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JPH0718180B2 - Foam spout - Google Patents
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JPH0718180B2 - Foam spout - Google Patents

Foam spout

Info

Publication number
JPH0718180B2
JPH0718180B2 JP1199864A JP19986489A JPH0718180B2 JP H0718180 B2 JPH0718180 B2 JP H0718180B2 JP 1199864 A JP1199864 A JP 1199864A JP 19986489 A JP19986489 A JP 19986489A JP H0718180 B2 JPH0718180 B2 JP H0718180B2
Authority
JP
Japan
Prior art keywords
water
chamber
swirl
flow
discharge
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.)
Expired - Lifetime
Application number
JP1199864A
Other languages
Japanese (ja)
Other versions
JPH0363333A (en
Inventor
英司 松田
正寿 榎
浩司 中野
Original Assignee
東陶機器株式会社
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 東陶機器株式会社 filed Critical 東陶機器株式会社
Priority to JP1199864A priority Critical patent/JPH0718180B2/en
Publication of JPH0363333A publication Critical patent/JPH0363333A/en
Publication of JPH0718180B2 publication Critical patent/JPH0718180B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/40Protecting water resources
    • Y02A20/411Water saving techniques at user level

Landscapes

  • Domestic Plumbing Installations (AREA)

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。
Description: TECHNICAL FIELD The present invention relates to a foam spout that is attached to the tip of a spout of a faucet, a shower head, or the like to foam water supply.

〔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使用され
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 A faucet provided with a foam spouting port has been conventionally used to reduce the noise of water supply and the noise of falling to a sink or the like and to prevent splashing of water. The most commonly used one is, for example, one described in Japanese Patent Publication No. 63-31621.

第7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51の周壁に
外の空気を給水中に取り入れる空気孔53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網54が配置さ
れている。
FIG. 7 is a cross-sectional view showing the outline of the foam spout according to 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 fixed to the tip of a spout 50 of a water faucet. Then, an air hole 53 for taking in outside air into the water supply is opened in the peripheral wall of the water discharge cap 51 downstream of the pressure reducing plate 52, and a plurality of rectifying nets 54 for rectifying the flow are arranged at the outlet. There is.

このような泡沫吐水口では、スパウト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速される。
このため、減圧板52の下流側の吐水キャップ51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攪拌される
ため、更に泡沫化が促進される。
In such a foam spout, the flow speed is increased when the water supply from the spout 50 passes through the small hole 52a of the pressure reducing plate 52.
Therefore, the inside of the water discharge cap 51 on the downstream side of the pressure reducing plate 52 is depressurized, and the outside air is sucked in through the air port 53, and the air is mixed into the water supply to foam the flow. Further, since the mesh of the rectifying net 54 is fine, the water supply is vigorously agitated even when the water supply hits against the water flow and flows away, further promoting foam formation.

〔発明が解決しようとする課題〕[Problems 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
な吐水圧が得られず、流量を小さくした場合には使い勝
手が悪くなり、泡沫化も十分に行えない。
However, the water supplied from the spout 50 is supplied through the small hole 52a of the pressure reducing plate 52.
Therefore, the pressure loss of the flow is considerably large. For this reason, unless the valve opening of the faucet is set to a certain value or more, an appropriate water discharge pressure cannot be obtained, and when the flow rate is reduced, usability becomes poor and foaming cannot be sufficiently performed.

また、減圧板52及び整流網54を2段に備えているので、
給水中の異物が詰まったり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。
Further, since the pressure reducing plate 52 and the rectifying network 54 are provided in two stages,
It is easy for foreign matter in the water supply to become clogged and scale to adhere. For this reason, if the flow passage area becomes small and the amount of water discharge becomes insufficient, or if the small holes 52a of the pressure reducing plate 52 are closed, proper foaming cannot be performed.

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、給水の圧力損失及び流路の
閉塞等の問題が避けられなかった。
As described above, the conventional foam spout uses the speedup of the water supply using the pressure reducing plate and the suction of the outside air due to the depressurization of the internal flow path based on this, so that the pressure loss of the water supply and the blockage of the flow path, etc. The problem was unavoidable.

