pressure in the space inside the conical water film F decreases. Therefore, air is sucked in from the air flow path 22a, and the water film F from the discharge port 3a collides with the female screw 5a of the foaming champer 5, and air is mixed with the broken water, thereby foaming the supplied water. Then, the foamed water flows into the drainage hole 21, the flow is adjusted by the current plate 23, and the water is discharged.

以上の流れにおいて、泡沫化チャンパ5の上部側に設け
た逆流防止板26. 27は、放出口3aからの円錐状
の水[F及び空気吸入筒22の上端からの吸引空気に対
して障壁となることなく、これらの水及び空気を速やか
に下側へ通過させる。そして、水膜Fが雌ネジ5aに当
たって砕けて空気を混入した泡沫水は、逆流防止板26
. 27が障壁となるため放出口3a及び空気吸入筒2
2の上端側への逆流することが阻止される。このため、
空気吸入筒22の上端が泡沫水や放出口3aからの給水
を被ることがなく、空気の吸引が円滑に行われる。した
がって、空気の吸引量が十分に確保されて泡沫化が促進
されると共に、流れ込む空気に対して直接給水が混じり
合う度合も小さくなるので空気吸引音や給水音も低減さ
れる。
In the above flow, the backflow prevention plate 26 provided on the upper side of the foaming chamber 5. 27 is a cone-shaped water [F from the discharge port 3a] and the suction air from the upper end of the air suction tube 22 does not act as a barrier, but allows these water and air to quickly pass downward. Then, the water film F hits the female screw 5a and breaks, and the foamy water mixed with air flows to the backflow prevention plate 26.
.. 27 acts as a barrier, the discharge port 3a and the air intake tube 2
2 is prevented from flowing backward to the upper end side. For this reason,
The upper end of the air suction cylinder 22 is not covered with foamy water or water supplied from the discharge port 3a, and air suction is performed smoothly. Therefore, a sufficient amount of air suction is ensured to promote foam formation, and the degree to which water is directly mixed with the flowing air is also reduced, so air suction noise and water supply noise are also reduced.

また、水膜Fは泡沫化チャンバ5の雌ネジ5aに突き当
たり、その表面の凹凸によって流れの脈動等に干渉して
これを減衰させる。すなわち、給水は旋回流チャンパ4
の中で強制的に旋回させられて流動エネルギを高くした
後に放出口3aから水膜F状に流れ込む。このため、流
れ自体の脈動や慣性等によって一峻の管内流れに比べる
と、圧力変動等を生じやすい。これに対して、雌ネジ5
a等のように微小な凹凸面を設け、流れを反射させる方
向に異ならせるようにすれば、脈動エネルギの干渉が可
能となり、流れを安定化させることができる。したがっ
て、空気を混入した泡沫水が断続的な流れになったり強
弱を伴うことはなく、定流量の安定吐水が可能となる。
Further, the water film F hits the female thread 5a of the foaming chamber 5, and due to the unevenness of its surface, it interferes with the pulsation of the flow and damps it. In other words, the water supply flows through the swirling flow chamber 4.
After being forced to swirl in the water to increase the flow energy, it flows into the water film F shape from the outlet 3a. Therefore, pressure fluctuations are more likely to occur due to pulsation and inertia of the flow itself, compared to a straight pipe flow. On the other hand, female screw 5
If a minute uneven surface is provided as shown in a, and the flow is reflected in different directions, it is possible to interfere with the pulsating energy, and the flow can be stabilized. Therefore, the foamy water mixed with air does not flow intermittently or have any strength or weakness, and stable water discharge at a constant flow rate is possible.

