JPH01258795A - Method and device for cleaning and circulating hot water of bath tub - Google Patents

Method and device for cleaning and circulating hot water of bath tub

Info

Publication number
JPH01258795A
JPH01258795A JP8440688A JP8440688A JPH01258795A JP H01258795 A JPH01258795 A JP H01258795A JP 8440688 A JP8440688 A JP 8440688A JP 8440688 A JP8440688 A JP 8440688A JP H01258795 A JPH01258795 A JP H01258795A
Authority
JP
Japan
Prior art keywords
hot water
ozone
bathtub
mixer
filtration
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP8440688A
Other languages
Japanese (ja)
Other versions
JPH0376196B2 (en
Inventor
Keisuke Kounou
鴻農 奎介
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.)
NIPPON HOME PROD KK
Original Assignee
NIPPON HOME PROD KK
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 NIPPON HOME PROD KK filed Critical NIPPON HOME PROD KK
Priority to JP8440688A priority Critical patent/JPH01258795A/en
Publication of JPH01258795A publication Critical patent/JPH01258795A/en
Publication of JPH0376196B2 publication Critical patent/JPH0376196B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To accelerate the functions of filter media having the function to accelerate the reaction of ozone and malodorous components and to activate the aerobic microorganisms near the filter media by injecting and mixing the ozone to and with hot water on the primary side of a filter device of the final stage at the time of injecting and mixing the ozone to and with the hot water. CONSTITUTION:A hot water circulating system consisting of a hot water inflow pipe system 6 for injecting the hot water in a bath tub 1 to the filter device 3 for executing the filter action of the final stage among filter means, a hot water outflow pipe system 12 and a circulating pump 9 is provided. Further, an ozone mixer 16 for injecting the ozone generated in an ozonizer 14 to the above-mentioned hot water circulating system is disposed. The ozone mixer 16 is disposed to the hot water inflow pipe system 6 corresponding to the primary side of the filter device 3 of the final stag based on the position of said device and a steam separator 17 is provided to the down stream position of the ozone mixer 16. As a result, the function of the filter media having the function to accelerate the reaction of the ozone and the malodorous component is accelerated and the aerobic microorganisms near the filter media are activated, by which the org. matter is decomposed away.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は浴槽温水の清浄循環方法及びその装置に係わり
、更に詳しくは循環浴槽温水中にオゾンを注入、混合す
るようにした技術の改良に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method and apparatus for purifying hot water in a bathtub, and more particularly, to an improvement in technology for injecting and mixing ozone into circulating hot water in a bathtub. .

[従来の技術] 周知の通り生活の高度化、多様化に伴ない入浴に関する
多種多様な工夫が施され、その−環として浴槽の温水を
清浄化したり、温水中の臭気街脱臭したり、あるいは温
水中の身体健康維持に不適当な菌類を殺菌、除菌したり
する手段が実用されている。即ち、通常、浴槽温水の清
浄又はクリーン化手段、あるいは脱臭、除菌化手段と称
されるもので、この装置は少なくとも、ろ過手段と、」
二足ろ過手段の内最終段のろ過作用を実施する為のろ過
装置に浴槽中の温水を流入せしめる為の温水流入管系と
、1−記ろ過装置から温水を浴槽中に環流せしめる為の
温水流出管系と、循環ポンプを有し、而も1記温水循環
系にオゾン発生器で生じたオゾンを注入、混合する為の
オゾン混合器を有している。上記に於いてろ過手段は単
数の場合の他、−次、二次と多段複数に配されている場
合もあり、且つろ過フィルターを用いたもの、活性炭を
用いたもの、バイオシュタイン(麦飯石)などの活性石
)を用いたもの、セラミックスを用いたもの1種々あり
、加えて」二足循環系に遠赤外線セラミックヒータを配
し循環温水を一定の温度、例えば42℃程度に保温する
ようにしたものもある。
[Prior Art] As is well known, as lifestyles have become more sophisticated and diversified, a wide variety of improvements have been made to bathing, such as purifying hot water in bathtubs, deodorizing hot water, and Means for sterilizing and sterilizing fungi that are unsuitable for maintaining physical health in warm water are in practical use. That is, it is usually referred to as a bathtub hot water purification or cleansing means, or a deodorizing and sterilizing means, and this device includes at least a filtration means.
A hot water inflow pipe system for causing hot water in the bathtub to flow into the filtration device for performing the final stage filtration action of the two-leg filtration means, and 1- hot water for circulating hot water from the filtration device into the bathtub. It has an outflow pipe system and a circulation pump, and also has an ozone mixer for injecting and mixing ozone generated by the ozone generator into the hot water circulation system. In the above, the filtration means is not only singular, but also may be arranged in multiple stages such as -order, secondary, etc. In addition, there are cases where the filtration means is arranged in multiple stages such as -order, secondary, etc.; There are various types, including activated stones (such as activated stones) and ceramics.In addition, a far-infrared ceramic heater is placed in the bipedal circulation system to keep the circulating hot water at a constant temperature, for example around 42℃. Some did.

