JPH0745017B2 - Foam spout - Google Patents
Foam spoutInfo
- Publication number
- JPH0745017B2 JPH0745017B2 JP1304491A JP30449189A JPH0745017B2 JP H0745017 B2 JPH0745017 B2 JP H0745017B2 JP 1304491 A JP1304491 A JP 1304491A JP 30449189 A JP30449189 A JP 30449189A JP H0745017 B2 JPH0745017 B2 JP H0745017B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- flow
- discharge port
- chamber
- outlet
- 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
Links
- 239000006260 foam Substances 0.000 title claims description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 161
- 238000005187 foaming Methods 0.000 claims description 32
- 230000002265 prevention Effects 0.000 claims description 28
- 238000004891 communication Methods 0.000 claims description 9
- 239000012530 fluid Substances 0.000 claims description 6
- 239000007921 spray Substances 0.000 description 25
- 238000005192 partition Methods 0.000 description 10
- 230000010349 pulsation Effects 0.000 description 6
- 230000001105 regulatory effect Effects 0.000 description 5
- 238000011144 upstream manufacturing Methods 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 230000002093 peripheral effect Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000004323 axial length Effects 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 230000002452 interceptive effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000008400 supply water Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Domestic Plumbing Installations (AREA)
- Nozzles (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.
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 described, for example, in Japanese Patent Publication No. 63-31621.
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. 9 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 51 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撹拌される
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 network 54 is fine, the water supply is vigorously agitated even when the water supply collides against it and flows away, further promoting foam formation.
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 one that promotes foaming by causing a water spray plate provided at the discharge end to collide with a flow having a high flow rate from a small hole of the pressure reducing plate and further stirring with the mixed air.
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, 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, it does not become foam or has no foam feeling. I will end up.
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。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. Therefore, if the flow passage area becomes small and the amount of water discharged 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、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 secure a flow rate without causing pressure loss and clogging of foreign matter, and to always obtain appropriate foaming.
本発明の泡沫吐水口は、以上の目的を達成するために、
流体の入口及び出口と、これらの入口と出口との間を連
通させる連通路と、該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
壁に対して流入軸が斜め方向流れとして供給する孔と、
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、該放出口
に連通すると共に前記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、前記出口側で外気に開放し前記放出
口側に向けてほぼ同軸上に形成した空気流路とを備えた
泡沫吐水口であって、前記空気流路の周りに突き出した
逆流防止板と、前記放出口の周りであって前記逆流防止
板よりも大きな範囲を占める環状の逆流防止板とを備
え、前記環状の逆流防止板の突き出し長さを前記放出口
から空気流路の逆流防止板までの距離よりも短くし、こ
れらの逆流防止板どうしの間の環状の隙間を前記放出口
からの放出水の通路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,
A fluid inlet and an outlet, a communication passage communicating between the inlet and the outlet, a swirl flow chamber arranged in the communication passage, and a fluid from the communication passage to an inner wall of the swirl flow chamber. A hole where the inflow shaft supplies as an oblique flow,
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 a space having a cross-sectional area larger than the opening area of the discharge port and communicating with the discharge port. A foam spout provided with a foaming chamber having an end thereof communicated with the outlet, and an air flow path formed on the outlet side to the outside air and formed substantially coaxially toward the outlet side. There is a backflow prevention plate protruding around the air flow path, and an annular backflow prevention plate around the discharge port and occupying a larger area than the backflow prevention plate, the annular backflow prevention plate The protrusion length of is shorter than the distance from the discharge port to the backflow prevention plate of the air flow path, and the annular gap between these backflow prevention plates is used as a passage for the water discharged from the discharge port. Characterize.
また、泡沫化チャンバ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。Moreover, if the inner wall of the foaming chamber is made into a minute uneven surface,
A pulsating flow or the like due to forced swirling in the swirling flow chamber can be interfered with, and a stable flow can be obtained.
