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JPH0376196B2 - - Google Patents
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JPH0376196B2 - - Google Patents

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Publication number
JPH0376196B2
JPH0376196B2 JP63084406A JP8440688A JPH0376196B2 JP H0376196 B2 JPH0376196 B2 JP H0376196B2 JP 63084406 A JP63084406 A JP 63084406A JP 8440688 A JP8440688 A JP 8440688A JP H0376196 B2 JPH0376196 B2 JP H0376196B2
Authority
JP
Japan
Prior art keywords
hot water
ozone
bathtub
filtration device
circulation
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
Application number
JP63084406A
Other languages
Japanese (ja)
Other versions
JPH01258795A (en
Inventor
Keisuke Kono
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 HOOMU PURODAKUTSU KK
Original Assignee
NIPPON HOOMU PURODAKUTSU 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 HOOMU PURODAKUTSU KK filed Critical NIPPON HOOMU PURODAKUTSU KK
Priority to JP63084406A 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

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  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Filtration Of Liquid (AREA)
  • Water Treatment By Sorption (AREA)

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] [Field of Industrial Application] The present invention relates to a method and apparatus for purifying warm bath water, 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、その一環とし
て浴槽の温水を清浄化したり、温水中の臭気を脱
臭したり、あるいは温水中の身体健維持に不適当
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、上記
ろ過手段の内最終段のろ過作用を実施する為のろ
過装置に浴槽中の温水を流入せしめる為の温水流
入管系と、上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、而も上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、一次、二次と多段複数に配されている場合も
あり、且つろ過フイルターを用いたもの、活性炭
を用いたもの、デバイオシユタイン(麦飯石)な
どの活性石)を用いたもの、セラミツクスを用い
たもの等種々あり、加えて上記循環系に遠赤外線
セラミツ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 become more sophisticated and diversified, a wide variety of improvements have been made to bathing, including purifying hot water in bathtubs, deodorizing odors in hot water, and There are methods in practical use to sterilize and eliminate fungi that are unsuitable for maintaining physical health inside the body. That is, it is usually called a means for purifying hot bath water or a means for deodorizing and sterilizing hot water, and this device includes at least a filtration means and a final stage of the filtration means. A hot water inflow pipe system for causing hot water in the bathtub to flow into the filtration device, a hot water outflow pipe system for circulating hot water from the filtration device into the bathtub, and a circulation pump, and the above hot water circulation system It has an ozone mixer for injecting and mixing ozone generated by an ozone generator. In the above, the filtration means may be singular, or may be arranged in multiple stages such as primary and secondary. There are various types such as those using activated stones such as
For example, there are some that are kept warm at around 42 degrees Celsius.

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 will see that in the past, an ozone mixer for injecting and mixing ozone generated in an ozone generator was extended from the secondary side of the filtration device. It is disposed in an outflow pipe system 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、上記単又は複数のろ過装置そ
のものによるろ過機能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
てフイルター及び活性石、またセラミツクス等を
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。即ち、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
装置内のろ材、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] When focusing on the filtration function of the single or plural filtration devices themselves, the above-mentioned prior art is capable of removing dirt, oil, etc. that get mixed into hot water in a bathtub, and producing hot water. When filters, activated stones, ceramics, etc. are used as cleaning and filtration media, they exhibit several excellent advantages such as their filtration function and mineralization of water quality. When considering the injection and mixing of ozone, several problems are found. That is, there are several and multifaceted reasons for injecting and mixing ozone into hot bath water, but some of them are as follows. 1 is that it deodorizes odors in hot water. More specifically, ozone odor may be used to mask odor, but in particular, it oxidizes and removes dissolved malodorous components. Furthermore, the filter medium in the filtration device, more preferably activated carbon or the like, promotes the reaction between ozone and malodorous components to oxidize and remove the odor.

2つ目は、オゾン自体の殺菌作用よる温水中の
有害菌の殺菌、除菌である。その3は、オゾンを
温水中に注入し、混合し、温水中の微生物の働き
を活発化し、より具体的にはチツ素成分等によつ
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、ほとんど
浴槽中の温水に対して、即ちろ過装置に循環流入
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循環を注入、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
の温水面から泡となて流出してしまうので脱臭に
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も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。即ちオゾン注
入と、ろ過装置の機能とが相関していない。
The second is the sterilization and sterilization of harmful bacteria in warm water due to the bactericidal action of ozone itself. Part 3 is injecting ozone into hot water and mixing it to activate the action of microorganisms in the warm water.More specifically, it activates the action of aerobic microorganisms through the use of nitrogen components, and more specifically, filtration. Activates the microorganisms that grow in the device,
These include decomposing and removing organic matter. However, in the past, an ozone mixer was placed at the outflow end of the bathtub, and the ozone mixer was placed at the outflow end of the bathtub, and the ozone mixer was used to circulate mostly the hot water in the bathtub, that is, the hot water coming out of the filtration device, rather than the hot water that was going to be circulated into the filtration device. Ozone itself has the functions of deodorizing, sterilizing, and decomposing organic matter, but it flows out in the form of bubbles from the hot water surface of the bathtub before being circulated to the filtration device, so it is difficult to deodorize. In other words, the deodorizing effect accompanying the promotion of the reaction between the filter medium and ozone in the filtration device is rarely utilized, resulting in low deodorizing efficiency. In addition, aerobic microorganisms breed in large numbers in the filtration device, but for the same reason, activation of these aerobic microorganisms by ozone is hardly expected, and the efficiency of organic matter decomposition is low. 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つている。 In particular, the following points are a major problem.

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つている。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
つて表われたり、毒性が人体に残つたり、時には
致死に至る。そこで、上述したオゾンの有効な機
能を出せしめる人体の害のない予かじめ定めた適
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、健康上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 dissolved amount 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 is not harmful to the human body and allows ozone to perform its effective functions as described above, but in reality, it is extremely difficult to set this. . Therefore, if the ozone 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, which is unfavorable for health.

[目的] 従つ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、ろ過手段のろ材に
よるオゾンと悪臭成分の溌応促進機能を利用し、
より脱臭効率を高めたり、余剰オゾンの吸訂除去
をろ材によつて図つたり、あるいはろ材の部分に
多く繁殖する好気性微生物の活性化をより促さ
り、より有機物の分解除去を可能ならしめたりす
るにある。
[Objective] Therefore, an object of the present invention is to provide a bathtub hot water circulation method and its apparatus that can correlate ozone injection with the function of a filtration device.
Specifically, by injecting and mixing ozone at the upstream side of the final stage of filtration, we utilize the function of promoting the reaction between ozone and malodorous components by the filter media of the filtration means.
By increasing the deodorizing efficiency, by absorbing and removing excess ozone using a filter medium, or by promoting the activation of aerobic microorganisms that breed in large numbers in the filter medium, it is possible to further decompose and remove organic matter. There is something to do.

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
るエアーロツク現象を防止できる手段を提供する
にある。
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, it is an object of the present invention to provide a means for preventing the air lock phenomenon in the hot water circulation process.

[課題を解決するための手段] 上記目的を達成する為に本発明は次の技術的手
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
浄化、活性化及び定温化する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してから循環させ
るようにした事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
置である。
[Means for Solving the Problems] In order to achieve the above object, the present invention has the following technical means. That is, to explain this using the reference numerals in the accompanying drawings corresponding to the embodiments, the method of the present invention sucks hot water from a bathtub, then filters it, or filters and activates the hot water and heats it to keep it warm, and then drains the bathtub side. In a bathtub hot water purification method, the hot water is purified or purified, activated and temperature-controlled by flowing out into the hot water, and ozone is injected into the hot water during the hot water circulation process; The ozone is injected into the circulating warm water at a position upstream of the position where the final stage filtration action is applied, and air generated in the hot water is separated at a position downstream of the ozone injection position before being circulated. This is a method for purifying hot water in a bathtub 1, characterized in that the invention includes at least a filtration means and a filtration device 3 for carrying out a final stage filtration action of the above-mentioned filtration means. It has a hot water circulation system consisting of a hot water inflow pipe system 6 for injecting W, a hot water outflow pipe system 12 for flowing hot water W from the filtration device 3 into the bathtub 1, and a circulation pump 9, and an ozone generator. In a bathtub hot water purification and circulation system having an ozone mixer for injecting the ozone generated in step 14 into the hot water circulation system; an ozone mixer 16 connected to the ozone generator 14 via an ozone injection pipe 15, Based on the position of the final stage filtration device 3, a gas-liquid separator 17 is disposed in the hot water inflow pipe system 6 corresponding to the primary side thereof, and a gas-liquid separator 17 is located downstream of the ozone mixer 16.
This is a bathtub hot water purifying circulation device that is characterized by being equipped with.

[作用] 上記構成なので、浴槽1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。次いで温水流出管12を介して浴槽
へ流出される。即ち温水が循環によつて清浄化さ
れる。
[Function] With the above configuration, hot water in the bathtub 1 is supplied to the circulation pump 9.
The hot water flows into the filtration device 3 via the hot water inflow pipe 6. It is filtered there. In this case, just dirt,
In addition to separating oil, it is also filtered using functions depending on the type of filter media. Moreover, the deodorizing effect is also carried out by the filter medium itself. The hot water then flows out through the hot water outflow pipe 12 into the bathtub. 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16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つて脱臭
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 16. Deodorization is achieved by masking or oxidation by the dissolved ozone itself, and harmful bacteria in the warm water are sterilized by the bactericidal action. 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、その有機分解除去が効率
よく実施される。
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 promoted. In addition, aerobic microorganisms breed near the filter medium, making it easy to activate these aerobic microorganisms and efficiently decomposing and removing organic matter.

とりわけ、オゾン混合器16からのオゾン注入
量がやや過剰であつても、人体のある浴槽1中へ
行く前に液分離器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 amount of ozone injected from the ozone mixer 16 is slightly excessive, the excess that is not dissolved in the liquid separator 17 is released into the atmosphere before going into the bathtub 1 where the human body is located.

故に最適オゾン注入量の設定が容易となる。 Therefore, it becomes easy to set the optimum ozone injection amount.

[実施例] 次に添付図に従い本発明の好適な実施例を詳述
する。
[Embodiments] 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
遠赤外線セラミツクヒータが配設され、上流側ろ
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 filtration device 3 is provided with 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、バイオシユタイ
ンなどの活性石、セラミツクス等適宜のろ材が選
択される。次いで、浴槽1の下方部分4と、ろ過
装置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、一次清浄手段(ろ過装置)としてのヘアキヤ
ツプ8、温水循環ポンプ9が配設されている。
As the filter stone 3B, an appropriate filter medium such as activated carbon, activated stone such as biosituine, ceramics, etc. is selected. Then, 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;
In the middle of the hot water inflow pipe 6, a valve 7, a hair cap 8 as a primary cleaning means (filtration device), and a hot water circulation pump 9 are disposed in order from upstream.

他方浴槽1の上方部分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, a hot water outflow pipe 12 is connected between the upper part 10 of the bathtub 1 and the outflow end 11 of the filtration device 3, and a valve 13 is attached to the middle of this hot water outflow pipe 12.

以上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 above 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16を配す
る。オゾン混合器16はオリフイス型、対向流吐
出型等幾つかの手段を用いることができる。その
内オリフイス型の例は第2図、対向吐出型の例は
第4図に示し、これらの作用は後述する動作の所
で簡述する。
First, when focusing on the filtration device 3 located at the final stage among the above-mentioned filtration means, an ozone mixer 16 is disposed at the hot water inflow pipe 6 located on the primary side thereof. The ozone mixer 16 can be of several types, such as an orifice type or a counterflow discharge type. An example of the orifice type is shown in FIG. 2, and an example of the opposing discharge type is shown in FIG. 4, and the effects of these will be briefly explained in the operation section below.

上記オゾン混合器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14
A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14Bとオゾン混合器16の間
がオゾン注入管15によつて接続されている。
A known ozone generator 14 is used as means for sending ozone to the ozone mixer 16.
A and an air pump 14B for feeding, and an ozone injection pipe 15 connects the ozone generation source 14B and the ozone mixer 16.

改良の第2は、上記オゾン混合器16の位置を
基準として、その下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
に配した例を示してある。気液分離器17として
は、第3図に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 downstream of the ozone mixer 16, and in this example, it is installed at the top of the filtration device 3. . The gas-liquid separator 17 may be of the float type shown in FIG. 3 or may be of a solenoid valve type with timer control or sensor detection control.

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

循環ポンプ9の駆動により浴槽1中の温水W
は、温水流入管6を介して流入し、ヘアキヤツチ
ヤ8でヘア等が除去される。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1へ戻る。
The hot water W in the bathtub 1 is driven by the circulation pump 9.
The water flows in through the hot water inflow pipe 6, and the hair etc. are removed by the hair catcher 8. Next, it enters the filtration device 3 and is heated by the heater 3A. Heater 3A operates at a predetermined constant temperature, e.g. 42°C or higher.
It is set to turn off, and turn on when the temperature is lower than that, keeping the hot water warm. The hot water enters the filter medium 3B,
There, dirt and oil are separated or adsorbed, or the pH is adjusted. Then, the hot water W returns to the bathtub 1 via the hot water outflow pipe 12 again.

このようにろ過手段によつて清浄化される。 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, hot water W is supplied from the ozone mixer 16.
Ozone is injected and mixed inside.

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
り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, ozone's masking action masks the malodorous components of hot water, and its oxidizing action decomposes the malodorous components. Alternatively, it is sterilized or sterilized by the bactericidal action of ozone.

加えて溶存オゾンにより好気性微生物を活性化
し、有機物を分離、除去する等々である。
In addition, dissolved ozone activates aerobic microorganisms and separates 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。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。
By the way, ozone is injected and mixed before the filtration device 3. 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、溶存オゾ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 present in the filter media, activation by dissolved ozone is further promoted, 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の最上部で気液分
離器17により大気中へ気体となつて分離できる
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 converted into gas by the gas-liquid separator 17 at the top of the filtration device 3 into the atmosphere. Since excess ozone can be separated by water, 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ツクも防止
される。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28が空気出口27を開放
して実施される。
In addition, air lock due to excess ozone is also prevented. The gas-liquid separation operation in this example is performed by lowering the float 25 and causing the nozzle pin 28 to open the air outlet 27, as shown in FIG.

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イス型のオゾン混合器16
の作用を簡述すると、流入側18と流出側19の
間にオリフイス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-
流入側18方向から圧力Poで送水した時、直径
d2-のオリフイス部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Piと、直径Di
の流出側19での圧力P2は次式で表わされる。
Furthermore, the orifice type ozone mixer 16 of this example
To briefly explain the operation, an orifice 20 is formed between the inflow side 18 and the outflow side 19, and an ozone injection pipe end 22 is connected to the expansion part 21. When water is fed from 18 directions on the inlet side of diameter D 2- with pressure Po, the diameter
The pressure loss P 2- due to the orifice part 20 of d 2- , the negative pressure Pi generated in the expansion part 21 of diameter D 2 , and the diameter Di
The pressure P 2 at the outlet side 19 of is expressed by the following equation.

Po=P2-+(−Pi)+P2 この膨張部21での負圧Piは、オリフイス部2
0による流速の上昇に伴なうカルマン渦が原因で
発生するが、 D2->D2>Di>d2->di を適度に設定することにより、オゾン流入管端2
2が大気圧より低い値になる。
Po=P 2- + (-Pi) + P 2 This negative pressure Pi in the expansion part 21 is
This is caused by the Karman vortex that accompanies the increase in flow velocity due to
2 becomes a value lower than atmospheric pressure.

即ちオリフイス部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上の比重が軽くな
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、より大
量のオゾンが吸入される。
That is, when a jet is generated by the orifice part 20 and a negative pressure is generated in the expansion part 21, and ozone is inhaled from the ozone injection pipe 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 a larger amount of ozone is sucked.

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ヤンバー3
0を形成し、ノズル31を対向させる。オゾン注
入管15は上記チヤンバー30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. 4,
A small-diameter branch pipe 28 is branched from the hot water inflow pipe 6, and a pump 29 is arranged in the middle, and the injection chamber 3
0 is formed and the nozzles 31 are opposed to each other. The ozone injection pipe 15 is connected to the chamber 30. According to this, ozone is discharged from the nozzle 31 facing the hot water 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、混合するに当たり最終段のろ過装
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ろ材の、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。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, it has the function of promoting the reaction between ozone and malodorous components. The function of the filter media can be further promoted, and deodorization can be better achieved.Since many aerobic microorganisms exist in the filtration device, aerobic microorganisms near the filter media can be further activated, and organic matter can be further decomposed and removed. can. Ozone injection and filtration function can be organically correlated.

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、仮に誤つて過
剰に注入しても、オゾン混合器16の下流側、即
ち浴槽1に至らない段階で分離してしまうので人
体に対する通性影響を可及的に排除できる。加え
てエアーロツクを防止でき、温水循環に支障がな
い等実用上各種の利を呈する。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 it reaches the downstream side of the ozone mixer 16, that is, before it reaches the bathtub 1. Therefore, facultative 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 not interfering with hot water circulation. More specifically,
Ozone is not directly injected into the bathtub hot water, but is forcibly mixed directly before the final filtration means, so the sterilization and purification effect of ozone can be used more effectively and safely for the human body. It is possible.

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

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図はオリフイス型のオゾ
ン混合器の例図、第3図は気液分離器の例図、第
4図は対向流吐出型のオゾン混合器の例図であ
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、16はオゾン混合
器、17は気液分離器である。
The accompanying drawings show embodiments of the present invention, and FIG. 1 is a longitudinal sectional view showing the whole, FIG. 2 is an example of an orifice type ozone mixer, FIG. 3 is an example of a gas-liquid separator, and FIG. The figure shows an example of a counterflow discharge type ozone mixer. It is a liquid separator.

Claims (1)

【特許請求の範囲】 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過熱し、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
ようにすると共に、上記オゾン注入位置より下流
位置に於いて上記温水中に発生したエアを分離し
てから循環させるようにした事を特徴とする浴槽
温水の循環方法。 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を注入せしめる為り温水流入管系
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正常循
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。 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。
[Scope of Claims] 1. Inhale hot water from a bathtub, then filter it, or filter and activate the hot water and keep it heated, and then let it flow out to the bathtub side to purify or purify, activate and purify the hot water. In a bathtub hot water purification method in which the temperature is kept constant and ozone is injected into the hot water during the hot water circulation process; A method for circulating hot water in a bathtub, characterized in that air generated in the warm water is separated at a position downstream from the ozone injection position and then circulated. . 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 carrying out the final stage filtration action of the filtration means, and a hot water inflow pipe system 6 for injecting the hot water W from the filtration device 3 It has a hot water circulation system consisting of a hot water outflow pipe system 12 and a circulation pump 9 for discharging W into the bathtub 1, and an ozone mixer for injecting ozone generated in the ozone generator 14 into the hot water circulation system. In a bathtub hot water normal circulation system having: The ozone mixer 16 connected to the ozone generator 14 via the ozone injection pipe 15 corresponds to the primary side with respect to the position of the final stage filtration device 3. A gas-liquid separator 17 is disposed in the hot water inflow pipe system 6 and is located downstream of the ozone mixer 16.
A bathtub warm water purifying circulation device characterized by being equipped with. 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.
JP63084406A 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
JP63084406A 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
JP63084406A 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 JPH01258795A (en) 1989-10-16
JPH0376196B2 true JPH0376196B2 (en) 1991-12-04

Family

ID=13829707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63084406A 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)

Families Citing this family (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
JP6967037B2 (en) * 2019-06-21 2021-11-17 東京都 Water treatment system and water treatment method

Also Published As

Publication number Publication date
JPH01258795A (en) 1989-10-16

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