JPH0363333A - Foam spout - Google Patents
Foam spoutInfo
- Publication number
- JPH0363333A JPH0363333A JP1199864A JP19986489A JPH0363333A JP H0363333 A JPH0363333 A JP H0363333A JP 1199864 A JP1199864 A JP 1199864A JP 19986489 A JP19986489 A JP 19986489A JP H0363333 A JPH0363333 A JP H0363333A
- Authority
- JP
- Japan
- Prior art keywords
- water
- chamber
- air
- foaming
- flow
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/40—Protecting water resources
- Y02A20/411—Water saving techniques at user level
Landscapes
- Domestic Plumbing Installations (AREA)
Abstract
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.
給水前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 to reduce the sound of water falling into a sink or the like, and to eliminate splashing. The most commonly used one is, for example, the one described in Japanese Patent Publication No. 31621/1983.
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510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
整流網54が配置されている。FIG. 7 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 510 downstream of this pressure reducing plate 52 to introduce outside air into the water supply.
3, 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 speed 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.
ところが、スパウト50からの給水は減圧板52の小孔
52を通過するため、流れの圧力損失がかなり大きい。However, since the water supplied from the spout 50 passes through the small holes 52 of the pressure reducing plate 52, the pressure loss of the flow is quite large.
このため、水栓の弁開度を成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。For this reason, an 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, it becomes inconvenient to use and cannot produce sufficient foam.
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 rectifying net 54 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、給水の圧力損失及び流路の
閉塞等の問題が避けられなかった。In this way, the conventional foam spout uses a pressure reducing plate to increase the speed of the water supply, and based on this, reduces the pressure in the internal flow path to suck in outside air, so there are problems such as pressure loss of the water supply and blockage of the flow path. problem was unavoidable.
更に、スパウト50の先端に設けた吐水キ+ツブ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1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。Further, in the case of foaming water spouted from the water spouting knob 51 provided at the tip of the spout 50, the size of the water spouted water is determined by the water spouting cap 51. For this reason, if the water spouting cap 51 has the same diameter as the spout 50, the spread will be the same as when the supplied water is directly spouted before foaming. On the other hand, since the foam water discharge softens the water supply, it can be suitably used for showers, etc. However, if the water spouting range is small, it may be suitable for a faucet, but the water spouting range is too small for a shower.
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。For this reason, the water discharge cap 51 may be made larger, but the pressure loss also increases accordingly, resulting in 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 aims to ensure a flow rate without causing pressure loss or clogging with foreign objects, and to always obtain appropriate foaming, and to expand the range of water spout so that it can be used appropriately for showers, etc. The purpose is to
本発明の泡沫吐水口は、以上の目的を遠戚するため、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ずる泡沫化チャンバとを備え、該
泡沫化チャンバは、前記放出口からの水の流入によって
外部から空気を吸引して泡沫吐水可能としたことを特徴
とする。In order to achieve the above object, the foam spout of the present invention includes a swirling flow chamber that communicates with a water supply source and swirls the flow, and a discharge port that is opened approximately in the center of the swirling flow chamber. The foaming chamber is characterized in that the foaming chamber is capable of discharging foamy water by sucking air from the outside by the inflow of water from the discharge port.
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 film from the outlet and forming bubbles. 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 an air hole, 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.
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。Moreover, since the water from the swirling flow chamber spreads into a conical shape due to centrifugal force, if the water is spouted in this spread state, the final water spouting area will also be expanded.
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。In the figure, a water discharging head 1 for foaming is attached to the tip of a spout 50. The water discharging head 1 is a second
As shown in the figure, it has a circular cross section, and a connecting tube 1a to a spout 50 protrudes in the radial direction from the upper end.
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。A streamline extending substantially horizontally from the connecting tube 1a curves downward from the center of the water discharging head 1 at a right angle, forming an internal flow path through which water is discharged from the rectifying cap 2 provided at the lower end.
吐水ヘッドl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 inside of the water discharging head l 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 outer swirling flow chamber 7 and an inner swirling flow chamber 8 by an annular wall 6 that connects the partition wall 3 and the inner wall at the upper end of the water discharging head 1 . The outer swirling flow chamber 7 communicates with the connecting tube 1a, and the inner swirling flow chamber 8 communicates with the foaming chamber 5 through a discharge port 3a formed in the partition wall 3. The partition wall 3 and the annular wall 6 are integrally molded, and the assembly structure is such that the partition wall 3 and the annular wall 6 are fixed in the water discharging head 1.
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411所に孔6aを開けている。これ
らの孔6aは、環状9!6の内部の内旋回流チャンバ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 flow path cross section of the water discharging head 1, and has holes 6a at 411 locations as shown in FIG. These holes 6a form an internal swirling flow chamber 8 inside the annular shape 9!6.