所で、この温水循環清浄化装置の具体的な従来技術をみ
てみると、従来はオゾン発生器で生じたオゾンを注入、
混合する為のオゾン混合器を、上記ろ過装置の二次側か
ら延び浴槽の流出端に接続される流出管系、特に浴槽の
流出端に近接した位置の流出管系に配設している。
By the way, if we look at the specific conventional technology of this hot water circulation purification device, we can see that in the past, ozone generated by an ozone generator was injected,
An ozone mixer for mixing is arranged in an outflow pipe system extending from the secondary side of the filtration device and connected to the outflow end of the bathtub, particularly in an outflow pipe system located close to the outflow end of the bathtub.

[発明が解決しようとする課題] 上記従来技術は、ト記単又は複数のろ過装置そのものに
よるろ過機俺に着目した場合その発揮によりそれなりに
、浴槽温水中に混入せる汚れや油分等を除去し温水を清
浄化し、且つろ過媒体としてフィルター及び活性石、ま
たセラミックス等を用いた場合そのろ過機能や、水質を
ミネラル化するなどの幾つかの勝れた利点を発揮するも
のであるが、浴槽、温水にオゾンを注入、混合する点に
ついて検討すると幾つかの不具合点が見い出される。I
!Ilち、浴槽温水中にオゾンを注入、混合する理由は
幾つかあり、多面的であるが、幾つかを上げると次の通
りである。1つは温水中の臭気を脱臭するという点であ
る。より具体的には、オゾン臭により臭気をマスクする
こともあるが、特に溶存悪臭成分を酸化除去する点にあ
る。更に言えばろ過装置内のる材2より好適には活性炭
等がオゾンと悪臭成分との反応を促進して臭気を酸化除
去するものである。
[Problems to be Solved by the Invention] The above-mentioned prior art is capable of removing dirt, oil, etc. mixed into bathtub hot water by its performance when focusing on a filter using one or more of the filtration devices themselves. When using filters, activated stones, ceramics, etc. as filtration media to purify hot water, they exhibit several excellent advantages such as their filtration function and mineralization of water quality. When considering the injecting and mixing of ozone into hot water, several problems are found. I
! There are several and multifaceted reasons for injecting and mixing ozone into hot bath water, but some of them are as follows. One is that it deodorizes odors in hot water. More specifically, the ozone odor may be used to mask odor, but in particular, it oxidizes and removes dissolved malodorous components. Furthermore, activated carbon or the like is more preferable than the material 2 in the filtration device, which promotes the reaction between ozone and malodorous components to oxidize and remove odors.

2つ目は、オゾン自体の殺菌作用による温水中の有害菌
の殺菌、除菌である。その3は、オゾンを温水中に注入
、混合し、温水中の微生物の働きを活発化し、より具体
的にはチッ素成分等によって好気性微生物の働きを活発
化し、更に言えばろ過装置の部分に繁殖する好気性微生
物を活性化し、有機物を分解除去する点等々である。所
が従来はオゾン混合器を浴槽の流出端に配置し、はとん
ど浴槽中の温水に対して、即ちろ過装置に11’JJ1
3流入せんとしている温水にではなく、ろ過装置から出
てきた温水に対してオゾンを注入、混合しているので、
オゾン自体の脱臭、殺菌、有機物分解の機能はあるもの
の、ろ過装置の所に循環する前に浴槽の温水面から気泡
となって流出してしまうので脱臭について言えば、ろ過
装置に於けるろ材とオゾンの反応促進に伴なう脱臭作用
がほとんど利用されていず脱臭効率が低い、又好気性微
生物はろ過装置部分に多く繁殖しているが、同様な理由
で、オゾンによるその好気性微生物の活性化がほとんど
期待されず、有機物分解の効率が低い。
The second is the sterilization and sterilization of harmful bacteria in warm water due to the sterilizing effect of ozone itself. Part 3 is to inject and mix ozone into hot water to activate the action of microorganisms in the warm water, and more specifically, to activate the action of aerobic microorganisms with nitrogen components, and more specifically to the filtration equipment. These include activating aerobic microorganisms that breed in the water and decomposing and removing organic matter. However, in the past, the ozone mixer was placed at the outflow end of the bathtub, and most of the time, the ozone mixer was placed at the outflow end of the bathtub, and the ozone mixer was generally used for the hot water in the bathtub, that is, for the filtration device.
3. Ozone is injected and mixed into the hot water coming out of the filtration device, not into the hot water that is about to flow in.
Although ozone itself has the functions of deodorizing, sterilizing, and decomposing organic matter, it flows out in the form of bubbles from the hot water surface of the bathtub before being circulated to the filtration device. The deodorizing effect of ozone that accompanies the reaction promotion is hardly used, resulting in low deodorizing efficiency.Also, aerobic microorganisms breed in large numbers in the filtration device, and for the same reason, ozone activates the aerobic microorganisms. The efficiency of organic matter decomposition is low.

即ちオゾン注入と、ろ過装置の機能とが相関していない
That is, there is no correlation between ozone injection and the function of the filtration device.

更に特に、次の点が大きな問題となっている。In particular, the following points are major problems.

即ちオゾンはそれ自体有効であるものの、他方人体に及
ぼす毒性をもっている。その溶存量が適当でない場合に
は、即ち過剰の場合には刺激となって表われたり、毒性
が人体に残ったり、時には致死に至る。そこで、上述し
たオゾンの有効な機能を出さしめ人体の害のない予かし
め定めた適正濃度の下、オゾンを温水中に注入、混合す
る必要があるが、実際問題その設定が著しく困難である
。それ故に、従来技術のように浴槽の流出端の所で注入
、混合すると過剰オゾンが人体に直接接触するおそれが
あり、I!康−L好ましくないものである。
That is, although ozone itself is effective, it is also toxic to the human body. If the amount dissolved is not appropriate, that is, if it is in excess, it may cause irritation, remain toxic to the human body, and sometimes lead to death. Therefore, it is necessary to inject and mix ozone into warm water at a predetermined appropriate concentration that will bring out the effective function of ozone and will not cause any harm to the human body, but in reality, it is extremely difficult to set this. Therefore, if it is injected and mixed at the outflow end of the bathtub as in the prior art, excess ozone may come into direct contact with the human body, and I! Health-L is unfavorable.

[目的] 従って本発明の目的とする所は、オゾン注入とろ過装置
の機能とを相関させることのできる浴槽温水の循環方法
及びその装置を提供するにある。具体的には、オゾンを
最終段のろ過作用の上流側で注入、混合することにより
、ろ過手段のる材によるオゾンと悪臭成分の反応促進機
能を利用し、より脱臭効率を高めたり、余剰オゾンの吸
着除去をろ材によって図ったり、あるいはる材の部分に
多く繁殖する好気性微生物の活性化をより促がし、より
有機物の分解除去を可能ならしめたりするにある。
[Object] Accordingly, an object of the present invention is to provide a bathtub hot water circulation method and its device that can correlate ozone injection with the function of a filtration device. Specifically, by injecting and mixing ozone upstream of the final stage of filtration, the material used in the filtration means promotes the reaction between ozone and malodorous components, thereby increasing deodorizing efficiency and removing excess ozone. The purpose is to remove the organic matter by adsorption using a filter material, or to further promote the activation of aerobic microorganisms that proliferate in the filter material, thereby making it possible to decompose and remove more organic matter.

加えて、特にオゾンを過剰に注入、混合することなく人
体に対する悪影響を可及的に排除できるようにするにあ
る。而も、温水循環過程に於けるエアーロック現象を防
+hできる手段を提供するにある・ [課題を解決する為の手段] 上記目的を達成する為に本発明は次の技術酌り段を有す
る。即ち、実施例に対応する添付図面中の符号を用いて
これを説明すると、本発明方法は浴槽の温水を吸入し、
次いでろ過し、又はろ過及び温水活性化並びに保温加熱
し、続いて浴槽側に流出せしめることにより上記温水を
清浄化又は清n化、活性化及び定温化するようにすると
共に1−記温水の循環過程で上記温水中にオゾンを注入
するようにした浴槽温水の清浄循環方法に於いてに記オ
ゾンは、最終段のろ過作用が与えられる位置のヒ流位置
で循環温水中に注入せしめられると共に、」二足オゾン
注入位置より下流位置に於いて温水中に発生したエアを
分離可能にした喜を特徴とする浴槽温水の清浄循環方法
であり、その装置発明は少なくとも、ろ過手段と、上記
ろ過手段の内最終段のろ過作用を実施する為のろ過装置
3に浴槽1中の温水Wを注入せしめる為の温水流入管系
6と、上記ろ過装置3から温水Wを浴槽1中に流出せし
める為の温水流出管系12並びに循環ポンプ9より成る
温水循環系を有すると共に、オゾン発生器14で生じた
オゾンを上記温水循環系に注入する為のオゾン混合器を
有する浴槽温水の清浄循環装置に於いて; 上記オゾン発生器14にオゾン注入管15を介して連な
るオゾン混合器!6は、上記最終段のろ過装置3の位置
を基準として、その一次側に相当する温水流入管系6に
配設されていると共に、上記オゾン混合器16の下流位
置に気液分離器17を配設した事を特徴とする浴槽温水
の清浄循環装置である。
In addition, the objective is to eliminate as much as possible the negative effects on the human body without injecting or mixing ozone excessively. Moreover, the present invention has the following technical considerations in order to achieve the above object. . That is, to explain this using the reference numerals in the accompanying drawings corresponding to the embodiments, the method of the present invention inhales hot water from a bathtub,
Next, the hot water is purified or purified, activated, and kept at a constant temperature by filtration, filtration, hot water activation, and thermal insulation heating, and then flowing out to the bathtub side. In the bathtub hot water purification and circulation method in which ozone is injected into the hot water in the process, the ozone is injected into the circulating hot water at a position where the final stage of filtration is applied, and at the same time, '' A bathtub hot water purification method characterized by the ability to separate air generated in hot water at a position downstream from the ozone injection position, and the device invention comprises at least a filtration means and the above-mentioned filtration means. A hot water inflow pipe system 6 for injecting the hot water W in the bathtub 1 into the filtration device 3 for carrying out the final stage filtration action, and a hot water inflow pipe system 6 for causing the hot water W to flow out from the filtration device 3 into the bathtub 1. In a bathtub hot water purification and circulation device which has a hot water circulation system consisting of a hot water outflow pipe system 12 and a circulation pump 9, and also has an ozone mixer for injecting ozone generated by an ozone generator 14 into the hot water circulation system. ; An ozone mixer connected to the ozone generator 14 via an ozone injection pipe 15! 6 is disposed in the hot water inflow pipe system 6 corresponding to the primary side with respect to the position of the final stage filtration device 3, and a gas-liquid separator 17 is installed downstream of the ozone mixer 16. This is a bathtub warm water purifying circulation device that is characterized by the following:

[作用] 上記構成なので、浴槽lの温水は循環ポンプ9によりろ
過装置3内へ温水流入管6を介して流入する。そこでろ
過される。この場合、単に汚れ、油分が分離される他、
ろ材の種類に応じた機能でろ過される。且つこのろ材自
体による脱臭作用も実施される0次いで温水流出管12
を介し・℃浴槽へ流出される。即ち温水が循環によって
清浄化される。
[Function] With the above configuration, hot water in the bathtub 1 flows into the filtration device 3 via the hot water inflow pipe 6 by the circulation pump 9. It is filtered there. In this case, in addition to simply separating dirt and oil,
Filtering is performed using functions depending on the type of filter media. In addition, the filter medium itself also performs a deodorizing effect.
It flows out into the bathtub through the temperature. That is, the hot water is purified by circulation.

そして、この循環過程でオゾン混合器1Gからオゾンが
注入、混合される。溶存したオゾン自体によるマスキン
グあるいは酸化作用によって脱臭が図られると共に、殺
菌作用により温水中の有害菌が殺菌される。加えて好気
性微生物の増殖活性化が図られ、有機物が分解除去され
る。等々である。
During this circulation process, ozone is injected and mixed from the ozone mixer 1G. Deodorization is achieved through masking or oxidation by the dissolved ozone itself, and harmful bacteria in the warm water are sterilized through sterilization. In addition, the growth of aerobic microorganisms is activated, and organic matter is decomposed and removed. etc.

しかしながら本発明の特徴的な作用は次の通りである。However, the characteristic effects of the present invention are as follows.

オゾンは最終段のろ過装置3の手前で注入される。Ozone is injected before the final stage filtration device 3.

故にろ過装置3のろ材によるオゾンと悪臭成分の反応促
進機能が助長され易い、加えて好気性微生物の繁殖場所
はろ材近辺であり、それら好気性微生物を活性化し易く
、その有機物分解除去が効率よ〈実施される。
Therefore, the function of promoting the reaction between ozone and malodorous components by the filter medium of the filter device 3 is likely to be facilitated, and in addition, aerobic microorganisms breed near the filter medium, making it easy to activate these aerobic microorganisms and decomposing and removing organic matter efficiently. <Implemented.

とりわけ、オゾン混合器16からのオゾン注入礒がやや
過剰であっても、人体のある浴Jfll中へ行< 1i
ijに気液分m器17の所で溶解しない過剰分が大気へ
放出される。
In particular, even if the ozone injection from the ozone mixer 16 is slightly excessive, it will not be possible to enter the bath where the human body is located.
The excess amount that is not dissolved in the gas-liquid separator 17 is discharged to the atmosphere.

故に最適オゾン注入量の設定が容易となる[実施例] 次に添付図面に従い本発明の好適な実施例を詳述する。Therefore, it is easy to set the optimal ozone injection amount [Example] Next, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

図に於いて1は浴槽、2は温水清浄循環装置を各々示し
ている。
In the figure, 1 indicates a bathtub, and 2 indicates a hot water purifying circulation device.

上記温水清浄循環装置2内にはろ過手段が配設されてい
る。この例ではろ過装置3として示され、これが最終段
に位置している。そしてこの例ではろ過装置3は、下流
側にヒータ3A、例えば遠赤外線セラミックヒータが配
設され、上流側にろ過石3Bが配設されている。
A filtration means is disposed within the hot water purifying circulation device 2. In this example, it is shown as filtration device 3, which is located at the final stage. In this example, the filter device 3 includes a heater 3A, for example, a far-infrared ceramic heater, on the downstream side, and a filter stone 3B on the upstream side.

ろ過石3Bとしては、活性炭、バイオシュタインなどの
活性石、セラミックス等適宜のる材が選択される9次い
で、浴槽1の下方部分4と、ろ過装ご3の流入端5間に
温水流入管6が接続され、その温水流入管6の途中に上
流より順次バルブ7、−次清節化手段(ろ過装置)とし
てのヘアキャッチャ8.温水循環ポンプ9が配設されて
いる。
As the filter stone 3B, an appropriate material such as activated carbon, activated stone such as biostein, ceramics, etc. is selected.9 Next, a hot water inflow pipe 6 is connected between the lower part 4 of the bathtub 1 and the inflow end 5 of the filtration device 3. are connected to the hot water inflow pipe 6, and a valve 7, a hair catcher 8 as a filtering means (filtering device) are connected to the hot water inlet pipe 6 in order from upstream. A hot water circulation pump 9 is provided.

他方浴槽lのF方部分10と、ろ過装置3の流出端11
の間に温水流出管12が接続され、この温水流出管12
の中途にバルブ13が取着されている。
On the other hand, the F side portion 10 of the bathtub l and the outflow end 11 of the filtration device 3
A hot water outflow pipe 12 is connected between the hot water outflow pipe 12 and
A valve 13 is attached in the middle.

以りは従来一般の温水清浄循環装置の一例を示したもの
であるが、本発明は首記した目的を達成する為に次のよ
うにしたものである。
The following is an example of a conventional general hot water purifying circulation device, but the present invention is made as follows in order to achieve the above-mentioned object.

第1は、上記ろ過手段の内、最終段に位置するろ過装置
3に着目した場合、その一次側に位置する温水流入管6
の所にオゾン混合器1Bを配する。
First, when focusing on the filtration device 3 located at the final stage of the above-mentioned filtration means, the hot water inflow pipe 6 located on the primary side thereof.
Place the ozone mixer 1B at the location.

オゾン混合器16はオリフィス型、対向流吐出型憧憬つ
かの手段を用いることができる。その内オリフィス型の
例は第2図、対向流吐出型の例は第4図に示し、これら
の作用は後述する動作の所で前述する。
The ozone mixer 16 may be of an orifice type or a counterflow discharge type. An example of the orifice type is shown in FIG. 2, and an example of the counterflow discharge type is shown in FIG. 4, and their actions will be described in the section of operation described below.

土足オゾン混合器16にオゾンを送る手段は公知のオゾ
ン発生器14を用い、オゾン発生源14Aと、送り込み
の為のエアーポンプ14Bより成り、オゾン発生源14
Aとオゾン混合器18の間がオゾン注入管15によって
接続されている。
The means for sending ozone to the ozone mixer 16 uses a known ozone generator 14, which is composed of an ozone generation source 14A and an air pump 14B for feeding.
A and an ozone mixer 18 are connected by an ozone injection pipe 15.

改良の第2は、上記オゾン混合器16の位置を基準とし
て、その上流位置に気液分離器17を取着するものであ
り、この例ではろ過装置3の頂部に配した例を示しであ
る。気液分離器17としては、第3図に示すフロートタ
イプの他、タイマー制御やセンサー検出制御等の電磁弁
タイプでもよい。
The second improvement is to install a gas-liquid separator 17 at a position upstream of the ozone mixer 16, and in this example, it is installed at the top of the filtration device 3. . In addition to the float type shown in FIG. 3, the gas-liquid separator 17 may be of a solenoid valve type such as timer control or sensor detection control.

に記構成に基づきその動作を説明する。The operation will be explained based on the configuration described below.

循環ポンプ9の駆動により浴槽l中の温水Wは、温水流
入管6を介して流入し、ヘアキャッチャ8でヘア等が除
去される0次いでろ過装置3内に入り、ヒータ3Aで加
熱される。ヒータ3Aは予かじめ定めた一定温度、例え
ば42℃以上でOFFとなり、それ以下でONとなるよ
う定められ、温水を保温する。温水はろ材3B中に入り
、そこで汚れ、油分が分離又は吸着あるいはPH調節等
される。そして温水Wは再び温水流出管12を介して浴
槽lへ戻る。
As the circulation pump 9 is driven, the hot water W in the bathtub 1 flows in through the hot water inflow pipe 6, hair etc. are removed by the hair catcher 8, and then enters the filtration device 3 where it is heated by the heater 3A. The heater 3A is set to be turned off at a predetermined temperature, for example, 42° C. or higher, and turned on at a temperature lower than that, to keep the hot water warm. The hot water enters the filter medium 3B, where dirt and oil are separated or adsorbed or the pH is adjusted. The hot water W then returns to the bathtub l via the hot water outflow pipe 12 again.

