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JPH0679684B2 - Foam spout - Google Patents

Foam spout

Info

Publication number
JPH0679684B2
JPH0679684B2 JP30449289A JP30449289A JPH0679684B2 JP H0679684 B2 JPH0679684 B2 JP H0679684B2 JP 30449289 A JP30449289 A JP 30449289A JP 30449289 A JP30449289 A JP 30449289A JP H0679684 B2 JPH0679684 B2 JP H0679684B2
Authority
JP
Japan
Prior art keywords
water
chamber
flow
holes
discharge port
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 - Fee Related
Application number
JP30449289A
Other languages
Japanese (ja)
Other versions
JPH03165855A (en
Inventor
健次 岡山
雅彦 今園
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 JP30449289A priority Critical patent/JPH0679684B2/en
Publication of JPH03165855A publication Critical patent/JPH03165855A/en
Publication of JPH0679684B2 publication Critical patent/JPH0679684B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
取り付けられ空気を混入した泡沫水を吐水可能とした吐
水機構及びこれを使って泡沫水が得られるようにした泡
沫吐水口に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of use] The present invention relates to a water discharge mechanism attached to the tip of a spout of a faucet, a shower head or the like and capable of discharging foam water containing air, and a foaming mechanism using the same. It relates to a foam spout that allows water to be obtained.

〔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 A faucet provided with a foam spouting port has been conventionally used in order to reduce the sound of water supply and the sound 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8図はこの公報に記載のもの及び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ヘッド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よりも下流の吐水ヘッド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. 8 is a cross-sectional view showing the outline of another general foam spouting outlet described in this publication. In the figure, a pressure reducing plate 52 having a large number of small holes 52a is housed in a water discharge head 51 fixed to the tip of a spout 50 of a faucet. And
An air hole 53 for taking in outside air into the water supply is formed in the peripheral wall of the water discharge head 51 downstream of the pressure reducing plate 52, and a plurality of rectifying nets 54 for rectifying the flow are arranged at the outlet.

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の下流側の吐水ヘッド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 head 51 on the downstream side of the pressure reducing plate 52 is depressurized, the outside air is sucked from the air port 53, and the flow is foamed by mixing this air into the water supply. 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
(内径ほぼ1mm程度)を通過するため、流れの圧力損失
がかなり大きくなる。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り、使い勝手が悪くなる。更に、
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。
However, the water supplied from the spout 50 is supplied through the small hole 52a of the pressure reducing plate 52.
Since it passes through (inner diameter of about 1 mm), the pressure loss of the flow becomes considerably large. Therefore, unless the valve opening of the faucet is set to a certain value or more, an appropriate water discharge pressure cannot be obtained. Further, when the flow rate is reduced, water is not foamed or has no foamy feeling, resulting in poor usability. Furthermore,
Since the pressure reducing plate 52 and the flow straightening net 54 are provided in two stages, foreign matter in the water supply is easily clogged and scale is likely 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。
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 is large and In addition to obstacles such as blockage, there was a problem that it could not be used properly at low flow rates.

そこで、本発明は、従来の泡沫化に代えて、圧力損失が
小さくて済みスケール付着等もなく、且つ常に適切な泡
沫水が得られるようにすることを目的とする。
Therefore, it is an object of the present invention to replace the conventional foaming with a small pressure loss and to prevent scale adhesion and to always obtain appropriate foamed water.

〔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、吐水ヘッドの内部に、ほぼ環状
の上流側室及び該上流側室との間に隔壁を形成して区画
した下流側室を形成し、前記下流側室の底部のほぼ中央
に放出口を開け、前記隔壁に前記下流側室の内部で給水
を旋回させる流路軸線を持つ複数の孔をそれぞれの高さ
位置を互いに異ならせて配列し、前記放出口に一端が連
通し他端を吐水端とした泡沫化チャンバを備え、該泡沫
化チャンバに前記放出口へ向けて空気吸引用の空気流路
を備えてなることを特徴とする。
The foam water discharge port of the present invention forms a substantially annular upstream side chamber inside the water discharge head and a downstream side chamber defined by forming a partition wall between the upstream side chamber and the upstream side chamber, and the foamed water discharge port is discharged to approximately the center of the bottom of the downstream side chamber. An outlet is opened, and a plurality of holes having a flow path axis for swirling the water supply inside the downstream chamber are arranged in the partition wall at different height positions, and one end communicates with the discharge port and the other end It is characterized in that a foaming chamber serving as a water discharge end is provided, and the foaming chamber is provided with an air flow path for sucking air toward the discharge port.