更に、スパウト50の先端に設けた吐水キャップ51からの
泡沫吐水では、吐水の大きさは吐水キャップ51によって
決まる。このため、吐水キャップ51がスパウト50と同じ
程度の径であれば、泡沫化する前の給水をそのまま吐水
したときの広がりと同様になる。一方、泡沫吐水は給水
を和らげるため、シャワー等にも好適に利用できる。し
かし、吐水範囲が小さいと、水栓用としては適切でも、
シャワー用としては吐水範囲が小さすぎる。このため、
吐水キャップ51を大きくすればよいが、圧力損失もこれ
につれて大きくなり、前記と同様な問題が生じてしま
う。
Further, in the foam water discharge from the water discharge cap 51 provided at the tip of the spout 50, the size of the water discharge is determined by the water discharge cap 51. Therefore, if the spout cap 51 has the same diameter as the spout 50, the spout 50 has the same spread as the spouted water before being foamed. On the other hand, since foam water discharge softens the water supply, it can be suitably used for a shower or the like. However, if the water discharge range is small, it is suitable for faucets,
The water discharge range is too small for shower use. For this reason,
Although it is sufficient to increase the size of the water discharge cap 51, the pressure loss also increases accordingly, causing the same problem as described above.

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
ようにすると共に、吐水範囲を拡大してシャワー等にも
適切に利用できるようにすることを目的とする。
Therefore, the present invention ensures a flow rate without causing pressure loss or clogging of foreign matter, and always makes it possible to obtain appropriate foaming, and also to expand the water discharge range so that it can be appropriately used in a shower or the like. The purpose is to

〔課題を解決するための手段〕[Means for Solving the Problems]

本発明の泡沫吐水口は、以上の目的を達成するため、流
体の入口及び出口と、前記入口と前記出口との間を連通
させる連通路と、前記連通路に配置された旋回流チャン
バと、前記連通路からの流体を前記旋回流チャンバの内
壁に沿って流入軸が斜め方向流れとして供給する旋回孔
と、前記旋回流チャンバ内での流体の旋回流れの中心付
近であって前記出口側への連通路に臨む放出口と、前記
放出口に連通すると共に該放出口の開口面積より大きな
横断面積の空間を有し且つその端部を前記出口に連通さ
せた泡沫化チャンバと、前記泡沫化チャンバに外気と連
通させる空気流路とを備えたことを特徴とする。
In order to achieve the above object, the foam water spouting port of the present invention has an inlet and an outlet for a fluid, a communication passage communicating between the inlet and the outlet, and a swirling flow chamber arranged in the communication passage, A swirl hole for supplying the fluid from the communication passage along the inner wall of the swirl flow chamber as an oblique flow with an inflow axis, and to the outlet side near the center of the swirl flow of the fluid in the swirl flow chamber A foaming chamber facing the communication passage, a foaming chamber communicating with the discharge opening, having a cross-sectional area larger than the opening area of the discharge opening, and having an end communicating with the outlet, and the foaming chamber. The chamber is provided with an air flow path communicating with outside air.

〔作用〕[Action]

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
水膜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、泡沫化チャンバを空気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。そして、この吸引され
た空気は流れ込んでいる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。
The water that has flowed into the swirl flow chamber becomes a spiral swirl flow, and the centrifugal force outward acts on the flow itself. And
Since the flow at the discharge port opened almost in the center of the swirl chamber is also swirl-shaped, the water flowing out from the discharge port is blown outward by the centrifugal force, forming a conical water film like a foam from the discharge port. It is sent to the chemical conversion chamber. As a result, the water flowing into the foaming chamber is already easily scattered, and if the foaming chamber is opened to the atmosphere by air or the like, the air is sucked by the depressurizing effect of the water flowing in at a high speed from the discharge port. Then, the sucked air is promptly mixed into the water film-shaped water supply that is flowing in, and is discharged as foam water discharge.

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。
As described above, without using a pressure reducing plate having a large number of small holes, by supplying air after swirling the water supply to make it easily scattered, foam spouting can be obtained, and foaming with reduced pressure loss can be achieved. It will be possible.

また、旋回流チャンバからの水は遠心力によって円錐状
に広がるので、この広がったままの吐水とすれば、最終
的な吐水範囲も広がる。
Further, since the water from the swirling flow chamber spreads in a conical shape due to the centrifugal force, if the discharged water is spread as it is, the final water discharge range is also expanded.

〔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, the features of the present invention will be specifically described with reference to the 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I−I線矢視断面図である。
FIG. 1 is a longitudinal sectional view of an essential part of a water spout showing an embodiment of the present invention, and FIG. 2 is a sectional view taken along the line I-I of FIG.