このようにろ過手段によって清浄化される。In this way, it is cleaned by the filtration means.

上記過程に於いてオゾン混合器16から温水W中にオゾ
ンが注入、混合される。
In the above process, ozone is injected into the hot water W from the ozone mixer 16 and mixed.

それ故に、オゾンのマスキング作用により温水の悪臭成
分がマスクされたり、その酸化作用によす悪臭成分が分
解される。あるいはオゾンの殺菌作用により殺菌あるい
は滅菌される。
Therefore, the masking effect of ozone masks the malodorous components of hot water, and the malodorous components caused by its oxidizing action are decomposed. Alternatively, it is sterilized or sterilized by the bactericidal action of ozone.

加えて溶存すシンにより好気性微生物を活性化し、有機
物を分解、除去する等々である。
In addition, dissolved syn causes activation of aerobic microorganisms, which decomposes and removes organic matter.

所で、オゾンはろ過装置3の手前で注入、混合される。By the way, ozone is injected and mixed before the filtration device 3.

この為、ろ過装置3内のろ材による悪臭成分とオゾンの
反応促進の利益を直接受け、よりよく脱臭が図られる。
Therefore, the user directly benefits from the promotion of the reaction between malodorous components and ozone by the filter medium in the filtration device 3, and can achieve better deodorization.

加えてろ材の所に好気性微生物が多く存するので、溶存
すシンによる活性化がより図られ、有機物の分解がより
進む。
In addition, since there are many aerobic microorganisms in the filter media, they are more activated by dissolved syn, and the decomposition of organic matter is further promoted.

特にオゾンを注入、混合する場合、その最適濃度の設定
がむずかしい所であるが、仮に余剰にオゾンを注入して
も、ろ過装置3の最り流で気液分#rl、17により大
気中へ気体となって分離できるから、過剰オゾンを浴槽
中へ環流し、人体に毒性を及ぼすことが可及的に防止さ
れる。
In particular, when injecting and mixing ozone, it is difficult to set the optimum concentration, but even if excess ozone is injected, it will be released into the atmosphere by the gas-liquid component #rl, 17 in the last stream of the filtration device 3. Since it can be separated as a gas, it is possible to prevent excess ozone from flowing back into the bathtub and causing toxicity to the human body.

加えて、過剰オゾンによるエアーロックも防止される。In addition, air locks caused by excess ozone are also prevented.

而してこの例に於ける気液分離の動作は、第3図に示す
ようにフロート25が下がることにより、ノズルピン2
6が空気出口27を開放して実施される。
The gas-liquid separation operation in this example is performed by lowering the float 25 as shown in FIG.
6 is carried out with the air outlet 27 open.

尚、23はケーシング、24はフロート摺動支持具であ
る。
In addition, 23 is a casing, and 24 is a float sliding support.

更にこの例のオリフィス型のオゾン混合器18の作用を
前述すると、流入側18と流出側18の間にオリフィス
20が形成され、膨張部21にオゾン注入管端22が接
続されている。直径D2−の流入側18方向から圧力P
Oで送水した時、直径d2−のオリフィス部20による
圧力損失P2−と、直径D2の膨張部21で発生する負
圧PLと、直径DAの流出側19での圧力P2は次式で
表わされる。
Further, the operation of the orifice type ozone mixer 18 of this example will be described in detail. An orifice 20 is formed between the inflow side 18 and the outflow side 18, and the ozone injection pipe end 22 is connected to the expansion part 21. Pressure P from the inlet side 18 direction of diameter D2-
When water is fed at O, the pressure loss P2- due to the orifice part 20 with diameter d2-, the negative pressure PL generated in the expansion part 21 with diameter D2, and the pressure P2 at the outflow side 19 with diameter DA are expressed by the following formula. .

Pa = P2−+ (−Pi)+P2この膨張部21
での負圧pLは、オリフィス部20による流速の−hM
に伴なうカルマン渦が原因で発生するが、 D、>n2>DL>d2−>dL を適度に設定することにより、オゾン流入管端22が大
気圧より低い値になる。
Pa = P2-+ (-Pi) + P2 This expansion part 21
The negative pressure pL at
This is caused by the Karman vortex associated with , but by appropriately setting D,>n2>DL>d2->dL, the pressure at the ozone inlet pipe end 22 becomes lower than atmospheric pressure.

即ちオリフィス部20により噴流が生じ、膨張部21に
負圧が発生し、オゾン注入管端22よりオゾンが吸入さ
れると、流出側19に至る経路ではオゾンと温水が混合
され見掛りの比重が軽くなる。この為、膨張部21と流
出側19での流路損失が減り、膨張部21の負圧は更に
増し、より失活のオゾンが吸入される。
That is, when a jet is generated by the orifice part 20 and negative pressure is generated in the expansion part 21, and ozone is sucked from the ozone injection pipe end 22, ozone and hot water are mixed in the path leading to the outflow side 19, and the apparent specific gravity is reduced. It becomes lighter. Therefore, the flow path loss at the expansion part 21 and the outflow side 19 is reduced, the negative pressure in the expansion part 21 is further increased, and more deactivated ozone is sucked in.

更に第4図の対向流吐出型を用いる場合には、温水流入
管6から細径の分岐管28を分岐し、中途にポンプ29
を配すると共に注入チャンバー30を形成し、ノズル3
1を対向させる。オゾン注入管15は上記チャンバー3
0に接続される。これによると温水に対してノズル31
から対向してオゾンが吐出され温水に混合される。
Furthermore, when using the counterflow discharge type shown in FIG.
The injection chamber 30 is formed, and the nozzle 3
1 to face each other. The ozone injection pipe 15 is connected to the chamber 3
Connected to 0. According to this, nozzle 31 for hot water
Ozone is discharged from the opposite side and mixed with the hot water.

勿論、本発明はこれらのオゾン混合器16の例に特定さ
れるものではない。
Of course, the present invention is not limited to these examples of ozone mixer 16.

[発明の効果] 以上詳述した如く、この発明によれば、オゾンを温水に
注入、混合するに当り最終段のろ過装置の一次側に於い
て行うので、オゾンと悪臭成分の反応促進機能をもつる
材の、その機能をより促進でき、よりよく脱臭が可能に
されると共に、好気性微生物はろ過装置部分に多く存す
るので、そのろ材付近の好気性微生物をより活性化でき
、より有機物を分解除去できる9等々オゾン注入とろ過
機能を有機的に相関できる。
[Effects of the Invention] As detailed above, according to the present invention, since ozone is injected into hot water and mixed on the primary side of the final stage filtration device, the function of promoting the reaction between ozone and malodorous components is enhanced. The function of the vine material can be further promoted and deodorization can be achieved better.Since many aerobic microorganisms exist in the filtration device, the aerobic microorganisms near the filter material can be further activated and organic matter can be removed more effectively. 9, etc., which can be decomposed and removed, organically correlates ozone injection and filtration function.

特に、オゾンの温水に対する注入、混合濃度の適正設定
がむずかしい所であるが、仮に誤って過剰に注入しても
、オゾン混合器16の上流側、即ち浴槽lに至らない段
階で分離してしまうので人体に対する毒性影響を可及的
に排除できる。加えてエアーロックを防ILでき、温水
循環に支障がない等実用上各種の利点を呈する。より具
体的には、浴槽温水内に直接オゾンを注入せず、最終の
ろ過手段の手前でオゾンを強制的に直接混合する為に、
オゾンによる殺菌浄化作用をより効果的にかつ人体に対
して安全に利用することが可能である。
In particular, it is difficult to inject ozone into hot water and properly set the mixing concentration, but even if you inadvertently inject too much ozone, it will separate before reaching the upstream side of the ozone mixer 16, that is, the bathtub l. Therefore, toxic effects on the human body can be eliminated as much as possible. In addition, it has various practical advantages, such as preventing air locks and preventing hot water circulation. More specifically, in order to forcibly mix ozone directly before the final filtration method, instead of injecting ozone directly into the hot bath water,
It is possible to utilize the sterilization and purification effect of ozone more effectively and safely for the human body.

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

添付図面は本発明の実施例を示し、第1図は全体を示す
縦断面図、第2図はオリフィス型のオゾン混合器の偶因
、第3図は気液分離器の偶因、第4図は対向流吐出型の
オゾン混合器の偶因であり、図中1は浴槽、Wは温水、
2は温水清浄循環装置、3は最終段のろ過装置、18は
オゾン混合器、17は気液分離器である。 ・−7−二・:] 第2 叫 辛4図 ¥3斗
The accompanying drawings show embodiments of the present invention, in which Fig. 1 is a longitudinal sectional view showing the whole, Fig. 2 is a contingency diagram of an orifice type ozone mixer, Fig. 3 is a contingency diagram of a gas-liquid separator, and Fig. 4 is a longitudinal sectional view showing the whole. The figure shows the accidental causes of a counterflow discharge type ozone mixer. In the figure, 1 is a bathtub, W is a hot water tank,
2 is a hot water purifying circulation device, 3 is a final stage filtration device, 18 is an ozone mixer, and 17 is a gas-liquid separator.・−7−2・:] 2nd Shouting 4 Figures ¥3 To

Claims (3)

【特許請求の範囲】[Claims] (1)浴槽の温水を吸入し、次いでろ過し、又はろ過及
び温水活性化並びに保温加熱し、続いて浴槽側に流出せ
しめることにより上記温水を清浄化又は清浄化、活性化
及び定温化するようにすると共に上記温水の循環過程で
上記温水中にオゾンを注入するようにした浴槽温水の清
浄循環方法に於いて; 上記オゾンは、最終段のろ過作用が与えられる位置の上
流位置で循環温水中に注入せしめられると共に、上記オ
ゾン注入位置より下流位置に於いて温水中に発生したエ
アを分離可能にした事を特徴とする浴槽温水の清浄循環
方法。
(1) Inhale hot water from the bathtub, then filter it, or filter it and activate the hot water, heat it to keep it warm, and then let it flow out to the bathtub side to purify or purify the hot water, activate it, and keep it at a constant temperature. In the bathtub hot water purification method, the ozone is injected into the hot water during the hot water circulation process; A method for cleaning and circulating hot water in a bathtub, characterized in that the air generated in the hot water can be separated at a position downstream from the ozone injection position.
(2)少なくとも、ろ過手段と、上記ろ過手段の内最終
段のろ過作用を実施する為のろ過装置3に浴槽1中の温
水Wを注入せしめる為の温水流入管系6と、上記ろ過装
置3から温水Wを浴槽1中に流出せしめる為の温水流出
管系12並びに循環ポンプ9より成る温水循環系を有す
ると共に、オゾン発生器14で生じたオゾンを上記温水
循環系に注入する為のオゾン混合器を有する浴槽温水の
清浄循環装置に於いて; 上記オゾン発生器14にオゾン注入管15を介して連な
るオゾン混合器16は、上記最終段のろ過装置3の位置
を基準として、その一次側に相当する温水流入管系6に
配設されていると共に、上記オゾン混合器16の下流位
置に気液分離器17を配設した事を特徴とする浴槽温水
の清浄循環装置。
(2) At least a filtration means, a hot water inflow pipe system 6 for injecting the hot water W in the bathtub 1 into the filtration device 3 for performing the final stage of filtration action among the filtration means, and the filtration device 3 It has a hot water circulation system consisting of a hot water outflow pipe system 12 for causing hot water W to flow out into the bathtub 1 and a circulation pump 9, and an ozone mixing system for injecting ozone generated in the ozone generator 14 into the hot water circulation system. In the bathtub warm water purifying and circulating device having a bathtub water tank, the ozone mixer 16 is connected to the ozone generator 14 via the ozone injection pipe 15, and the ozone mixer 16 is connected to the ozone generator 14 via the ozone injection pipe 15, and the ozone mixer 16 has a A bathtub hot water purification and circulation device characterized in that a gas-liquid separator 17 is installed in a corresponding hot water inflow pipe system 6 and at a downstream position of the ozone mixer 16.
(3)上記気液分離器17は最終段のろ過装置3の上部
に配した事を特徴とする請求項第2項記載の浴槽温水の
清浄循環装置。
(3) The bathtub warm water purification and circulation system according to claim 2, wherein the gas-liquid separator 17 is disposed above the final stage filtration device 3.
JP8440688A 1988-04-06 1988-04-06 Method and device for cleaning and circulating hot water of bath tub Granted JPH01258795A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8440688A JPH01258795A (en) 1988-04-06 1988-04-06 Method and device for cleaning and circulating hot water of bath tub

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8440688A JPH01258795A (en) 1988-04-06 1988-04-06 Method and device for cleaning and circulating hot water of bath tub

Publications (2)

Publication Number Publication Date
JPH01258795A true JPH01258795A (en) 1989-10-16
JPH0376196B2 JPH0376196B2 (en) 1991-12-04

Family

ID=13829707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8440688A Granted JPH01258795A (en) 1988-04-06 1988-04-06 Method and device for cleaning and circulating hot water of bath tub

Country Status (1)

Country Link
JP (1) JPH01258795A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03155818A (en) * 1989-11-14 1991-07-03 O D S:Kk Circulating type bath
JPH0465197U (en) * 1990-10-19 1992-06-05
JP2021000276A (en) * 2019-06-21 2021-01-07 東京都 Water treatment system, and water treatment method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03155818A (en) * 1989-11-14 1991-07-03 O D S:Kk Circulating type bath
JPH0445202B2 (en) * 1989-11-14 1992-07-24 Oo Deii Esu Kk
JPH0465197U (en) * 1990-10-19 1992-06-05
JP2021000276A (en) * 2019-06-21 2021-01-07 東京都 Water treatment system, and water treatment method

Also Published As

Publication number Publication date
JPH0376196B2 (en) 1991-12-04

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