〔作用〕[Action]

吐水ヘッドに供給された水は上流側室に流入した後、隔
壁に開けた孔から下流側室に流れ込む。このとき、孔の
姿勢を適切にすることによって、下流側室内での流れは
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、下流側室のほぼ中央に開けた放出
口部分での流れが渦巻き状となるため、放出口から流れ
出る水は遠心力により外側へ吹き飛ばされ、放出口から
円錐の水膜状となって吐水される。このとき、隔壁に開
けた複数の孔はその高さ位置が互いに異なっているの
で、各孔から下流側室に送り込まれた水どうしの干渉が
抑えられ、旋回力を上げる結果となる。
The water supplied to the water discharge head flows into the upstream chamber, and then flows into the downstream chamber from the hole formed in the partition wall. At this time, by appropriately adjusting the posture of the holes, the flow in the downstream chamber becomes a swirling swirl flow, and an outward centrifugal force acts on the flow itself. Then, since the flow at the discharge port opened in the center of the downstream chamber becomes a spiral, the water flowing out from the discharge port is blown out by the centrifugal force to the outside, and is discharged as a conical water film from the discharge port. It At this time, since the plurality of holes formed in the partition wall have different height positions from each other, the interference between the water sent from each hole to the downstream chamber is suppressed, and the turning force is increased.

また、泡沫化チャンバを一体に備えたとき、放出口から
の水は円錐状の水膜状となって泡沫化チャンバに送り込
まれる。そして、泡沫化チャンバには放出口へ向けて空
気流路を設けているので、放出口から高速で流入する水
による減圧効果によって、空気流路から空気が吸引され
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。
Further, when the foaming chamber is integrally provided, the water from the discharge port becomes a conical water film and is sent to the foaming chamber. Since the air passage is provided in the foaming chamber toward the outlet, the air is sucked from the air passage due to the depressurizing effect of the water flowing at a high speed from the outlet. 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.

〔実施例〕〔Example〕

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線矢視断面図である。
FIG. 1 is a longitudinal sectional view of a main part of a foam 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1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 spouting head 1 has a circular cross section, and a streamline extending from the spout 50 in a substantially horizontal direction is bent at a right angle downward from the center of the water spouting head 1 to form an internal flow path discharged from a water spray plate 2 provided at the lower end. Has been done.

吐水ヘッド1の内部は仕切壁3によって上下に分割さ
れ、この仕切壁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、仕
切壁3と吐水ヘッド1の上端内壁との間を繋ぐ環状の隔
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は仕切
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、仕切壁3及び環状の隔壁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 divided into upper and lower parts by a partition wall 3, and an upper part of the partition wall 3 is a swirling flow chamber 4 and a lower part thereof is a foaming chamber 5. The swirl flow chamber 4 is partitioned into an upstream chamber 7 and a downstream chamber 8 by an annular partition wall 6 that connects the partition wall 3 and the inner wall of the upper end 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 opened in the partition wall 3. The partition wall 3 and the ring-shaped partition wall 6 are integrally molded and fixed in the water discharge head 1.

隔壁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3箇所に孔6a,6b,6cを開けている。これ
らの孔6a〜6cの詳細を第3図及び第4図に示す。
The partition wall 6 is arranged coaxially with the flow passage cross section of the water discharge head 1, and
As shown in the figure, holes 6a, 6b, 6c are opened at three locations. Details of these holes 6a to 6c are shown in FIG. 3 and FIG.