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。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 swirling flow chamber is also spiral, 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 in a state of being easily scattered, and if the foaming chamber is opened to the atmosphere through an air hole 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、空気流路の周りの逆流防止板及び放出口周りの環
状の逆流防止板は、泡沫水の空気流路側及び放出口側へ
向かおうとする流れを阻止し、空気流路からの空気の吸
引及び放出口からの旋回流の放出のそれぞれが速やなな
流れとして維持される。Further, the backflow prevention plate around the air flow path and the annular backflow prevention plate around the discharge port prevent the flow of the foam water toward the air flow path side and the discharge port side, and prevent the air from the air flow path. Each of the suction and the discharge of the swirling flow from the discharge port is maintained as a rapid flow.
更に、泡沫化チャンバの内壁を微小な凹凸形状とするこ
とで、放出口からの放出水の波動等に干渉して流れを安
定させることが可能となる。Furthermore, by forming the inner wall of the foaming chamber into a minute uneven shape, it becomes possible to stabilize the flow by interfering with the wave motion of the water discharged from the discharge port.
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 divided into an upstream side chamber 7 and a downstream side chamber 8 by an annular wall 6 that connects the partition wall 3 and the upper end 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 integrally molded, and are assembled in the water discharge 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 discharge head 1, and has holes 6a at four positions as shown in FIG. These holes 6a are arranged so that the streamlines are tangential to the transverse section of the downstream chamber 8 inside the annular wall 6. On the other hand, the discharge port 3a opened to the bottom of the downstream side chamber 8 is located at the center of the downstream side chamber 8 and its inner diameter is significantly smaller than the inner diameter of the downstream side 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 is provided with an air suction structure for rectifying and discharging the foam water and foaming the water, and FIG. 3 (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
同軸上に形成し、その内部に空気流路22aを設けてい
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 (see FIG. 4).
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.
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、その高さは散水孔21の軸線長さの半分程度で
ある。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。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。In the base 20, as shown in FIG. 1, the axial length of the water sprinkling hole 21 is increased to some extent so that the passing foam water can be rectified. Then, a cross-shaped straightening plate 23 is incorporated inside each of the water spray holes 21, so that the turbulence of the flow of the foam water flowing through the water spray holes 21 is eliminated. Also,
On the upper surface of the base 20, as shown, six straightening vanes 24 radially extending from the air suction cylinder 22 are provided. These flow straightening vanes 24 penetrate between the adjacent water spray holes 21 and reach the edge of the base 20, and the height thereof is about half the axial length of the water spray holes 21. Further, on the upper surface of the base 20, there is provided a circular annular current plate 25 which is coaxial with the base 20 and passes through the center of the water spray hole 21. This annular flow straightening plate 25 passes above the intersection of the cross-shaped flow straightening plates 23 provided in the water spray holes 21 as shown in FIG. 1, and its height is about twice that of the flow straightening vanes 24.
空気吸入筒22は、ベース20の上面から径を小さくした円
錐台状に形成され、その外周に円錐面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
等径の筒状に形成され、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 cylinder 22 is formed in a truncated cone shape with a diameter reduced from the upper surface of the base 20, and the conical surface 22b is used as a guide for the foam water on the outer circumference thereof. Further, the conical surface 22b is formed in a cylindrical shape having an equal diameter from the upper end portion, and the upper end thereof faces the discharge port 3a of the swirl flow chamber 4. A backflow prevention plate 26 is provided at a position higher than the upper half of the air suction cylinder 22. This backflow prevention plate 26 is a disc shape and is attached in a horizontal posture,
The outer diameter thereof 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 on the lower surface of the partition wall 3 and is coaxial with the foaming chamber 5.
Are integrated. The inner diameter of the backflow prevention plate 27 is equal to or larger than that of the backflow prevention plate 26 below, and the ring-shaped straightening plate 25
Is almost equal to.
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(b)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本のステー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、ベー
ス20の上面に設ける環状整流板25は、第5図に示すよう
に各散水孔21の間に頂角を持つ六角形状としてもよい。The annular backflow prevention plate 27 may be provided on the water spray plate 2 side as shown in FIG. 3B, instead of being provided integrally with the partition wall 3. In this case, the backflow prevention plate 27 is the air suction cylinder.