図において、スパウト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、第2図
に示すように円形の横断面を持ち上端部分にはスパウト
50への接続筒1aを半径方向に突き出している。そして、
接続筒1aからほぼ水平方向に向かう流線は吐水ヘッド1
の中心から下に直角に曲がり、下端に設けた整流キャッ
プ2から吐出される内部流路が形成されている。
In the figure, a water discharge head 1 for foaming is attached to the tip of a spout 50. The water discharge head 1 has a circular cross section as shown in FIG. 2 and has a spout at the upper end.
The connecting cylinder 1a to 50 is projected in the radial direction. And
The streamline extending from the connecting tube 1a in a substantially horizontal direction is the water discharge head 1
An internal flow path is formed which is bent at a right angle downward from the center of and is discharged from the rectification cap 2 provided at the lower end.

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
外旋回流チャンバ7及び内旋回流チャンバ8に区画され
ている。外旋回流チャンバ7は接続筒1aに連通し、内旋
回流チャンバ8は隔壁3に開けた放出口3aによって泡沫
化チャンバ5に連通している。なお、隔壁3及び環状壁
6は一体成形品としておき、これを吐水ヘッド1の中に
固定する組立て構造とする。
The interior of the water discharge head 1 is vertically divided by a partition wall 3,
The swirl chamber 4 is above the partition 3 and the foaming chamber 5 is below. The swirl flow chamber 4 is partitioned into an outer swirl flow chamber 7 and an inner swirl flow 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 outer swirl chamber 7 is in communication with the connecting cylinder 1a, and the inner swirl chamber 8 is in communication with the foaming chamber 5 by means of a discharge port 3a opened in the partition wall 3. The partition wall 3 and the annular wall 6 are integrally molded and fixed in the water discharge head 1 to have an assembled structure.

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の内部に内旋回流チャンバ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、内旋回流チャンバ8の底部に開放し
ている放出口3aは内旋回流チャンバ8の中心に位置し、
その内径は内旋回流チャンバ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 discharge head 1, and has holes 6a at four positions as shown in FIG. These holes 6a are positioned inside the annular wall 6 such that the streamlines are tangential to the cross section of the inner swirling flow chamber 8. On the other hand, the discharge port 3a opened to the bottom of the inner swirl chamber 8 is located at the center of the inner swirl chamber 8,
Its inner diameter is much smaller than the inner diameter of the inner swirl flow chamber 8.

更に、泡沫化チャンバ5の周壁には空気孔5aが開けら
れ、これから空気を吸引して給水を泡沫化する。そし
て、泡沫化チャンバ5の内部は、放出口3aから吹き出さ
れ給水が空気孔5aからの空気によって十分に泡沫化でき
るような高さ及び内径を持つものとする。
Further, an air hole 5a is opened in the peripheral wall of the foaming chamber 5, from which air is sucked to foam the water supply. The inside of the foaming chamber 5 has such a height and an inner diameter that the water supplied from the discharge port 3a can be sufficiently foamed by the air from the air hole 5a.

整流キャップ2はネジ2a接合によって吐水ヘッド1の下
端に取り付けられ、その間に泡沫化促進のための網9を
設けている。そして、整流キャップ2には、泡沫水を速
やかに吐水するための整流板2bが組み込まれている。
The flow regulating cap 2 is attached to the lower end of the water discharge head 1 by joining the screws 2a, and a mesh 9 for promoting foam formation is provided therebetween. The rectifying cap 2 has a rectifying plate 2b for promptly discharging the foamed water.