第3図(b)のように隔壁6に開けた孔6a〜6cは内部の
下流側室8の横断面に対して流路軸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。たとえば、下流側室8の内径を18mmとしたとき放出
口3aの内径は8mm程度であり、また孔6a〜6cの内径は5mm
程度であって隔壁6の肉厚はほぼ3mm程度である。そし
て、第3図(b)のようにそれぞれの孔6a〜6cの流路軸
線は下流側室8の内周壁に対する接線と平行であり、隔
壁6の肉厚が3mm程度であっても内周壁に連なる流路長
さが十分に大きく、供給される水に方向性を与えながら
下流側室8に送り込むことができる。
As shown in FIG. 3 (b), the holes 6a to 6c formed in the partition wall 6 are in such a posture that the flow path axis is in the tangential direction with respect to the cross section of the internal downstream chamber 8. On the other hand, the downstream chamber 8
The discharge port 3a which is open to the bottom is located at the center of the downstream chamber 8 and has an inner diameter much smaller than that of the downstream chamber 8. For example, when the inner diameter of the downstream chamber 8 is 18 mm, the inner diameter of the discharge port 3a is about 8 mm, and the inner diameter of the holes 6a to 6c is 5 mm.
The thickness of the partition wall 6 is about 3 mm. As shown in FIG. 3 (b), the flow axis of each of the holes 6a to 6c is parallel to the tangent line to the inner peripheral wall of the downstream chamber 8, and even if the partition wall 6 has a wall thickness of about 3 mm, The length of the continuous flow path is sufficiently large so that the supplied water can be fed to the downstream chamber 8 while giving directionality.

また、これらの孔6a〜6cは、第4図に示すように下流側
室8の底部からの高さが互いに異なっている。すなわ
ち、流入側に最も近い孔6aの高さが最も低く、第2図に
おいて時計方向に配列された孔6b及び6cがそれぞれ順に
高いレベルに開けられている。なお、流入側の孔6aから
孔6cまでの高さをこの順に低くするのが必須ではなく、
とにかく孔6a〜6cのレベルを互いに異ならせておけばよ
い。このように孔6a〜6cの高さを異ならせると、各孔6a
〜6cから下流側室8に流れ込む水は、互いの流れに干渉
し合う度合が小さくなり、孔6a〜6cからの水は下流側室
8の内周壁に沿った旋回流れを持続させることができ
る。つまり、孔6a〜6cを同じ高さとした場合では、各孔
6a〜6cからの流れは他の孔からの水の流入によって流れ
が乱れ、旋回流の力を互いに弱めてしまう。これに対
し、水の流れ込み位置を上下に分けておけば、それぞれ
の孔6a〜6cからの水が下流側室8の内周壁に沿ってほぼ
1周できるような流れとなり、上下に3段のこのような
流れによって下流側室8内での旋回流を強くすることが
できる。
Further, the holes 6a to 6c have different heights from the bottom of the downstream chamber 8 as shown in FIG. That is, the hole 6a closest to the inflow side has the lowest height, and the holes 6b and 6c arranged in the clockwise direction in FIG. Incidentally, it is not essential to lower the height from the inflow side hole 6a to the hole 6c in this order,
Anyway, the levels of the holes 6a to 6c should be different from each other. When the heights of the holes 6a to 6c are made different in this way, the respective holes 6a
The water flowing into the downstream chamber 8 from 6 to 6c is less likely to interfere with each other, and the water from the holes 6a to 6c can maintain the swirling flow along the inner peripheral wall of the downstream chamber 8. In other words, if holes 6a-6c have the same height,
The flow from 6a to 6c is disturbed by the inflow of water from other holes, and the forces of the swirling flows are weakened. On the other hand, if the water inflow position is divided into the upper and lower positions, the water from the holes 6a to 6c can flow almost once along the inner peripheral wall of the downstream side chamber 8, and the three upper and lower stages are formed. The swirling flow in the downstream chamber 8 can be strengthened by such a flow.