It is integrated with four stays 27a at the upper end of 22 and has a structure that does not impede the flow of water and air. Further, the annular flow regulating plate 25 provided on the upper surface of the base 20 may have a hexagonal shape having an apex angle between the water spray holes 21 as shown in FIG.
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。この雌ネジ5aは放出口3aから水
膜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。Further, a female screw 5a is formed as an interference surface on the inner peripheral wall of the foaming chamber 5. The female screw 5a has a function of attenuating the pulsation when the water that flows in the form of a water film from the discharge port 3a interferes with the pulsation when the water is pulsating. It should be noted that the reason why the female screw 5a is carved as the interference surface is for one reason that it is easy to process. Instead of this, the inner peripheral wall of the foaming chamber 5 may be provided with 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成しながら
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
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。Here, when water is sent from the spout 50, the water flows from the upstream chamber 7 through the hole 6a of the annular wall 6 into the downstream chamber 8.
At this time, the axis of the hole 6a is oriented in the tangential direction with respect to the downstream chamber 8 having a circular cross section, so that the water becomes a swirling flow in the downstream chamber 8. That is, as shown in FIG. 2, water flows along the inner wall from the outer peripheral portion of the downstream side chamber 8 and swirls in the downstream side chamber 8 while the water from the four holes 6a merges to form a vortex. start. 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 stays in the downstream chamber 8 occurs and the internal pressure rises to some extent. Therefore, in the inside of the downstream chamber 8, the flow energy of the water itself increases, and the centrifugal force due to the swirling flow acts. For this reason, the water flowing down from the discharge port 3a has the behavior of spreading outward under the influence of the centrifugal force, and is discharged as a conical water film F 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が泡沫化チャンバ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 of the foaming chamber 5, and the air is mixed with the crushed water to foam the water supply. Then, the foamed water flows into the water spray holes 21, and the straightening vanes 23
The flow is regulated by and is discharged.
以上の流れにおいて、泡沫化チャンバ5の上部側に設け
た逆流防止板26,27は、放出口3aからの円錐状の水膜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流へ通
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22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 plates 26, 27 provided on the upper side of the foaming chamber 5 are provided with the conical water film F from the discharge port 3a.
And, these water and air are allowed to pass immediately downstream without becoming a barrier against the suction air from the upper end of the air suction cylinder 22. The backflow prevention plates 26 and 27 serve as barriers to prevent the backflow of the foamed water in which the water film F hits the female screw 5a and is mixed with air, to the discharge port 3a and the upper end side of the air suction cylinder 22. It Therefore, the upper end of the air suction cylinder 22 is not covered with foamed water or water supply from the discharge port 3a, and air is smoothly sucked. Therefore, a sufficient amount of sucked air is secured to promote foaming, and the degree to which the feed water directly mixes with the inflowing air is reduced, so that the air suction sound and the water supply sound 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バ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般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5a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に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 screw 5a of the foaming chamber 5, and the unevenness of the surface thereof interferes with the pulsation of the flow to damp it. That is, the feed water is forcibly swirled in the swirling flow chamber 4 to increase the flow energy and then flows into the water film F from the discharge port 3a. Therefore, compared to general pipe flow due to pulsation and inertia of the flow itself,
Pressure fluctuations are likely to occur. On the other hand, if a minute uneven surface such as the female screw 5a is provided so as to be different in the direction in which the flow is reflected, pulsation energy can be interfered and the flow can be stabilized. Therefore, the foam water mixed with air does not flow intermittently and is not accompanied by strength, and stable water discharge with 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
も無くすることができる。Further, since the conical surface 22b of the air suction cylinder 22 guides the foam water to the water spray hole 21 while gently guiding the foam water, cavitation or separation from the flow path wall is prevented against the flow of the gas-liquid two-layer flow containing bubbles. It can be delivered without causing it. For this reason,
Generation of water supply noise at the time of water discharge is suppressed, and even if the flow rate is increased, the usage environment is not affected. Further, when the flow rate is small, the foam water is discharged without filling the inside of the foam formation chamber 5. In this case, the flow velocity of the foamed water also decreases and the streamline is apt to be disturbed, but the foamed water quickly flows off to each water spray hole 21 along the conical surface 22b. Therefore, even when the flow rate is small, it is possible to prevent the staying in the foaming chamber 5 by positively guiding the foam water, and by evenly feeding the foam water into each water spray hole 21, there is no fluctuation in the water discharge form. be able to.