The position is such that the streamlines are in the tangential direction with respect to the cross section. On the other hand, the outlet 3a open to the bottom of the inner swirling flow chamber 8 is located at the center of the inner swirling flow chamber 8, and its inner diameter is much smaller than the inner diameter of the inner swirling 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から噴き出さ
れた給水が空気孔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。Furthermore, an air hole 5a is opened in the peripheral wall of the foaming chamber 5, through which air is sucked to foam the supplied water. The inside of the foaming chamber 5 has a height and an inner diameter such that the supplied water spouted 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エの
下端に取り付(すられ、その間に泡沫化促進のための1
19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 rectifying cap 2 is attached to the lower end of the water spouting head by screws 2a, and a
There are 19. The rectifying cap 2 includes a rectifying plate 2b for quickly discharging foamy 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!!6の孔6&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に対してタンジェンシャル方
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5a’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のそれよりも太きければ
、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。Here, when water is sent from the spout 50, it flows from the outer swirling flow chamber 7 into an annular shape! ! Water flows into the internal swirling flow chamber 8 through the holes 6& of 6. At this time, since the axis of the hole 6a is oriented in the tangential direction with respect to the inner swirling flow chamber 8 having a circular cross section, water forms a swirling flow within the inner swirling flow chamber 8. That is, as shown in FIG. 3, water flows from the outer periphery of the inner swirling flow chamber 8 along the inner wall, and the water from the four holes 5a' joins to form a vortex while flowing into the inner swirling flow chamber 8. Start turning inside. At this time, hole 6a
If the entire flow path area is larger than that of the discharge port 3a, water will remain in the internal swirling flow chamber 8, and the internal pressure will increase somewhat. Therefore, the inner swirling flow chamber 8
Inside, the flow energy of the water itself increases, and centrifugal force acts due to the swirling flow. Therefore, the water flowing down from the discharge port 3a spreads outward under the influence of centrifugal force, and is discharged as a conical water film F as shown by the broken line in the figure.
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12!9に衝き当たる。In other words, the water does not flow down from the discharge port 3a as a cylindrical channel cross section, but is blown away 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. The thickness of the water film F becomes thinner as it moves away from the discharge port 3a, and it impinges on the lower end 12!9 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 approximately at the center of the foaming chamber 5, and since water with centrifugal force flows out at a high flow rate, the internal pressure in the space outside the conical water film F decreases. For this reason,
Air is sucked in through the air holes 5a, and the air is mixed with the water that hits the net 9 and breaks up, thereby turning the supplied water into foam.
辺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 that has become foamy as above is rectified while passing through the rectifying plate 2b of the rectifying cap 2, and is then flowed into the water discharging head 1.
is discharged from.
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1
0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の下端内周は複床がりの断面を持
つ傾斜部ioaとして形成され、ガイド11はこの傾斜
部tOaに沿うテーパ面11aを備えている。そして、
これらの傾斜110 a及びテーパ面11aとの間の隙
間が、複床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, the discharge port 3a has a cylindrical discharge cylinder 1 facing downward.
0 is formed, and a guide 11 is attached to the inner periphery of the lower end. The inner periphery of the lower end of the discharge tube 10 is formed as an inclined part ioa having a double-bedded cross section, and the guide 11 is provided with a tapered surface 11a along this inclined part tOa. and,
The gap between the slope 110a and the tapered surface 11a has a double-bedded truncated conical cross section, 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 outlet 3a can be adopted instead of that shown in FIG. In this case, in addition to the centrifugal force applied to the flow in the swirling flow chamber 4, the guide 11 guides the streamlines of the water in a shape that spreads toward the end, so that the water film F is stably formed. Further, even if the structure is such that water is directly fed without the swirling flow chamber 4, the water film F can be formed because the effect of expanding the streamlines of the water remains the same.
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°C飛散させる構
造としたものである。Furthermore, FIG. 5 shows that instead of forming a water film, a foaming chamber 5
The structure is such that the water is violently merged inside the tank to disperse °C.
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12
a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 tube 12 is formed below the discharge port 3a as in the case of FIG. 4, and a plurality of holes 12 are provided at the lower end thereof.
A is opened so that all of the openings are oriented toward the axis of the discharge port 3a. Water from the discharge port 3a is discharged in the axial direction of the hole 12a, and flows so as to merge on the axis of the discharge port 3. Therefore, after merging, the water scatters in the foaming chamber 5 as shown by the broken line in the figure, and it becomes easier to foam when it hits 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”J6の上端に天板6bを
設けて外筒回流チャンバ7とは分離した部屋として内旋
回流チャンバ8を形威し天板6bに孔6Cを開けた点が
異なっている。FIG. 6 shows an example of a structure that allows water to be scattered within the foaming chamber 5 with a small pressure loss. this is,
In contrast to the structure shown in Fig. 1, a top plate 6b is provided at the upper end of the annular J6, an inner swirling flow chamber 8 is formed as a room separate from the outer cylinder circulation chamber 7, and a hole 6C is bored in the top plate 6b. The points are different.