また、第2図に示すように上流側室7に堰7aを設けて水
が図において時計方向にのみ流れるようにしてもよい。
そして、給水は堰7aに行くに連れて流動エネルギが減衰
してゆくので、これを補うために孔6a〜6cの開口面積を
この順に小さくしておき、下流側室8に流れ込む水を増
速させるようにする。このような水の流れにより、上流
側室7を2方向に分かれて供給する場合に比べると、下
流側室8内では強い旋回力の渦流を発生させることがで
きる。
Further, as shown in FIG. 2, a weir 7a may be provided in the upstream chamber 7 so that water flows only in the clockwise direction in the figure.
The flow energy of the water supply decreases as it goes to the weir 7a. To compensate for this, the opening areas of the holes 6a to 6c are reduced in this order to accelerate the water flowing into the downstream chamber 8. To do so. By such a flow of water, a swirl flow having a strong swirling force can be generated in the downstream side chamber 8 as compared with a case where the upstream side chamber 7 is divided and supplied in two directions.

なお、第1図においては、説明のために孔6a〜6cの位置
を実際とは異なったものとして示している。また、第2
図においても孔6a〜6cが全て開口として示しているが、
実際には第4図のようにそれぞれの孔6a〜6cの高さは異
なっている。
In FIG. 1, the positions of the holes 6a to 6c are shown as being different from the actual positions for the sake of explanation. Also, the second
Although the holes 6a to 6c are all shown as openings in the figure,
Actually, the heights of the holes 6a to 6c are different as shown in FIG.

一方、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5図
(a)にその全体斜視図を示す。
On the other hand, the water sprinkling plate 2 is provided with an air suction structure for rectifying and discharging the foam water and foaming the foam water, and FIG. 5 (a) is an overall perspective view thereof.

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20に
合計6個の散水孔21が設けられている(第6図)。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
上に形成し、その内部に空気流路22aを設けている。各
散水孔21の内部には十字状の整流板23が組み込まれ、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が設けられている。更
に、ベース20の上面にはベース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。
At one end of the water spray plate 2 is provided a base 20 integrated with the discharge end of the water discharge head 1 by screwing or the like, and a total of six water spray holes 21 are provided in this base 20 (FIG. 6). An air suction cylinder 22 is formed coaxially upward from the center of the base 20, and an air flow path 22a is provided inside the air suction cylinder 22. A cross-shaped straightening vane 23 is incorporated in each water spray hole 21, and six straightening vanes 24 extending radially from the air suction cylinder 22 are provided on the upper surface of the base 20 as shown in the drawing. In addition, the top surface of the base 20 is coaxial with the base 20 and has a water spray hole.
A circular ring-shaped straightening plate 25 passing through the center of 21 is provided.

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
いか又は同じ程度である。更に、第1図に示すように仕
切壁3の下には泡沫化チャンバ5と同軸配置となるよう
に環状の逆流防止板27が設けられる。なお、この逆流防
止板27は第5図(b)に示すように散水板2に一体化し
てもよい。この場合では、空気吸入筒22の上端に4本の
ステー27aを連結して環状の逆流防止板27を一体化し、
水や空気の流れに障害を与えない構造とする。そして、
吐水ヘッド1に組み込んだときには逆流防止板27の上端
が仕切壁3の上面に密着させる。更に、泡沫化チャンバ
5の内周壁には雌ネジ5aが干渉面として形成されてい
る。
A backflow prevention plate 26 is provided at a position higher than the upper half of the air suction cylinder 22. The backflow prevention plate 26 has a disc shape and is attached in a horizontal posture, and its outer diameter is smaller than or equal to that of the annular flow regulating plate 25. Further, as shown in FIG. 1, an annular backflow prevention plate 27 is provided below the partition wall 3 so as to be coaxially arranged with the foaming chamber 5. The backflow prevention plate 27 may be integrated with the water spray plate 2 as shown in FIG. 5 (b). In this case, four stays 27a are connected to the upper end of the air suction cylinder 22 to integrate the annular backflow prevention plate 27,
The structure will not interfere with the flow of water and air. And
When incorporated in the water discharge head 1, the upper end of the backflow prevention plate 27 is brought into close contact with the upper surface of the partition wall 3. Further, a female screw 5a is formed as an interference surface on the inner peripheral wall of the foaming chamber 5.

ここで、スパウト50から水を送り込むと、上流側室7か
ら隔壁6の孔6a〜6cを通って下流側室8に水が流れ込
む。このとき、既に説明したように各孔6a〜6cの軸線の
姿勢によって、流れ込んだ水は下流側室8内で旋回流と
なる。このとき、孔6a〜6cの全体の流路面積が放出口3a
のそれよりも大きければ、下流側室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、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膜Fとなっ
て吐出される。そして、前記のような孔6a〜6cの内径及
びその位置,下流側室8の内径及び放出口3aの内径等の
寸法関係の場合、一般的なシャワーの通常流量であって
浴槽への給水給湯厚程度の条件に設定しておけば、下流
側室8内での流れの旋回力を強くすることができる。ま
た、孔6a〜6cを第4図のように高さが異なるように開け
ることによって、各孔6a〜6cからの流れどうしの干渉を
抑え、更に旋回力を上げることができる。
Here, when water is sent from the spout 50, the water flows from the upstream chamber 7 through the holes 6a to 6c of the partition wall 6 into the downstream chamber 8. At this time, as described above, the flowed water becomes a swirling flow in the downstream chamber 8 depending on the posture of the axes of the holes 6a to 6c. At this time, the entire flow passage area of the holes 6a to 6c is the discharge port 3a.
If it is larger than that, the phenomenon that water stays in the downstream chamber 8 occurs, and the internal pressure rises to some extent. Therefore, inside the downstream chamber 8, the flow energy of the water itself increases, and the centrifugal force due to the swirling flow acts. Therefore, 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 an arrow in FIG. Then, in the case of the dimensional relationships such as the inner diameters and positions of the holes 6a to 6c, the inner diameter of the downstream chamber 8 and the inner diameter of the discharge port 3a as described above, the normal flow rate of a general shower and the thickness of water supplied to the bathtub By setting the conditions to some extent, the swirling force of the flow in the downstream chamber 8 can be increased. Further, by opening the holes 6a to 6c so as to have different heights as shown in FIG. 4, it is possible to suppress interference between the flows from the holes 6a to 6c and further increase the turning force.

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が泡沫化チャンバ5に刻んだ雌ネジ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、泡沫化された水は散水孔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 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 inside the conical water film F decreases. Therefore, the air is sucked from the air flow path 22a, the water film F from the discharge port 3a hits the female screw 5a carved in the foaming chamber 5, and the air is mixed with the crushed water to foam the water supply. It Then, the foamed water flows into the water spray holes 21, and the flow is regulated by the straightening vane 23 to be discharged.

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。このため、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25,整流羽根24によって泡沫水を安定化させて整流板2
3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 supply water is swirled and sent into the foam formation chamber 5 as a conical water film F, and air is mixed into this to form foam, so compared to the case where a pressure reducing plate is used as in the conventional case. As a result, the pressure loss is significantly reduced. Therefore, even if the flow rate is small, the water supply is sufficiently foamed, and the foamed water is stabilized by the annular flow straightening plate 25 and the flow straightening vanes 24 to stabilize the flow of water.
Since 3 is passed, optimum foam spouting can be obtained without flow turbulence.

なお、空気吸入筒22の空気流路22aの流路断面の内径を
3.5mm程度とし空気吸入筒22の上端と仕切壁3の下面と
の距離を6mm程度とすれば、通常の一般家庭用の給水圧
の場合に騒音が小さくしかも空気吸引量も多いことが確
認された。したがって、このような寸法関係を持たせる
ことにより、低騒音でしかも泡沫化が良好に行える製品
として供給できる。
Note that the inner diameter of the flow passage cross section of the air flow passage 22a of the air suction cylinder 22 is
If the distance between the upper end of the air suction cylinder 22 and the lower surface of the partition wall 3 is set to about 6 mm, it is confirmed that the noise is small and the amount of air suction is large in the case of ordinary household water supply pressure. It was Therefore, by providing such a dimensional relationship, it can be supplied as a product with low noise and good foaming.

第7図は旋回流による水膜吐水を可能とした例を示す概
略断面図であり、これは吐水ヘッド1に旋回流チャンバ
4のみを設けたものである。
FIG. 7 is a schematic cross-sectional view showing an example in which a water film can be discharged by a swirling flow, in which the water discharge head 1 is provided with only a swirling flow chamber 4.

図において、吐水ヘッド1の内部には、第1図と同様に
環状の隔壁6が形成されてその外部をスパウト50に連通
する上流側室7及び内部を下流側室8としている。下流
側室8の底部の中央には吐水口8aが放出口として開けら
れ、第3図で説明した寸法関係及び流路軸線を持って隔
壁6に孔6a〜6cを設けている。そして、これらの孔6a〜
6cは第4図のようにそれぞれ高さ位置を異ならせて配置
され、下流側室8へ各孔6a〜6cから流れ込むそれぞれの
流れどうしの干渉を抑える。
In the drawing, an annular partition wall 6 is formed inside the water discharge head 1 as in FIG. 1, and the outside thereof is connected to the spout 50, and an upstream side chamber 7 and an inside thereof are referred to as a downstream side chamber 8. A water discharge port 8a is opened at the center of the bottom of the downstream chamber 8 as a discharge port, and holes 6a to 6c are provided in the partition wall 6 with the dimensional relationship and the flow channel axis line described in FIG. And these holes 6a ~
As shown in FIG. 4, 6c are arranged at different height positions to suppress interference between the respective flows flowing from the holes 6a to 6c into the downstream chamber 8.

このように旋回流チャンバ4のみを備えた構成でも、供
給された水は下流側室8内で旋回して渦流れとなり、吐
出口8aからの水は遠心力の作用によって外に広がり図中
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。そして、孔6a〜6cの高さ位置を異ならせて流れの旋
回力を強くしているので、吐出口8aからの吐水の遠心力
も大きくなり、水膜Fのミスト化が促進される。このた
め水膜Fを利用した泡沫吐水に代わるソフトタッチの吐
水が得られる。
Even in the configuration including only the swirl flow chamber 4 as described above, the supplied water swirls in the downstream chamber 8 to form a swirl flow, and the water from the discharge port 8a spreads out by the action of the centrifugal force to the broken line in the figure. As shown by, the water is discharged as a conical water film F. Since the height positions of the holes 6a to 6c are made different to strengthen the swirling force of the flow, the centrifugal force of the water discharged from the discharge port 8a also becomes large, and the mist formation of the water film F is promoted. For this reason, soft-touch water discharge using the water film F instead of foam water discharge can be obtained.

〔発明の効果〕〔The invention's effect〕

以上に説明したように、本発明では、給水を旋回させた
後にこれを円錐状の水膜流れとして排出するようにし、
空気の吸引によって泡沫化して吐水できるようにしてい
る。このため、従来のように減圧板を利用するのに比べ
ると圧力損失も小さくスケール付着の問題も解消され
る。また、旋回流とするために開けた環状壁の複数の孔
の高さ位置を異ならせているので、それぞれの孔からの
水の流れどうしの干渉を抑えることができ、旋回力が強
くなる。このため、流量が小さい場合でも流れの旋回が
促進され、一般に小流量では泡沫化が不十分であった問
題も解消できる。
As described above, in the present invention, after swirling the water supply, it is discharged as a conical water film flow,
It is made to foam and spout water by suction of air. Therefore, the pressure loss is small as compared to the conventional case where the pressure reducing plate is used, and the problem of scale adhesion is solved. Further, since the height positions of the plurality of holes of the annular wall opened to form the swirling flow are made different, it is possible to suppress the interference between the water flows from the respective holes, and the swirling force becomes stronger. Therefore, swirling of the flow is promoted even when the flow rate is small, and the problem that foaming is generally insufficient at a small flow rate can be solved.