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、
ベース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
21から一様な泡沫水が得られる。The foamed water having a stable flow as described above is reflected from the female screw 5a toward each water spray hole 21 as shown by the arrow in FIG. 1, and this behavior becomes remarkable especially when the flow rate increases. At this time,
The annular flow regulating plate 25 on the base 20 prevents the foam water from concentrating on the center side. That is, the ring-shaped rectifying plate 25 acts as a baffle to prevent the inflow to the center side, so that the foam water is not discharged only from the center side of the water spray holes 21, and the water spray holes are provided.
A uniform foamy water is obtained from 21.
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、より一層吐水状態が安定す
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、各散水
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。Further, the foamed water, whose concentration on the center side is suppressed and which is uniformized in the radial direction, is further stabilized in the water discharge state by the flow regulating vanes 24 that are radially arranged and partition between the water spray holes 21. That is, the straightening vanes 24 arranged radially reduce the swirling force of the water supply by the swirling flow chamber 4 and prevent the flows toward the water spray holes 21 from interfering with each other. For this reason, the dynamic water discharge is stabilized by the reduction of the turning force, and at the same time, only the amount of the foam water divided by the flow control vanes 24 is discharged in a stable state without being affected by the external environment.
また、吐出される直前では、泡沫水は散水孔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21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 foam water is straightened by the cross-shaped straightening plate 23 when passing through the water spray holes 21. rectifier
Since 23 divides the flow path in the sprinkling hole 21 into four, the foamed water is divided into flows while passing through the straightening vane 23 and is rectified so as to be parallel to each other, and spreads outward or to the center. You can get water spout without concentration.
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. Even if the flow rate is small, the water supply is sufficiently foamed, and
5. Since the foam water is stabilized by the flow straightening vanes 24 and passed through the flow straightening plate 23, the optimum foam water discharge can be obtained without the turbulence of the flow.
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 cross-sectional view of a main part showing an example in which the foam spout according to the present invention is a hand shower type water faucet, and FIG. 7 is a perspective view showing a state of installation in a kitchen. The same members as those shown in FIGS. 1 to 5 are designated by common reference numerals, and detailed description 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、その内部に形成した流路30a
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)を連結して湯水混
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 discharge head 1 is integrated with the shower body 30 for use as a hand shower, and has a flow passage 30a formed therein.
Is in communication with. The shower main body 30 is supported by a holder 33 fixed to a counter 32 of a cabinet 31 so that it can be freely taken in and out, and a hose (not shown) is connected to the base end of the shower main body 30 to supply water or hot water from a hot and cold water mixing tap or an electric water heater. To do. And
The holder 33 allows the shower main body 30 including the hose to be pulled out, and the holder 33 can be held by hand to wash the container and the like.
A hand shower that is equipped with such a hose and can be pulled out is generally used conventionally.
また、上流側室7はシャワー本体30に組み込んだときに
環状に形成され、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 side chamber 7 is formed in an annular shape when incorporated in the shower body 30, the annular backflow prevention plate 27 is integrally provided on the partition wall 3 side, and the other structures are almost the same as those 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
とが並べて形成され、本発明の泡沫吐水口を備えた吐水
ヘッド1は浅いシンク34側に設置されている。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。On the other hand, the counter 32 has a shallow sink 34 and a deep sink 35.