更に、空気吸入筒22の円錐面22bは、泡沫水を緩や
かに案内しながら散水孔21へ導くので、気泡を含む気
液二層流の流れに対してキャビテーションや流路壁から
の剥離等を生じることなく送り出すことができる。この
ため、吐水時の給水音の発生が抑えられ、流量を大きく
しても使用環境に影響を及ぼすことがない。また、流量
が小さいときには、泡沫化チャンバ5内が満水にならな
いまま泡沫水が吐出される。この場合、泡沫水の流速も
低下して流線の乱れが発生しやすいが、円錐面22bに
沿って各散水孔21へ泡沫水は速やかに流れ去る。した
がって、流量が小さいときでも、泡沫水を積極的にガイ
ドすることで泡沫化チャンバ5内での滞留を防ぐことが
でき、各散水孔21へ均等に送り込むことによって、吐
水形態の変動も無くすことができる。
Furthermore, the conical surface 22b of the air suction cylinder 22 gently guides the foamy water to the water sprinkling hole 21, thereby preventing cavitation or separation from the channel wall for the gas-liquid two-layer flow containing air bubbles. It can be sent out without being generated. Therefore, the generation of water supply noise during water discharging is suppressed, and even if the flow rate is increased, the usage environment is not affected. Moreover, when the flow rate is small, foamy water is discharged without filling the foaming chamber 5 with water. In this case, the flow velocity of the foamy water also decreases and disturbance of the streamlines is likely to occur, but the foamy water quickly flows away to each water sprinkling hole 21 along the conical surface 22b. Therefore, even when the flow rate is small, by actively guiding the foamy water, it is possible to prevent it from stagnation in the foaming chamber 5, and by sending it evenly to each watering hole 21, it is possible to eliminate fluctuations in the water spouting form. Can be done.

以上のように安定させた流れの泡沫水は、雌ネジ5aか
ら第1図の矢印のように各散水孔21方向へ反射され、
特に流量が増えてくるとこの挙動は顕著となる。このと
き、ペース20上の環状整流板25は、泡沫水が中央側
へ集中することを防ぐ。すなわち、環状整流板25が邪
魔板となってこの中央側への流れ込みを抑えるので、泡
沫水が散水孔21の中央側からのみ吐水されることがな
く、各散水孔2lから一様な泡沫水が得られる。
The foamy water stabilized as described above is reflected from the female screw 5a toward each water sprinkling hole 21 as shown by the arrow in FIG.
This behavior becomes particularly noticeable as the flow rate increases. At this time, the annular current plate 25 on the pace 20 prevents foamy water from concentrating toward the center. That is, since the annular rectifying plate 25 acts as a baffle plate and suppresses the flow toward the center, foamy water is not spouted only from the center side of the water sprinkling holes 21, and foamy water is uniformly distributed from each water sprinkling hole 2l. is obtained.

更に、中央側への集中が抑えられて半径方向へ均等化し
た泡沫水は、放射状に配置されて各散水孔21の間を区
画する整流羽根24によって、より一層吐氷状態が安定
する。すなわち、放射状に配列した整流羽根24は、旋
回流チャンバ4による給水の旋回力を弱めると共に、各
敗水孔21へ向かう流れどうしを干渉させないようにす
る。このため、旋回力の低下によって動的な吐水を安定
化させると同時に、各整流羽根24によって区画された
分のみの泡沫水が外界からの影響を受けないまま安定し
た状態で吐水される。
Furthermore, the foamy water, which is suppressed from concentrating on the center side and is equalized in the radial direction, is further stabilized in the ice discharging state by the rectifying blades 24 that are arranged radially and partition the spaces between the respective water sprinkling holes 21. That is, the radially arranged rectifying vanes 24 weaken the swirling force of the water supplied by the swirling flow chamber 4, and prevent the flows toward the respective drainage holes 21 from interfering with each other. Therefore, dynamic water spouting is stabilized by reducing the swirling force, and at the same time, foamy water divided by each rectifying blade 24 is stably spouted without being influenced by the outside world.

また、吐出される直前では、泡沫水は敗水孔21を通過
するときに十字状の整流板23によって整流される。整
流板23は散水孔2lの中の流路を4分割するので、泡
沫水は整流板23を通過する間に区画された流れとなっ
て互いに平行流となるように整流され、外側へ広がった
り中央へ集中することのない吐水が得られる。
Immediately before being discharged, the foamy water is rectified by a cross-shaped rectifying plate 23 when passing through the drainage hole 21 . Since the rectifying plate 23 divides the flow path in the water sprinkling hole 2l into four, the foamy water becomes divided flows while passing through the rectifying plate 23, is rectified so that they flow parallel to each other, and spreads outward. You can get water that is not concentrated in the center.

以上のように、給水を旋回させて泡沫化チャンバ5の中
へ円錐状の水膜Fとして送り込み、これに空気を混入し
て泡沫化するので、従来のように減圧板を利用する場合
に比べて、圧力損失が格段に小さくなる。また、流量が
小さい場合でも給水は十分に泡沫化され、環状整流板2
5.整流羽根24によって泡沫水を安定化させて整流板
23を通過させるので、流れの乱れを伴うことなく最適
な泡沫吐水が得られる。
As described above, the supplied water is swirled and sent into the foaming chamber 5 as a conical water film F, and air is mixed into this to create foam, compared to the conventional case where a pressure reducing plate is used. As a result, pressure loss is significantly reduced. In addition, even when the flow rate is small, the water supply is sufficiently foamed, and the annular current plate 2
5. Since foamy water is stabilized by the straightening vanes 24 and passed through the current plate 23, optimal foamy water can be obtained without flow disturbance.

第6図は本発明の泡沫吐水口をハンドシャワータイプの
水栓とした例を示す要部の断面図、第7図はキッチンへ
の据え付け状況を示す斜視図である。なお、第1図から
第5図に示したものと同じ部材については共通の符番で
指示し、その詳細な説明は省略する。
FIG. 6 is a sectional view of the main parts of an example of a hand shower type faucet using the foam spout of the present invention, and FIG. 7 is a perspective view showing how it is installed in a kitchen. Note that the same members as those shown in FIGS. 1 to 5 are indicated by common reference numerals, and detailed explanation thereof will be omitted.

吐水ヘッド1は、ハンドシャワーとして使うためにシャ
ワー本体30に一体化され、その内部に形威した流路3
0aに連通している。シャワー本体30はキャビネット
31のカウンター32に固定されたホルダ33に出し入
れ自在に支持され、その基端にホース(図示せず)を瀉
結して湯水混合栓や電気温水器等からの給水.給湯を行
う。そして、ホルダ33はホースも含めてシャワー本体
30を引き抜き可能とし、手で握って容器等を洗えるよ
うになっている。なお、このようなホースを備えて引き
出し自在なハンドシャワーは、従来から一般に利用され
ているものである。
The water discharging head 1 is integrated into a shower body 30 for use as a hand shower, and has a flow path 3 formed inside the shower body 30.
It communicates with 0a. The shower main body 30 is supported by a holder 33 fixed to a counter 32 of a cabinet 31 so as to be able to be taken in and taken out, and a hose (not shown) is connected to the base end of the holder 33 to supply water from a hot water mixer tap, an electric water heater, etc. Provide hot water. The holder 33 allows the shower main body 30 including the hose to be pulled out, and can be held in the hand to wash containers and the like. Note that such a hand shower that is equipped with a hose and can be freely pulled out has been commonly used.

また、上流側室7はシャワー本体30に組み込んだとき
に環状に形戒され、環状の逆流防止板27は隔壁3側に
一体に設けられ、その他の構造は第1図のものとほぼ同
様である。
Further, the upstream chamber 7 is formed into an annular shape when assembled into the shower main body 30, and the annular backflow prevention plate 27 is integrally provided on the partition wall 3 side, and the other structure is almost the same as that in FIG. .

一方、カウンター32には、浅いシンク34と深いシン
ク35とが並べて形戊され、本発明の泡沫吐水口を備え
た吐水ヘッドlは浅いシンク34側に設置されている。
On the other hand, a shallow sink 34 and a deep sink 35 are formed side by side on the counter 32, and the water spout head l provided with the foam spout of the present invention is installed on the shallow sink 34 side.

また、深いシンク35側には通常のシングルレバー式の
湯水混合栓35aが設けられている。
Further, on the side of the deep sink 35, a normal single-lever type hot water mixing faucet 35a is provided.

吐水ヘッド1を設けたシャワー本体30からの泡沫吐水
は、既に説明したように泡沫化された後に流れが乱され
ることのない安定したシャワー散水となる。このため、
シンク34が浅くても、泡沫水が複数の流線に別れてシ
ャワー吐水されるので、水の飛散度が小さくなり、水は
ねの障害を無くすことができる。特に、図示のようにま
な板34aを浅いシンク34に設けた段部34bを利用
してスライドさせ、このまな板34aの上に吐水する場
合でも水はねが大きくならないことから、床を濡らした
りすることもない。
As already explained, the foamy water spouted from the shower body 30 provided with the water spouting head 1 becomes a stable shower water sprinkling without any disturbance in its flow after being turned into foam. For this reason,
Even if the sink 34 is shallow, foamy water is separated into a plurality of streamlines and showered, so the degree of water scattering is reduced and the problem of water splashing can be eliminated. In particular, even when the cutting board 34a is slid using the stepped portion 34b provided in the shallow sink 34 as shown in the figure, and water is spouted onto the cutting board 34a, the water does not splash so much that it prevents the floor from getting wet. Nor.

このように、泡沫化した後に流れが乱れないようにして
シャワー散水すれば、シンクの底面に当たったときの水
はねが少なくなるだけでなく、容器等を洗う場合の水は
ねも少なくなり、更に使い勝手が向上する。
In this way, if you sprinkle water in the shower without disturbing the flow after it turns into foam, not only will there be less water splashing when it hits the bottom of the sink, but there will also be less water splashing when washing containers, etc. , further improving usability.

第8図は従来構造との特性を比較した定性的なグラフで
あり、第6図の構造を用いた場合の特性を実線で示し、
従来構造のものを破線で示す。
Figure 8 is a qualitative graph comparing the characteristics with the conventional structure, and the solid line shows the characteristics when using the structure in Figure 6.
The conventional structure is shown by a broken line.

第8図(a)は横軸は給水量及び縦軸は内部流路におけ
る圧力降下の値をとって示す圧力損失を示すものであり
、従来構造に比べると、圧力損失が低減されている。そ
して、この圧力損失の低下により、泡沫化チャンバ5へ
流れ込む水の流速が保たれるため第8図(ロ)のように
内圧の降下も従来構造のものに比べて大きくなっている
。そして、この内圧降下は、流量が小さい域から急激に
大きくなっているので、小流量の場合でも空気の混入が
促進され、適切な泡沫化が可能となる。なお、第8図(
C)は空気の吸い込み量を示すもので、内圧降下が大き
い分だけ従来構造に比べると空気吸引量も増えている。
In FIG. 8(a), the horizontal axis shows the amount of water supplied and the vertical axis shows the pressure loss, which is the value of the pressure drop in the internal flow path, and the pressure loss is reduced compared to the conventional structure. Due to this reduction in pressure loss, the flow rate of water flowing into the foaming chamber 5 is maintained, so that the drop in internal pressure is greater than in the conventional structure, as shown in FIG. 8(b). Since this internal pressure drop increases rapidly from a region where the flow rate is small, even in the case of a small flow rate, the mixing of air is promoted and appropriate foaming becomes possible. In addition, Figure 8 (
C) indicates the amount of air sucked in, and the amount of air sucked is increased compared to the conventional structure due to the large internal pressure drop.

このように、圧力損失の低減が可能となったほか、空気
の混入も速やかに行われるため、特に泡沫化が困難であ
った低流量域でも十分な泡沫度の吐水が得られる。
In this way, in addition to being able to reduce pressure loss, air is quickly mixed in, making it possible to obtain water with sufficient foaminess even in the low flow rate region where foaming has been particularly difficult.

〔発明の効果〕〔Effect of the invention〕

以上に説明したように、本発明では、給水を旋回させる
ことにより流れに遠心力を発生させ、これを利用して泡
沫チャンパの中へ円錐状の水膜流れとして送り込み、こ
のときに発生する内圧の低下によって空気を混入させて
いる。このため、従来のように多数の小孔を開けた減圧
板を用いる場合に比べると、圧力損失が小さくなって流
量が確保され、また異物やスケールの付着による吐水不
良も解消される また、圧力損失の低減は換言すると内部流れの増速であ
りこれに基づく内部負圧の発生も大きくなる。このため
、空気流路からの空気吸引率も高くなり、低流量値でも
十分な泡沫度の吐水が得られ、広い分野での使用が可能
となる。
As explained above, in the present invention, centrifugal force is generated in the flow by swirling the supplied water, and using this, the water is sent into the foam chamber as a conical water film flow, and the internal pressure generated at this time is air is mixed in due to the drop in For this reason, compared to the conventional case of using a pressure reducing plate with many small holes, the pressure loss is reduced and a sufficient flow rate is ensured, and problems with water discharge caused by foreign matter or scale adhesion are eliminated. In other words, the reduction in loss means an increase in the speed of the internal flow, and the generation of internal negative pressure based on this also increases. For this reason, the air suction rate from the air flow path becomes high, and water with sufficient foaminess can be obtained even at a low flow rate, making it possible to use it in a wide range of fields.

更に、泡沫化チャンバの内壁に微小な凹凸を設けておけ
ば、放出口からの給水の波動に対して干渉効果を持たせ
ることができ、強制的に旋回流としたときに生じる脈動
等を減衰させて流れを安定化させることができる。
Furthermore, by providing minute irregularities on the inner wall of the foaming chamber, it is possible to create an interference effect on the wave motion of the water supplied from the outlet, attenuating the pulsation that occurs when a swirling flow is forced. This allows the flow to be stabilized.

【図面の簡単な説明】[Brief explanation of the drawing]

第l図は本発明の一実施例を示す泡沫吐水口の要部縦断
面図、第2図は環状壁の内部での旋回流の発生を示す第
1図の1−1線矢視断面図、第3図(a)は散水板の斜
視図、第3図(b)は上端に環状の逆流防止板を一体化
した場合の散水板の斜視図、第4図は吐水ヘッドの底面
図、第5図は他の整流板構造を示す吐水ヘッドの横断面
図、第6図はシャワー本体に吐水ヘッドを組み込んだ例
を示す縦断面図、第7図はキッチンのカウンターへの設
置を示す斜視図、第8図は従来構造との特性比較を示す
グラフ、第9図は従来例の概略図である。 1:吐水ヘッド   2:散水板 3:隔壁      3a:放出口 4:旋回流チャンバ 5:泡沫化チャンバ 6:環状壁 7:上流側室 20:ベース 22:空気吸入筒 5a:雌ネジ 6a:孔 8:下流側室 21:散水孔 22a:空気流路 22b:円誰面 23:整流板 25:m状整流板 27:逆流防止板 30:シャワー本体 31:キャビネット 33:ホルダ 24:整流羽根 26:逆流防止板 27a:ステー 30a:流路 32:カウンター
Fig. 1 is a longitudinal cross-sectional view of a main part of a foam spout showing an embodiment of the present invention, and Fig. 2 is a cross-sectional view taken along the line 1-1 in Fig. 1, showing the generation of swirling flow inside the annular wall. , FIG. 3(a) is a perspective view of the water sprinkling plate, FIG. 3(b) is a perspective view of the water sprinkling plate with an annular backflow prevention plate integrated at the upper end, and FIG. 4 is a bottom view of the water discharging head. Figure 5 is a cross-sectional view of the water discharge head showing another straightening plate structure, Figure 6 is a vertical cross-sectional view showing an example of the water discharge head being incorporated into the shower body, and Figure 7 is a perspective view showing installation on a kitchen counter. 8 is a graph showing a comparison of characteristics with a conventional structure, and FIG. 9 is a schematic diagram of the conventional structure. 1: Water discharge head 2: Sprinkling plate 3: Partition wall 3a: Discharge port 4: Swirling flow chamber 5: Foaming chamber 6: Annular wall 7: Upstream chamber 20: Base 22: Air suction tube 5a: Female thread 6a: Hole 8: Downstream chamber 21: Sprinkle hole 22a: Air flow path 22b: Circular surface 23: Rectifier plate 25: M-shaped rectifier plate 27: Backflow prevention plate 30: Shower body 31: Cabinet 33: Holder 24: Rectification blade 26: Backflow prevention plate 27a: Stay 30a: Channel 32: Counter

Claims (1)

【特許請求の範囲】 1、給水源に連通して流れを旋回させる旋回流チャンバ
と、前記旋回流チャンバのほぼ中央に開けた放出口によ
って該旋回流チャンバに連通する泡沫化チャンバと、前
記放出口からの水流入時の減圧降下によって前記泡沫化
チャンバに空気を吸引する空気流路とを備え、前記泡沫
化チャンバは、空気吸入部及び空気と給水の混合部とを
区画する逆流防止機構を備えていることを特徴とする泡
沫吐水口。 2、泡沫化チャンバの内壁を、前記放出口からの給水を
受けて流れに干渉する凹凸面としたことを特徴とする請
求項1記載の泡沫吐水口。
[Scope of Claims] 1. A swirling flow chamber that communicates with a water supply source and swirls the flow; a foaming chamber that communicates with the swirling flow chamber through a discharge port opened approximately in the center of the swirling flow chamber; an air flow path that sucks air into the foaming chamber by a reduced pressure drop when water flows in from the outlet; A foam spout characterized by being equipped with a foam spout. 2. The foam spout according to claim 1, wherein the inner wall of the foam forming chamber has an uneven surface that receives the water supplied from the discharge port and interferes with the flow.
JP1304491A 1989-11-21 1989-11-21 Foam spout Expired - Fee Related JPH0745017B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP1304491A JPH0745017B2 (en) 1989-11-21 1989-11-21 Foam spout
US07/614,905 US5143295A (en) 1989-11-21 1990-11-16 Bubbly water outlet device
KR1019900018592A KR970002860B1 (en) 1989-11-21 1990-11-16 Jet regulators with aerating means
CA002030677A CA2030677A1 (en) 1989-11-21 1990-11-20 Bubbly water outlet device
DE69028832T DE69028832T2 (en) 1989-11-21 1990-11-20 Spout for water enriched with air
AT90122199T ATE144015T1 (en) 1989-11-21 1990-11-20 OUTLET FOR AERATED WATER
EP90122199A EP0429068B1 (en) 1989-11-21 1990-11-20 Aerated water outlet device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1304491A JPH0745017B2 (en) 1989-11-21 1989-11-21 Foam spout

Publications (2)

Publication Number Publication Date
JPH03161063A true JPH03161063A (en) 1991-07-11
JPH0745017B2 JPH0745017B2 (en) 1995-05-17

Family

ID=17933674

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1304491A Expired - Fee Related JPH0745017B2 (en) 1989-11-21 1989-11-21 Foam spout

Country Status (1)

Country Link
JP (1) JPH0745017B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015027331A (en) * 2013-07-30 2015-02-12 Toto株式会社 Shower head device
JP2015192796A (en) * 2014-03-31 2015-11-05 Toto株式会社 Shower device
JP2015192797A (en) * 2014-03-31 2015-11-05 Toto株式会社 Shower bath
JP2015192795A (en) * 2014-03-31 2015-11-05 Toto株式会社 Shower device
JP2021020141A (en) * 2019-07-25 2021-02-18 株式会社サイエンス Bubble generating device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55140569U (en) * 1979-03-28 1980-10-07

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55140569U (en) * 1979-03-28 1980-10-07

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015027331A (en) * 2013-07-30 2015-02-12 Toto株式会社 Shower head device
JP2015192796A (en) * 2014-03-31 2015-11-05 Toto株式会社 Shower device
JP2015192797A (en) * 2014-03-31 2015-11-05 Toto株式会社 Shower bath
JP2015192795A (en) * 2014-03-31 2015-11-05 Toto株式会社 Shower device
JP2021020141A (en) * 2019-07-25 2021-02-18 株式会社サイエンス Bubble generating device

Also Published As

Publication number Publication date
JPH0745017B2 (en) 1995-05-17

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