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

第1図は本発明の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)は環状壁に開
ける孔の詳細を示す縦断面図、第3図(b)は横断面
図、第4図は環状壁に開けた孔の高さ位置を示す図、第
5図は散水板の斜視図、第6図は第1図の底面図、第7
図は旋回流チャンバによる水膜吐水を示す図、第8図は
従来例の概略図である。 1:吐水ヘッド、2:散水板 3:仕切壁、3a:放出口 4:旋回流チャンバ 5:泡沫化チャンバ、5a:雌ネジ 6:隔壁、6a,6b,6c:孔 7:上流側室 8:下流側室、8a:吐水口(放出口) 20:ベース、21:散水孔 22:空気吸入筒、22a:空気流路 23:整流板、24:整流羽根 25:環状整流板、26,27:逆流防止板
1 is a longitudinal sectional view of a main part of a foam spout according to the present invention, FIG. 2 is a sectional view taken along the line II of FIG. 1, and FIG. 3 (a) is a longitudinal sectional view showing details of holes formed in an annular wall. Fig. 3 (b) is a cross-sectional view, Fig. 4 is a diagram showing the height position of holes formed in the annular wall, Fig. 5 is a perspective view of the water spray plate, and Fig. 6 is a bottom view of Fig. 1. Figure, 7th
FIG. 8 is a diagram showing water film discharge by a swirl flow chamber, and FIG. 8 is a schematic diagram of a conventional example. 1: Water discharge head, 2: Water sprinkling plate 3: Partition wall, 3a: Outlet port 4: Swirling flow chamber 5: Foaming chamber, 5a: Female screw 6: Partition wall, 6a, 6b, 6c: Hole 7: Upstream chamber 8: Downstream side chamber, 8a: Water discharge port (discharge port) 20: Base, 21: Water sprinkling hole 22: Air suction tube, 22a: Air flow path 23: Flow plate, 24: Flow vane 25: Annular flow plate, 26, 27: Reverse flow Prevention plate

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】吐水ヘッドの内部に、ほぼ環状の上流側室
及び該上流側室との間に隔壁を形成して区画した下流側
室を形成し、前記下流側室の底部のほぼ中央に放出口を
開け、前記隔壁に前記下流側室の内部で給水を旋回させ
る流路軸線を持つ複数の孔をそれぞれの高さ位置を互い
に異ならせて配列し、前記放出口に一端が連通し他端を
吐水端とした泡沫化チャンバを備え、該泡沫化チャンバ
に前記放出口へ向けて空気吸引用の空気流路を備えてな
る泡沫吐水口。
1. A water discharge head is provided with a substantially annular upstream side chamber and a downstream side chamber defined by a partition wall formed between the upstream side chamber and the upstream side chamber, and a discharge port is opened substantially at the center of the bottom of the downstream side chamber. A plurality of holes having flow channel axes for swirling the water supply inside the downstream chamber are arranged in the partition wall at different height positions, and one end communicates with the discharge port and the other end serves as a water discharge end. A foam spout provided with the foaming chamber described above, and an air flow path for sucking air toward the discharge port in the foaming chamber.
JP30449289A 1989-11-21 1989-11-21 Foam spout Expired - Fee Related JPH0679684B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30449289A JPH0679684B2 (en) 1989-11-21 1989-11-21 Foam spout

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30449289A JPH0679684B2 (en) 1989-11-21 1989-11-21 Foam spout

Publications (2)

Publication Number Publication Date
JPH03165855A JPH03165855A (en) 1991-07-17
JPH0679684B2 true JPH0679684B2 (en) 1994-10-12

Family

ID=17933687

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30449289A Expired - Fee Related JPH0679684B2 (en) 1989-11-21 1989-11-21 Foam spout

Country Status (1)

Country Link
JP (1) JPH0679684B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL2412877T3 (en) * 2009-03-26 2019-07-31 Masaaki Takano Foamed-water generating plug
JP5556187B2 (en) * 2010-01-15 2014-07-23 Toto株式会社 Water discharge device
JP2011167675A (en) * 2010-02-22 2011-09-01 Nanoplanet Corp Device for generating whirling mist and method of generating whirling mist
CN103221618B (en) 2010-09-11 2015-05-20 高野雅彰 foam water generating plug
JP5854496B2 (en) * 2011-06-06 2016-02-09 株式会社k&kサービス Relief member and nozzle

Also Published As

Publication number Publication date
JPH03165855A (en) 1991-07-17

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