Is formed side by side, and the water discharge head 1 having the foam water discharge port of the present invention is installed on the shallow sink 34 side. In addition, on the deep sink 35 side, a normal single lever type hot and cold water mixing tap
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、図示のようにまた
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。The foam spouted water from the shower main body 30 provided with the water spouting head 1 becomes stable shower sprinkling without flow disturbance after being foamed as described above. For this reason,
Even if the sink 34 is shallow, the foam water is separated into a plurality of streamlines and discharged into the shower, so that the degree of water scattering is reduced and the obstacle of water splash can be eliminated. In particular, as shown in the drawing, the plate 34a is slid again by using the stepped portion 34b provided in the shallow sink 34, and even if water is discharged onto the cutting plate 34a, the water splash does not increase, so that the floor is wet. Nothing.
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 the shower water is sprayed without disturbing the flow after foaming, not only the water splash when hitting the bottom of the sink but also the water splash when washing the container etc. , Further improves 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。FIG. 8 is a qualitative graph comparing the characteristics with the conventional structure. The characteristics when the structure of FIG. 6 is used are shown by solid lines,
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(b)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 water supply amount and the vertical axis shows the pressure loss represented by the value of the pressure drop in the internal flow path, and the pressure loss is reduced as compared with the conventional structure.
Then, due to this decrease in pressure loss, the foaming chamber 5
Since the flow velocity of the water flowing in is maintained, the internal pressure drop is larger than that of the conventional structure as shown in FIG. 8 (b). Since this internal pressure drop rapidly increases from a small flow rate region, air mixing is promoted even when the flow rate is small, and proper foaming becomes possible. It should be noted that FIG. 8 (c) shows the amount of sucked air, and the amount of sucked air is larger than that of the conventional structure because the internal pressure drop is large.
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, the pressure loss can be reduced, and the air can be mixed in quickly, so that spouting with a sufficient degree of foaming can be obtained even in the low flow rate range where foaming is difficult.
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 described above, in the present invention, the centrifugal force is generated in the flow by swirling the feed water, and the centrifugal force is used to feed the centrifugal force into the foam chamber as a conical water film flow, and the internal pressure generated at this time is generated. The air is mixed due to the decrease of. 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.
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。In addition, the reduction of the pressure loss is, in other words, the speedup of the internal flow, and the internal negative pressure based on this is increased. For this reason, the air suction rate from the air flow path also becomes high, water discharge having a sufficient degree of foaming can be obtained even at a low flow rate value, and it can be used in a wide range of fields.
空気流路の周り及び放出口の周りにそれぞれ逆流防止板
を設けることによって、空気流路側及び放出口側への泡
沫水の流れを阻止でき、空気流路からの空気の吸引及び
放出口からの旋回流の放出のそれぞれが速やかに行わ
れ、より一層効果的に泡沫化が促進される。By providing backflow prevention plates around the air flow path and around the discharge port, respectively, the flow of foam water to the air flow path side and the discharge port side can be blocked, and suction and discharge of air from the air flow path Each of the swirling flows is discharged promptly, and foam formation is further effectively promoted.
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, if minute irregularities are provided on the inner wall of the foaming chamber, it is possible to have an interference effect on the waves of the feed water from the discharge port, and dampen the pulsations and the like that occur when a swirling flow is forced. To stabilize the flow.