水は孔5a、 5cから内旋回流チャンバ8に流れ込み
、このときにはクンジェンンヤル方向の孔6 a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 internal swirling flow chamber 8 through the holes 5a and 5c, and at this time, the water from the hole 6a in the Kunjennyar direction forms a swirling flow. Since water also flows in from the hole 6C of the top plate 6b, a flow that tries to push it out toward the discharge port 3a against the centrifugal force is also generated. For this reason, in the structure shown in Fig. 1, the water from the outlet 3a was released as a water film, but the water flux is now torn off by the pushing force of the water from the hole 6C, as indicated by the broken line. As shown, the water is discharged from the discharge port 3a as scattered water. Further, as shown in FIGS. 4 and 5, the water flow path is not greatly constricted, and the pressure loss is reduced compared to 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、i
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 scattered water as shown in FIGS. 4 to 6 is sent into the foaming chamber 5 from the discharge port 3a. In addition, since the flow velocity increases in either case, the air hole 5a
Air is also quickly sucked out. Therefore, i
Air is mixed into the water that collides with the inner wall of the foaming chamber 9 or the foaming chamber 5, and a good foamy water discharge is 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。Furthermore, since the water discharged from the swirling flow chamber 4 spreads in a conical shape, the range of water discharged into the foaming chamber 5 also increases. Therefore, by increasing the diameter of the foaming chamber 5, the range of water that can be finally spouted can be expanded even if the spout 50 is small.
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。Therefore, even if the maximum flow rate from the spout 50 is determined, water can be spouted more slowly over a larger water spouting range than in the conventional example. As a result, in addition to softening the water supply by turning it into foam, it is now possible to discharge water with a large diameter.
It can also be suitably used for showers and other purposes.
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。In addition to the embodiments, various structures for swirling the flow in the swirling flow chamber 4 and foaming the flow in the foaming chamber 5 are conceivable.
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
、導翼の間の流路を孔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l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。For example, instead of the annular wall 6 provided in the swirling flow chamber 4, it is possible to form what corresponds to the annular wall 6 by a large number of rows of blades, and use the flow path between the guiding blades as the hole 6a, or
For example, a slit is provided in the slit and used as a flow path. In any of these, in order to transform the water supply flowing into the swirling flow chamber 4 into a whirlpool, the basic configuration is to use blades or slits in the tangential direction to feed the water in the direction of swirling. In addition, instead of the air hole 5a provided in the foaming chamber 5, an air cylinder may be raised upward from the center of the rectifying cap 2 and the upper end thereof may be used as an air suction part, or conversely, a swirling flow may be caused from the upper end of the water discharging head l. An air cylinder may be provided so as to pass through the discharge port 3 through the chamber, and air may be fed from the lower end of the air cylinder.
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 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 Therefore, compared to the conventional case where a pressure reducing plate with a large number of small holes is used, pressure loss is reduced, a flow rate is secured, and water discharge failures due to adhesion of foreign matter or scale are 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。Furthermore, the centrifugal force generated by the swirling flow in the swirling flow chamber can spread the discharged water in a conical shape, and the range of the discharged water turned into foam in the foaming chamber can be expanded. Therefore, in addition to softening by foaming, water can be spouted slowly, making it suitable for use in showers, etc.
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−1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腹
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
飛散水を懲戒する例の断面図、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:外筒回流チャンバ
8:内筒回流チャンバ
9:網
10:放出筒
ll;ガイド
12:放出筒
10a:傾斜部
11a:テーバ面
12a:孔Fig. 1 is a vertical cross-sectional view of essential parts of a foam spout showing an embodiment of the present invention, Fig. 2 is a cross-sectional view taken along the line I-1 in Fig. 1, and Fig. 3 (
a) is a vertical cross-sectional view showing the generation of swirling flow inside the annular wall;
FIG. 3(b) is a cross-sectional view, FIG. 4 is a cross-sectional view of an example of forming a water belly using a guide, FIG. 5 is a cross-sectional view of an example of merging water to create splash water, and FIG. The figure is a cross-sectional view of an example in which an annular wall is used to suppress splashed water, and FIG. 7 is a cross-sectional view of a conventional foam spout. 1: Water discharge head 1a: Connection cylinder 2: Rectifying cap 2a: Screw 2b: Rectifying plate 3: Partition wall 3a: Discharge port 4: Swirling flow chamber 5: Foaming chamber 5a: Air hole 6: Annular wall 6a: Hole 6b: Ceiling Plate 6c: Hole 7: Outer cylinder recirculation chamber 8: Inner cylinder recirculation chamber 9: Net 10: Discharge cylinder ll; Guide 12: Discharge cylinder 10a: Inclined part 11a: Taber surface 12a: Hole
Claims (1)
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を備
え、該泡沫化チャンバは、前記放出口からの水の流入に
よって外部から空気を吸引して泡沫吐水可能としたこと
を特徴とする泡沫吐水口。1. A swirling flow chamber that communicates with a water supply source and swirls the flow, and a foaming chamber that communicates with the swirling flow chamber through a discharge port opened approximately in the center of the swirling flow chamber, the foaming chamber comprising: A foam spout, characterized in that air is sucked in from the outside by the inflow of water from the discharge port, and foam water can be spouted.
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 true JPH0363333A (en) | 1991-03-19 |
| JPH0718180B2 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) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3837744B1 (en) * | 2005-08-25 | 2006-10-25 | 東陶機器株式会社 | shower head |
-
1989
- 1989-07-31 JP JP1199864A patent/JPH0718180B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0718180B2 (en) | 1995-03-01 |
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