ここで、スパウト50から水を送り込むと、外旋回流チャ
ンバ7から環状壁6の孔6aを通って内旋回流チャンバ8
に水が流れ込む。このとき、孔6aの軸線は円形断面の内
旋回流チャンバ8に対してタンジェルシャル方向を向い
ているので、内旋回流チャンバ8内では水が旋回流とな
る。すなわち第3図に示すように、水は内旋回流チャン
バ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成しながら内旋回流チャンバ
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のそれよりも大きければ、内旋回流チャン
バ8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、内旋回流チャンバ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、図中の破線で示
すように円錐状の水膜Fとなって吐出される。つまり、
放出口3aから円筒状の流路断面として流れ落ちるのでは
なく、水自体が持つ遠心力の作用によって半径方向へ吹
き飛ばされ、これが連続流れとなって円錐状の水膜Fと
なる。そして、水膜Fの厚さは放出口3aから遠ざかるに
つれて薄くなり、泡沫化チャンバ5の下端の網9に衝き
当たる。
Here, when water is sent from the spout 50, the inner swirl flow chamber 8 passes from the outer swirl flow chamber 7 through the hole 6a of the annular wall 6.
Water flows into. At this time, since the axis of the hole 6a is oriented in the tangential direction with respect to the inner swirl flow chamber 8 having a circular cross section, the water becomes a swirl flow in the inner swirl flow chamber 8. That is, as shown in FIG. 3, water flows along the inner wall from the outer peripheral portion of the inner swirling flow chamber 8 and the four holes 6a are formed.
The water from the above starts to swirl inside the inner swirling flow chamber 8 while forming a vortex. At this time, if the entire flow passage area of the hole 6a is larger than that of the discharge port 3a, a phenomenon in which water accumulates in the inner swirling flow chamber 8 occurs and the internal pressure rises to some extent. Therefore, the flow energy of the water itself increases inside the inner swirl flow chamber 8, and the centrifugal force by the swirl flow acts. For this reason, the water flowing down from the discharge port 3a has a behavior of spreading outward under the influence of the centrifugal force, and is discharged as a conical water film F as shown by a broken line in the figure. That is,
Instead of flowing down from the discharge port 3a as a cylindrical flow path cross section, it is blown off in the radial direction by the action of the centrifugal force of the water itself, and this becomes a continuous flow to form a conical water film F. Then, the thickness of the water film F becomes thinner as it goes away from the discharge port 3 a, and hits the net 9 at the lower end of the foaming chamber 5.

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の外の空間の内圧が低下する。このため、
空気孔5aから空気が吸い込まれ、網9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。
On the other hand, the discharge port 3a is located almost in the center of the foaming chamber 5, and water accompanied by centrifugal force flows out at a high flow rate, so that the internal pressure of the space outside the conical water film F decreases. For this reason,
Air is sucked through the air holes 5a, hits the net 9, and is mixed with the water that has been crushed, so that the water supply is foamed.

以上のようにして泡沫化された水は、整流キャップ2の
整流板2bを通り過ぎる間に整流化され、吐水ヘッド1か
ら排出される。
The water foamed as described above is rectified while passing the rectifying plate 2b of the rectifying cap 2 and is discharged from the water discharge head 1.

第4図は円錐状の水膜を形成させるための放出口3aの他
の構造例を示す要部の断面図である。
FIG. 4 is a sectional view of a main part showing another example of the structure of the discharge port 3a for forming a conical water film.

図において、放出口3aには下に向けて筒状の放出筒10が
形成され、その下端内周にガイド11が取り付けられてい
る。放出筒10の下端内周は裾広がりの断面を持つ傾斜部
10aとして形成され、ガイド11はこの傾斜部10aに沿うテ
ーパ面11aを備えている。そして、これらの傾斜部10a及
びテーパ面11aとの間の隙間が、裾広がりの円錐台状の
断面となり、水はこの断面形状によって円錐状の水膜と
なって泡沫化チャンバ5に放出される。
In the figure, a cylindrical discharge cylinder 10 is formed downward at the discharge port 3a, and a guide 11 is attached to the inner circumference of the lower end thereof. The inner circumference of the lower end of the discharge cylinder 10 has a sloping portion with a hem-widening cross section
The guide 11 has a tapered surface 11a formed along the inclined portion 10a. The gap between the inclined portion 10a and the tapered surface 11a has a frustoconical cross section with a widened hem, and water is discharged into the foaming chamber 5 as a conical water film due to this cross sectional shape. .

このような放出口3aの構造は、第1図に示したものに代
えて採用できる。この場合、旋回流チャンバ4の中での
流れに与えた遠心力に加えてガイド11によって水の流線
を末広がり状に導くため、水膜Fが安定して形成され
る。また、旋回流チャンバ4を備えずに直接水を送り込
む構造としていても、水の流線を広げる作用は変わらな
いため、水膜Fの形成が可能である。
Such a structure of the discharge port 3a can be adopted instead of the structure shown in FIG. In this case, in addition to the centrifugal force applied to the flow in the swirl flow chamber 4, the guide 11 guides the streamline of the water in a divergent manner, so that the water film F is stably formed. Further, even if the swirling flow chamber 4 is not provided and the structure is such that the water is directly sent, the action of expanding the streamline of the water does not change, so that the water film F can be formed.

更に、第5図は水膜の形成に代えて、泡沫化チャンバ5
内で水を激しく合流させることによって飛散させる構造
としたものである。
Further, FIG. 5 shows that instead of forming a water film, the foaming chamber 5
It has a structure that scatters water by violently converging inside.

図において、放出口3aの下には第4図の場合と同様に放
出筒12が形成され、その下端部設けた複数の孔12aが全
て放出口3aの軸線を向く姿勢として開けられている。放
出口3aからの水は孔12aの軸線方向に向けて放出され、
放出口3の軸線上で合流するように流れる。このため、
合流した後は図中の破線で示すように水が泡沫化チャン
バ5の中で飛散し、下方の網9又は泡沫化チャンバ5の
内壁に衝き当たったときの泡沫化が容易になる。
In the figure, a discharge cylinder 12 is formed below the discharge port 3a as in the case of FIG. 4, and a plurality of holes 12a provided at the lower end portion thereof are all opened so as to face the axis of the discharge port 3a. Water from the discharge port 3a is discharged toward the axial direction of the hole 12a,
It flows so that it may join on the axis line of the discharge port 3. For this reason,
After the merging, as shown by the broken line in the figure, water splashes in the foaming chamber 5 and facilitates foaming when hitting the lower net 9 or the inner wall of the foaming chamber 5.

第6図は泡沫化チャンバ5内での水の飛散を圧力損失が
小さい状態で可能とした構造を示す例である。これは、
第1図の構造に対して、環状壁6の上端に天板6bを設け
て外旋回流チャンバ7とは分離した部屋として内旋回流
チャンバ8を形成した天板6bに孔6cを開けた点が異なっ
ている。
FIG. 6 is an example showing a structure in which water can be scattered in the foaming chamber 5 in a state where the pressure loss is small. this is,
In comparison with the structure shown in FIG. 1, a hole 6c is formed in a top plate 6b in which an inner swirl flow chamber 8 is formed as a room separated from the outer swirl flow chamber 7 by providing a top plate 6b at the upper end of the annular wall 6. Are different.

水は孔6a,6cから内旋回流チャンバ8に流れ込み、この
ときにはタンジェンシャル方向の孔6aからの水によって
旋回流となる。そして、天板6bの孔6cからも水が流れ込
むので、遠心力に対して放出口3aへ押し出そうとする流
れも発生する。このため、第1図の構造では放出口3aか
らの水は水膜となって放出されていたが、孔6cからの水
による押し出す作用力によって水の流束が引きちぎられ
るようになり、破線で示すように放出口3aから飛散水と
なって放出される。そして、第4図及び第5図に示した
ように水の流路を大きく絞ることがなく、これらの例に
比べると圧力損失が低減される。
Water flows into the inner swirl flow chamber 8 through the holes 6a and 6c, and at this time, a swirl flow is formed by the water from the holes 6a in the tangential direction. Then, since water also flows in from the hole 6c of the top plate 6b, a flow that tends to push out to the discharge port 3a due to centrifugal force also occurs. For this reason, in the structure of FIG. 1, the water from the discharge port 3a was discharged as a water film, but the action force of water pushing out from the hole 6c causes the water flux to be torn off. As shown in the drawing, the water is discharged from the discharge port 3a as splash water. Further, as shown in FIGS. 4 and 5, the water flow path is not greatly restricted, and the pressure loss is reduced as compared with these examples.

以上のように、放出口3aからは第1図及び第3図で示し
たような水膜F又は第4図から第6図で示したような飛
散水が泡沫化チャンバ5内へ送り込まれる。また、いず
れの場合でも流速が大きくなることから、空気孔5aから
の空気の吸引も速やかに行われる。したがって、網9ま
たは泡沫化チャンバ5の内壁に衝き当たって砕けた水に
空気が混ざり込み、良好な泡沫吐水が得られる。
As described above, the water film F as shown in FIGS. 1 and 3 or the splashed water as shown in FIGS. 4 to 6 is fed into the foaming chamber 5 from the discharge port 3a. In addition, since the flow velocity is high in any case, the suction of air from the air hole 5a is also performed quickly. Therefore, the air is mixed with the water crushed by hitting the net 9 or the inner wall of the foaming chamber 5, and good foam discharge can be obtained.

また、旋回流チャンバ4から放出される水は円錐状に広
がるので、泡沫化チャンバ5に流れ込む水の吐水範囲も
広がる。このため、泡沫化チャンバ5の径を大きくして
おけば、スパウト50は小さくても最終的に得られる吐水
の範囲は拡大する。したがって、スパウト50からの最大
流量が決まっていても、従来例に比べると吐水範囲が大
きなものをゆったりと吐水させることができる。その結
果、泡沫化による給水のソフト化に加えて大口径の吐水
が可能となり、シャワーやその他の用途にも好適に利用
できる。
Further, since the water discharged from the swirling flow chamber 4 spreads in a conical shape, the discharge range of the water flowing into the foaming chamber 5 also expands. For this reason, if the diameter of the foaming chamber 5 is increased, the range of the finally obtained spouting water is expanded even if the spout 50 is small. Therefore, even if the maximum flow rate from the spout 50 is determined, it is possible to loosely discharge water having a large water discharge range as compared with the conventional example. As a result, in addition to softening the water supply by foaming, it is possible to discharge water with a large diameter, and it can be suitably used for showers and other applications.

なお、旋回流チャンバ4における流れの旋回化及び泡沫
化チャンバ5における泡沫化のための構造は、実施例の
他にも各種のものが考えられる。たとえば、旋回流チャ
ンバ4に設ける環状壁6に代えて、多数の翼列によって
環状壁6に相当するものを形成し、各翼の間の流路を孔
6aとして使うことや、環状壁6にスリットを設けてこれ
を流路とする等である。これらのいずれにおいても、旋
回流チャンバ4に流れ込む給水を渦流化するために、翼
やスリットをタンジェンシャル方向として水を旋回させ
る方向へ送り込む構成とすることが基本である。また、
泡沫化チャンバ5に設ける空気孔5aに代えて、整流キャ
ップ2の中心部から上に空気筒を立ち上げてその上端を
空気吸引部としたり、また逆に吐水ヘッド1の上端から
旋回流チャンバを経て放出口3を貫通するように空気筒
を設けてその下端から空気を送り込むようにしてもよ
い。
In addition to the embodiment, various structures can be considered for the structure for swirling the flow in the swirling flow chamber 4 and foaming in the foaming chamber 5. For example, instead of the annular wall 6 provided in the swirl flow chamber 4, what is equivalent to the annular wall 6 is formed by a large number of blade rows, and the flow passages between the blades are opened.
It is used as 6a, or a slit is provided in the annular wall 6 to use this as a flow path. In any of these, in order to swirl the feed water flowing into the swirl flow chamber 4, it is basically configured to feed water in a swirling direction with the blades and slits as tangential directions. Also,
Instead of the air hole 5a provided in the foaming chamber 5, an air cylinder is raised from the central portion of the flow regulating cap 2 and the upper end thereof is used as an air suction portion, and conversely, a swirl flow chamber is provided from the upper end of the water discharge head 1. An air cylinder may be provided so as to penetrate through the discharge port 3 and the air may be sent from the lower end thereof.

〔発明の効果〕〔The invention's effect〕

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
沫化チャンバ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。
As described above, in the present invention, the centrifugal force is generated in the flow by swirling the water supply, and the centrifugal force is utilized to feed the centrifugal force into the foaming chamber as a conical water film flow.
Air is mixed due to the decrease in internal pressure generated at this time. Therefore, as compared with the conventional case where a pressure reducing plate having a large number of small holes is used, the pressure loss is reduced, the flow rate is secured, and defective water discharge due to adhesion of foreign matter or scale is eliminated.

更に、旋回流チャンバでの旋回流化による遠心力の発生
によって吐水を円錐状に広げることができ、泡沫化チャ
ンバで泡沫化した吐水の範囲を拡大させることができ
る。このため、泡沫化によるソフト化に加えてゆったり
とした吐水が可能となり、シャワー等にも適切に利用で
きる。
Further, the spouted water can be spread conically by the generation of centrifugal force due to the swirling flow in the swirl flow chamber, and the range of the spouted water spouted in the foaming chamber can be expanded. For this reason, in addition to softening by foaming, loose water can be discharged, and it can be appropriately used for a shower or the like.

【図面の簡単な説明】[Brief description of drawings]

第1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図は第1図のI−I線矢視断面図、第3図
(a)は環状壁の内部での旋回流の発生を示す縦断面
図、第3図(b)は横断面図、第4図はガイドを用いて
水膜を形成する例の断面図、第5図は水を合流させて飛
散水を造り出す例を示す断面図、第6図は環状壁を利用
して飛散水を形成する例の断面図、第7図は従来の泡沫
吐水口の断面図である。 1:吐水ヘッド、1a:接続筒 2:整流キャップ、2a:ネジ 2b:整流板 3:隔壁、3a:放出口 4:旋回流チャンバ 5:泡沫化チャンバ、5a:空気孔 6:環状壁、6a:孔 6b:天板、6c:孔 7:外旋回流チャンバ 8:内旋回流チャンバ 9:網 10:放出筒、10a:傾斜部 11:ガイド、11a:テーパ面 12:放出筒、12a:孔
FIG. 1 is a longitudinal sectional view of an essential part of a foam spout showing an embodiment of the present invention, FIG. 2 is a sectional view taken along the line II of FIG. 1, and FIG. Fig. 3 (b) is a cross-sectional view showing the generation of a swirl flow in Fig. 4, Fig. 4 is a cross-sectional view of an example in which a water film is formed using a guide, and Fig. 5 is a view showing the confluence of water. FIG. 6 is a sectional view showing an example of producing splashed water, FIG. 6 is a sectional view of an example of forming splashed water by utilizing an annular wall, and FIG. 7 is a sectional view of a conventional foam spout. 1: Water discharge head, 1a: Connection cylinder 2: Flow cap, 2a: Screw 2b: Flow plate 3: Partition wall, 3a: Outlet port 4: Swirling flow chamber 5: Foaming chamber, 5a: Air hole 6: Annular wall, 6a : Hole 6b: Top plate, 6c: Hole 7: Outer swirl flow chamber 8: Inner swirl flow chamber 9: Net 10: Discharge cylinder, 10a: Inclined part 11: Guide, 11a: Tapered surface 12: Discharge cylinder, 12a: Hole

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】流体の入口及び出口と、前記入口と前記出
口との間を連通させる連通路と、前記連通路に配置され
た旋回流チャンバと、前記連通路からの流体を前記旋回
流チャンバの内壁に沿って流入軸が斜め方向流れとして
供給する旋回孔と、前記旋回流チャンバ内での流体の旋
回流れの中心付近であって前記出口側への連通路に臨む
放出口と、前記放出口に連通すると共に該放出口の開口
面積より大きな横断面積の空間を有し且つその端部を前
記出口に連通させた泡沫化チャンバと、前記泡沫化チャ
ンバに外気と連通させる空気流路とを備えたことを特徴
とする泡沫吐水口。
1. A fluid inlet and an outlet, a communication passage for communicating between the inlet and the outlet, a swirl flow chamber arranged in the communication passage, and a fluid from the communication passage for the swirl chamber. A swirl hole in which the inflow axis supplies as an oblique flow along the inner wall of the swirl, a discharge port near the center of the swirl flow of the fluid in the swirl flow chamber and facing the communication path to the outlet side, and the discharge port. A foaming chamber communicating with the outlet and having a space with a cross-sectional area larger than the opening area of the outlet and having its end communicating with the outlet, and an air channel for communicating the outside with the foaming chamber. A foam spout that is equipped.
JP1199864A 1989-07-31 1989-07-31 Foam spout Expired - Lifetime JPH0718180B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1199864A JPH0718180B2 (en) 1989-07-31 1989-07-31 Foam spout

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1199864A JPH0718180B2 (en) 1989-07-31 1989-07-31 Foam spout

Publications (2)

Publication Number Publication Date
JPH0363333A JPH0363333A (en) 1991-03-19
JPH0718180B2 true JPH0718180B2 (en) 1995-03-01

Family

ID=16414917

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1199864A Expired - Lifetime JPH0718180B2 (en) 1989-07-31 1989-07-31 Foam spout

Country Status (1)

Country Link
JP (1) JPH0718180B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007056559A (en) * 2005-08-25 2007-03-08 Toto Ltd Shower head

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007056559A (en) * 2005-08-25 2007-03-08 Toto Ltd Shower head

Also Published As

Publication number Publication date
JPH0363333A (en) 1991-03-19

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