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図は環状壁の内部での旋回流の発生を示す第
1図のI−I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、5a:雌ネジ 6:環状壁、6a:孔 7:上流側室、8:下流側室 20:ベース、21:散水孔 22:空気吸入筒、22a:空気流路 22b:円錐面 23:整流板、24:整流羽根 25:環状整流板、26:逆流防止板 27:逆流防止板、27a:ステー 30:シャワー本体、30a:流路 31:キャビネット、32:カウンター 33:ホルダFIG. 1 is a longitudinal sectional view of an essential 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. 1 showing the generation of a swirling flow inside an annular wall. 3 (a) is a perspective view of the water spray plate, FIG. 3 (b) is a perspective view of the water spray plate when an annular backflow prevention plate is integrated at the upper end, and FIG. 4 is a bottom view of the water discharge head. FIG. 5 is a cross-sectional view of a water discharge head showing another rectifying plate structure, FIG. 6 is a vertical cross-sectional view showing an example in which the water discharge head is incorporated in the shower body, and FIG. 7 is a perspective view showing the installation on the counter of the kitchen. FIG. 8 is a graph showing a characteristic comparison with a conventional structure, and FIG. 9 is a schematic diagram of a conventional example. 1: Water discharge head, 2: Water spray plate 3: Partition wall, 3a: Discharge port 4: Swirling flow chamber 5: Foaming chamber, 5a: Female screw 6: Annular wall, 6a: Hole 7: Upstream chamber, 8: Downstream chamber 20 : Base, 21: Sprinkler hole 22: Air suction cylinder, 22a: Air flow path 22b: Conical surface 23: Straightening plate, 24: Straightening vane 25: Annular straightening plate, 26: Backflow prevention plate 27: Backflow prevention plate, 27a: Stay 30: Shower body, 30a: Flow path 31: Cabinet, 32: Counter 33: Holder
Claims (2)
口との間を連通させる連通路と、該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
チャンバの内壁に対して流入軸が斜め方向流れとして供
給する孔と、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、該放出口に連通すると共に前記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、前記出口側で外気に開
放し前記放出口側に向けてほぼ同軸上に形成した空気流
路とを備えた泡沫吐水口であって、 前記空気流路の周りに突き出した逆流防止板と、 前記放出口の周りであって前記逆流防止板よりも大きな
範囲を占める環状の逆流防止板とを備え、 前記環状の逆流防止板の突き出し長さを前記放出口から
空気流路の逆流防止板までの距離よりも短くし、これら
の逆流防止板どうしの間の環状の隙間を前記放出口から
の放出水の通路としたことを特徴とする泡沫吐水口。1. A fluid inlet and an outlet, a communication passage communicating between the inlet and the outlet, a swirl flow chamber arranged in the communication passage, and a fluid from the communication passage in the swirl flow chamber. A hole in which the inflow axis supplies as an oblique flow to the inner wall of the outlet, an outlet near the center of the swirling flow of the fluid in the swirl chamber and facing the communication path to the outlet, and the outlet. And a foaming chamber having a space having a cross-sectional area larger than the opening area of the discharge port and having its end communicating with the outlet, and open to the outside air on the outlet side toward the discharge port side. A foam discharge port having an air flow path formed substantially coaxially, the backflow prevention plate protruding around the air flow path, and a range larger than the backflow prevention plate around the discharge port. With an annular backflow prevention plate occupying, The protruding length of the annular backflow prevention plate is made shorter than the distance from the discharge port to the backflow prevention plate of the air flow path, and the annular gap between these backflow prevention plates is used to discharge water from the discharge port. The foam spout is characterized by being used as a passageway.
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。2. The foam spout according to claim 1, wherein the inner wall of the foaming chamber is an uneven surface which receives water supplied from the discharge port and interferes with the flow.
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 |
| 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 |
| 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 |
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 JPH03161063A (en) | 1991-07-11 |
| JPH0745017B2 true 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) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6071114B2 (en) * | 2013-07-30 | 2017-02-01 | Toto株式会社 | Shower head device |
| JP6032440B2 (en) * | 2014-03-31 | 2016-11-30 | Toto株式会社 | Shower equipment |
| JP6032441B2 (en) * | 2014-03-31 | 2016-11-30 | Toto株式会社 | Shower equipment |
| JP6032442B2 (en) * | 2014-03-31 | 2016-11-30 | Toto株式会社 | Shower equipment |
| JP7053047B2 (en) * | 2019-07-25 | 2022-04-12 | 株式会社サイエンス | Bubble generator |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS627725Y2 (en) * | 1979-03-28 | 1987-02-23 |
-
1989
- 1989-11-21 JP JP1304491A patent/JPH0745017B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03161063A (en) | 1991-07-11 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |