JP2001170636A - Water cleaning device - Google Patents

Water cleaning device

Info

Publication number
JP2001170636A
JP2001170636A JP35428899A JP35428899A JP2001170636A JP 2001170636 A JP2001170636 A JP 2001170636A JP 35428899 A JP35428899 A JP 35428899A JP 35428899 A JP35428899 A JP 35428899A JP 2001170636 A JP2001170636 A JP 2001170636A
Authority
JP
Japan
Prior art keywords
water
chlorine compound
chlorine
removing means
electrolytic
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.)
Pending
Application number
JP35428899A
Other languages
Japanese (ja)
Inventor
Takemi Oketa
岳見 桶田
Keijiro Kunimoto
啓次郎 国本
Tomohide Matsumoto
朋秀 松本
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP35428899A priority Critical patent/JP2001170636A/en
Publication of JP2001170636A publication Critical patent/JP2001170636A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To control residual chlorine concentration in a bath time, in a water cleaning device for producing electrolytic water by electrolysis and sterilizing and purifying water. SOLUTION: An adapter 20 having an inflow and outflow port of water, a pump 21 for feeding water, an electrolytic means 23 having a filter 22 removable suspended matter in water, valves 24, 25 and 26 for controlling inflow into and outflow of water from the electrolytic means, and a chlorine compound removing means 27, are provided in a circulation flow path 19. Since a water circuit by which water does not pass through the electrolytic means 23 but water is made to pass thorough the chlorine compound removing means 27 by switching the valves 24, 25 and 26, can be formed, the residual chlorine concentration in water can be controlled while sterilization performance by electrolyzed water is maintained.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、家庭用水道水、浴
槽水などの浄化、特に電気分解で生成した電解水による
水の殺菌に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to purification of domestic tap water and bathtub water, and more particularly to sterilization of water by electrolyzed water generated by electrolysis.

【0002】[0002]

【従来の技術】従来のこの種の水浄化装置は特開平11
−77055号公報に記載されているようなものが一般
的であった。この水浄化装置は図7に示すように、浴槽
1と、浴槽1に入口2と出口3を有する水の循環流路4
に、水を送り込むポンプ5と、フィルター6と、電解槽
7と、殺菌成分除去手段として脱塩素剤8(亜硫酸カル
シウム)が配置されており、電解槽7の上下流側に位置
するバルブ9、10と脱塩素剤8の上下流側にあるバル
ブ11、12と、脱塩素剤と並列に循環路に設けられた
バルブ13を備えている。また、電解槽7に食塩水14
を供給するバルブ15及び16が配管17に備えられて
おり、配管17から電解槽7に水道水及び食塩水を供給
可能としている。
2. Description of the Related Art A conventional water purification apparatus of this type is disclosed in
What was described in -77055 was common. As shown in FIG. 7, this water purifying device has a bathtub 1 and a water circulation flow path 4 having an inlet 2 and an outlet 3 in the bathtub 1.
, A pump 5, a filter 6, an electrolytic cell 7, and a dechlorinating agent 8 (calcium sulfite) as a disinfecting component removing means, and a valve 9, which is located upstream and downstream of the electrolytic cell 7, There are provided valves 11 and 12 on the upstream and downstream sides of the dechlorinating agent 10 and the dechlorinating agent 8, and a valve 13 provided in the circulation path in parallel with the dechlorinating agent. Also, a saline solution 14 is placed in the electrolytic cell 7.
The pipes 17 are provided with valves 15 and 16 for supplying tap water and salt water from the pipe 17 to the electrolytic cell 7.

【0003】そして、水浄化の際は、ポンプ5を動か
し、浴槽1内の水が、入口2から入り、フィルター6を
通過し、浴槽に戻素ことで湯垢などの除去を行う。そし
て、水の殺菌を行う場合は、電解槽7の上流及び下流側
のバルブ9、10を開き、電解槽7に水を充満させ、そ
の後、バルブ9、10を閉じ、配管17上のバルブ1
5、16を開き、食塩水14を電解槽7に送り込んで電
気分解により次亜塩素酸を生成する。ここで生成した次
亜塩素酸を出口から浴槽1に送り込み、浴槽1内の水の
殺菌を行っていた。さらに、殺菌終了後は、脱塩素剤8
の上流と下流側のバルブ11、12を開き、浴槽1内の
水を循環し、脱塩素剤と接触させることで、浴槽水の次
亜塩素酸を除去し、入浴に用いていた。
At the time of water purification, the pump 5 is operated to allow water in the bathtub 1 to enter through the inlet 2, pass through the filter 6, and return to the bathtub to remove scale and the like. Then, when sterilizing water, the valves 9 and 10 on the upstream and downstream sides of the electrolytic cell 7 are opened to fill the electrolytic cell 7 with water, and then the valves 9 and 10 are closed.
5 and 16 are opened, and the saline solution 14 is sent to the electrolytic cell 7 to generate hypochlorous acid by electrolysis. The hypochlorous acid generated here was sent to the bathtub 1 from the outlet, and the water in the bathtub 1 was sterilized. Further, after the sterilization is completed, a dechlorinating agent 8
By opening the valves 11 and 12 on the upstream and downstream sides of the bathtub, the water in the bathtub 1 is circulated and brought into contact with a dechlorinating agent to remove hypochlorous acid in the bathtub water and use it for bathing.

【0004】[0004]

【発明が解決しようとする課題】しかしながら上記従来
の水浄化装置では以下のような課題があった。
However, the above-mentioned conventional water purification apparatus has the following problems.

【0005】(1)浴槽水を連続して使用する場合、殺
菌後毎に殺菌成分を除去すると、生残した細菌が直ちに
増殖を開始し、浴槽内の水に濁りが生じる。
(1) In the case of continuously using bath water, if the sterilizing component is removed after each sterilization, the surviving bacteria immediately start to proliferate, and the water in the bath becomes turbid.

【0006】(2)殺菌後に殺菌成分を除去すること
で、殺菌後の水の塩素臭が減少する反面、水中の細菌等
の微生物が殺菌成分と接触する時間が短くなるので、殺
菌効果が減少する。
(2) By removing the germicidal components after sterilization, the chlorine odor of the sterilized water is reduced, but the time for microorganisms such as bacteria in the water to contact the germicidal components is shortened, so that the germicidal effect is reduced. I do.

【0007】(3)浴槽水中の殺菌成分を除去した後、
再び殺菌成分を注入し、浴槽水の殺菌を行う場合、殺菌
力が十分に得られるレベルに殺菌成分濃度を維持するに
は、毎回一定量の殺菌成分を注入する必要があるので、
殺菌成分の消費量が増加する。
(3) After removing the sterilizing components in the bath water,
When injecting the bactericidal component again and sterilizing bath water, it is necessary to inject a certain amount of bactericidal component each time to maintain the bactericidal component concentration at a level where sufficient bactericidal power is obtained,
The consumption of sterilizing components increases.

【0008】[0008]

【課題を解決するための手段】本発明は上記課題を解決
するため、循環流路に浴槽内の水を循環手段と、内部に
少なくとも一対の電極を有し、電気分解により塩素化合
物を含む電解水を生成可能な電解手段と、水の塩素化合
物を除去可能な塩素化合物除去手段とを備え、前記電解
水を水に添加することで連続的に浴槽内の水の殺菌・浄
化を行う構成において、制御手段により循環手段、電解
手段、塩素化合物除去手段のうち少なくとも一つの動作
を制御することで殺菌中一定時間だけ水中の塩素化合物
の濃度を低下させる動作制御を行う。
In order to solve the above-mentioned problems, the present invention has a means for circulating water in a bathtub in a circulation flow path and at least a pair of electrodes therein, and the electrolytic solution containing a chlorine compound by electrolysis. In a configuration comprising an electrolytic means capable of generating water and a chlorine compound removing means capable of removing a chlorine compound of water, the sterilizing and purifying water in the bathtub is continuously performed by adding the electrolytic water to water. By controlling at least one of the circulating means, the electrolytic means, and the chlorine compound removing means by the control means, the operation control for reducing the concentration of the chlorine compound in the water for a certain time during the sterilization is performed.

【0009】上記発明によれば、入浴時以外の浴槽水に
は殺菌効果を有する電解水を常に一定レベル以上の濃度
で維持できるので、水中の細菌などの微生物に常に酸性
物質でダメージを与えることができるので、少量の電解
水で最大の殺菌(または増殖抑制)効果を得ることがで
きると同時に、一日に複数回の電解水の添加を行う制御
では、電解水を注入し、殺菌終了後から次の殺菌までに
入浴をしないと判断される場合には、水中の塩素化合物
を除去せず放置することで、次の殺菌までの間、水中の
細菌などの微生物に長時間ダメージを与えることができ
るので、効果的な殺菌ができると同時に、水中への塩素
化合物の残留が期待できるので、次の殺菌時の電解水の
添加量を減少しても同等の効果を期待することができ
る。
According to the present invention, electrolyzed water having a bactericidal effect can always be maintained at a concentration equal to or higher than a certain level in bath water other than during bathing, so that microorganisms such as bacteria in the water are always damaged by acidic substances. As a result, the maximum sterilization (or growth suppression) effect can be obtained with a small amount of electrolyzed water. If it is determined that you will not take a bath before the next sterilization, leave the chlorine compound in the water without removing it and leave it for a long time to damage microorganisms such as bacteria in the water until the next sterilization Therefore, effective sterilization can be performed, and at the same time, a chlorine compound can be expected to remain in water. Therefore, the same effect can be expected even if the amount of electrolyzed water added during the next sterilization is reduced.

【0010】[0010]

【発明の実施の形態】本発明の請求項1にかかる水浄化
装置は、循環流路に浴槽内の水を循環手段と、内部に少
なくとも一対の電極を有し、電気分解により塩素化合物
を含む電解水を生成可能な電解手段と、水の塩素化合物
を除去可能な塩素化合物除去手段とを備え、前記電解水
を水に添加することで連続的に浴槽内の水の殺菌・浄化
を行う構成において、制御手段により循環手段、電解手
段、塩素化合物除去手段のうち少なくとも一つの動作を
制御することで殺菌中一定時間だけ水中の塩素化合物の
濃度を低下させる動作制御を行うものである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A water purifying apparatus according to a first aspect of the present invention has a circulating means for circulating water in a bathtub in a circulating flow path and at least a pair of electrodes inside, and contains a chlorine compound by electrolysis. A configuration including electrolysis means capable of generating electrolyzed water and chlorine compound removal means capable of removing a chlorine compound of water, and continuously sterilizing and purifying water in a bathtub by adding the electrolyzed water to water. Wherein the control means controls at least one of the circulating means, the electrolytic means, and the chlorine compound removing means to control the operation of reducing the concentration of the chlorine compound in the water for a certain period of time during sterilization.

【0011】そして、入浴時以外の浴槽水には殺菌効果
を有する電解水を常に一定レベル以上の濃度で維持でき
るので、水中の細菌などの微生物に常に酸性物質でダメ
ージを与えることができるので、少量の電解水で最大の
殺菌(または増殖抑制)効果を得ることができる。
[0011] Since electrolyzed water having a bactericidal effect can always be maintained at a concentration equal to or higher than a certain level in bath water other than when bathing, microorganisms such as bacteria in the water can always be damaged by acidic substances. The maximum sterilization (or growth suppression) effect can be obtained with a small amount of electrolyzed water.

【0012】本発明の請求項2にかかる水浄化装置は、
塩素供給手段への水の流入出を制御可能な流路切換手段
を有している。
[0012] The water purifying apparatus according to claim 2 of the present invention comprises:
It has a flow path switching means capable of controlling the flow of water into and out of the chlorine supply means.

【0013】本発明の請求項3にかかる水浄化装置は、
前記電解手段と塩素化合物除去手段を並列に設置したこ
とを特徴としている。
[0013] The water purifying apparatus according to claim 3 of the present invention comprises:
The electrolysis means and the chlorine compound removing means are provided in parallel.

【0014】そして、電解水を浴槽内に注入する際、電
解水を塩素化合物除去手段に通過させずに、浴槽に供給
できるので、電解手段で生成した電解水を有効に使用で
きる。
When the electrolyzed water is injected into the bath, the electrolyzed water can be supplied to the bath without passing through the chlorine compound removing means, so that the electrolyzed water generated by the electrolyzing means can be used effectively.

【0015】本発明の請求項4にかかる水浄化装置は、
制御手段により、浴槽内への注水中または注水後のいず
れかの時点で塩素化合物除去手段により水中の塩素化合
物を除去する制御を行うものである。
[0015] The water purifying apparatus according to claim 4 of the present invention comprises:
The control means controls the removal of chlorine compounds in the water by the chlorine compound removal means at any time after or after the water is injected into the bathtub.

【0016】そして、注水直後(注湯も含む)に存在す
る水道水中の塩素化合物の除去も可能となり、注水直後
から快適な入浴ができる。
[0016] It is also possible to remove chlorine compounds in tap water immediately after pouring (including pouring), so that comfortable bathing can be performed immediately after pouring.

【0017】本発明の請求項5にかかる水浄化装置は、
塩素化合物除去手段は、内部に還元剤を貯溜し、電解水
または被処理水に接触可能な構成としている。
According to a fifth aspect of the present invention, there is provided a water purifying apparatus.
The chlorine compound removing means is configured to store a reducing agent therein so as to be able to contact the electrolyzed water or the water to be treated.

【0018】そして、還元剤を使用することにより安価
かつ効果的な塩素化合物の除去が可能となる。
The use of the reducing agent makes it possible to remove the chlorine compound inexpensively and effectively.

【0019】本発明の請求項6にかかる水浄化装置は、
塩素化合物除去手段が、電解水中の塩素化合物を分解可
能な触媒で有ることを特徴としている。
[0019] The water purifying apparatus according to claim 6 of the present invention comprises:
The chlorine compound removing means is a catalyst capable of decomposing a chlorine compound in the electrolytic water.

【0020】そして、特定の触媒を使用することで、長
期間塩素化合物の除去性能を維持できるので、安定した
塩素化合物除去性能を得ることができる。
By using a specific catalyst, the chlorine compound removal performance can be maintained for a long period of time, so that a stable chlorine compound removal performance can be obtained.

【0021】本発明の請求項7にかかる水浄化装置は、
塩素化合物除去手段は、電解水中の塩素化合物を吸着可
能な吸着材であることを特徴としている。
[0021] The water purifying apparatus according to claim 7 of the present invention comprises:
The chlorine compound removing means is characterized by being an adsorbent capable of adsorbing a chlorine compound in the electrolytic water.

【0022】そして、塩素化合物だけでなく、塩素化合
物と同時の水中の有機物も除去可能なのでこれら由来の
臭気を減少させることができる。
Since not only chlorine compounds but also organic substances in water at the same time as chlorine compounds can be removed, odors derived from these substances can be reduced.

【0023】本発明の請求項8にかかる水浄化装置は、
塩素化合物除去手段は、超音波を発生可能な超音波発生
手段であり、超音波により塩素化合物を分解することを
特徴としている。
[0023] The water purification apparatus according to claim 8 of the present invention comprises:
The chlorine compound removing means is an ultrasonic wave generating means capable of generating ultrasonic waves, and is characterized by decomposing chlorine compounds by ultrasonic waves.

【0024】そして、超音波発生装置で超音波を発生さ
せて水中の塩素化合物を除去することで、塩素化合物除
去手段の構成の簡素化が図れるだけでなく、水のクラス
ターを小さくすることができるので、肌に優しい水での
入浴をかのうとする。
By removing the chlorine compounds in the water by generating ultrasonic waves with the ultrasonic generator, not only the structure of the chlorine compound removing means can be simplified, but also the cluster of water can be reduced. So try bathing in water that is gentle on your skin.

【0025】本発明の請求項9にかかる水浄化装置は、
塩素化合物除去手段は、紫外線を照射する紫外線照射手
段であり、紫外線によって塩素化合物を分解することを
特徴としている。
According to a ninth aspect of the present invention, there is provided a water purifying apparatus.
The chlorine compound removing means is an ultraviolet light irradiating means for irradiating ultraviolet light, and is characterized in that the chlorine compound is decomposed by the ultraviolet light.

【0026】そして、紫外線で塩素化合物を分解できる
と同時に水中の細菌を紫外線で殺菌できるので効果的な
殺菌ができる。
Since the chlorine compounds can be decomposed by ultraviolet rays and bacteria in water can be sterilized by ultraviolet rays, effective sterilization can be achieved.

【0027】[0027]

【実施例】以下、本発明の実施例について図面を用いて
説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0028】(実施例1)図1は本発明の実施例1の水
浄化装置を示す構成図である。
(Embodiment 1) FIG. 1 is a configuration diagram showing a water purification apparatus according to Embodiment 1 of the present invention.

【0029】図1において、18は浴槽で、循環流路1
9には、水の流入および流出口を有するアダプター20
と、水を循環流路19に送り込むポンプ21と、水中の
懸濁物質を除去可能なフィルター22を有する電解手段
23と、電解手段23および塩素化合物除去手段への水
の流入出を制御する流路切換手段の弁24、25、26
と、塩素化合物除去手段27を有している。また、弁2
4は流路28で弁26に接続された排水路29と接続さ
れると同時に、流路30で電解手段23に接続されてい
る。ここで、電解手段23と塩素化合物除去手段37は
循環流路19上で並列に配置されている。
In FIG. 1, reference numeral 18 denotes a bathtub,
9 includes an adapter 20 having an inlet and an outlet for water.
A pump 21 for feeding water into the circulation flow path 19; an electrolytic means 23 having a filter 22 capable of removing suspended substances in the water; and a flow for controlling inflow and outflow of water to the electrolytic means 23 and the chlorine compound removing means. Valves 24, 25, 26 of path switching means
And chlorine compound removing means 27. Valve 2
The channel 4 is connected to a drainage channel 29 connected to the valve 26 via a channel 28 and at the same time is connected to the electrolysis means 23 via a channel 30. Here, the electrolytic means 23 and the chlorine compound removing means 37 are arranged in parallel on the circulation channel 19.

【0030】電解手段23は、内部にフィルター22を
有し、フィルター22の下流側にバイパス路31を設
け、ここに電極32、33を備えている。そして、食塩
タンク34と電解手段23とを結ぶ食塩流路35と食塩
タンク34と循環流路19を結ぶ給水路36には食塩タ
ンク34に循環流路19の水を送り込むポンプ37が備
えられている。弁24、25、26、ポンプ21、37
の動作制御および電極32、33への通電制御は制御装
置38で行っている。この制御装置38で、入浴したい
時間帯、入浴人数を設定することで、入浴したい時間帯
に濁りのないきれいな水に入浴可能としている。
The electrolytic means 23 has a filter 22 inside, and a bypass 31 is provided downstream of the filter 22, and electrodes 32 and 33 are provided here. A pump 37 for feeding the water in the circulation channel 19 into the salt tank 34 is provided in a salt channel 35 connecting the salt tank 34 and the electrolysis means 23 and a water supply channel 36 connecting the salt tank 34 and the circulation channel 19. I have. Valves 24, 25, 26, pumps 21, 37
Is controlled by the control device 38. By setting a time zone for taking a bath and the number of people taking a bath with the control device 38, it is possible to take a bath with clear water without turbidity in a time zone for taking a bath.

【0031】また、フィルター22はプリーツ状フィル
ターを用いており、外側から入った水が濾過され、内部
の中空部39に入る構成となっており、電極32、33
の間には隔膜40を配置している。
The filter 22 is a pleated filter, in which water entering from the outside is filtered and enters a hollow portion 39 inside.
A diaphragm 40 is disposed between the two.

【0032】図2A〜Cは、塩素化合物除去手段27の
構成図であり、本実施例では同図Aの構成の塩素化合物
除去手段を用いた。タンク41内には還元剤のアスコル
ビン酸水溶液44が充填されており、アスコルビン酸水
溶液44はポンプ42により流路43を通って循環流路
19に送り込まれる。また、アスコルビン酸水溶液44
の供給制御は弁24、25、26及びポンプ42を制御
装置38で制御して行っている。本実施例においては、
このアスコルビン酸水溶液に酸(クエン酸、塩酸など)
を加え、水溶液中の細菌の繁殖によるアスコルビン酸の
分解を防いでいる。
FIGS. 2A to 2C are diagrams showing the structure of the chlorine compound removing means 27. In this embodiment, the chlorine compound removing means having the structure shown in FIG. 2A is used. The tank 41 is filled with an aqueous solution of ascorbic acid 44 as a reducing agent, and the aqueous solution of ascorbic acid 44 is sent to the circulation channel 19 through the channel 43 by the pump 42. In addition, ascorbic acid aqueous solution 44
Is controlled by controlling the valves 24, 25, 26 and the pump 42 by the control device 38. In this embodiment,
Add acid (citric acid, hydrochloric acid, etc.) to this ascorbic acid aqueous solution
To prevent the decomposition of ascorbic acid due to the propagation of bacteria in the aqueous solution.

【0033】なお、この流路42に循環流路19からの
水の逆流を防ぐ逆止弁を備えることで、循環流路19中
の水のタンク41への流入を抑えることができるので、
必要に応じ設置することが望ましい。
By providing a check valve for preventing the backflow of water from the circulation passage 19 in the passage 42, the flow of water into the tank 41 in the circulation passage 19 can be suppressed.
It is desirable to install as necessary.

【0034】次に動作、作用について説明する。浴槽1
8内の水はポンプ21によりアダプタ20から循環流路
19に送り込まれる。その後循環流路19の水は、電解
手段23に入り、内部のフィルター22で水中に含まれ
る懸濁物質が濾過除去される。そして、水は循環流路1
9からアダプター20に戻り、浴槽18内に排出される
ことで、水の濁度一定レベル以下に保っている。しか
し、この動作だけだと、水中の細菌の増殖を抑えること
ができないので、水が濁る場合が有る。このようなケー
スを想定して、定期的に電気分解を行い電解水(次亜塩
素酸、次亜塩素酸イオン、活性塩素などの塩素化合物を
含む水)を生成し、水の殺菌を行っている。つまり、ポ
ンプ21が停止した状態で、ポンプ37を動かし、食塩
タンク34内の食塩水を食塩流路35から電解手段23
の電極32、33間に送り込む。その後、電極32、3
3に直流電流を引加し、電気分解を行う。電気分解では
電解水だけでなく酸素及び水素の気泡も発生する。ここ
で発生した気泡は、電極32より上側のバイパス路31
に排出され、バイパス路31には上方向への水の流れが
発生する。この流れにより、フィルター22の下流側の
中空部39とバイパス路31との間に循環流が発生さ
せ、この中空部39とバイパス路31でl構成される空
間で循環を行いながら電気分解を行うことで、電解水の
生成効率が向上する。電解水を生成した後、弁25、2
6を切換え、ポンプ21を始動することで、バイパス路
31及び中空部39に溜まっている電解水は浴槽18へ
送り込まれ、殺菌が行われる。この時、電解水は塩素化
合物除去手段27を通過しない水回路としているので、
電気分解で生成した電解水中の次亜塩素酸等の殺菌性を
有する塩素化合物が除去されずに浴槽18に供給可能と
なるので、電解水を有効に使用し、殺菌性能を向上させ
ることができる。
Next, the operation and operation will be described. Bathtub 1
The water in 8 is sent from pump 20 to circulation channel 19 by pump 21. Thereafter, the water in the circulation flow path 19 enters the electrolysis means 23, and the suspended matter contained in the water is filtered off by the filter 22 inside. And water is in circulation channel 1
By returning from 9 to the adapter 20 and being discharged into the bath 18, the turbidity of the water is kept below a certain level. However, this operation alone cannot suppress the growth of bacteria in the water, so that the water may become turbid. Assuming such a case, electrolysis is performed periodically to generate electrolyzed water (water containing chlorine compounds such as hypochlorous acid, hypochlorite ions, and active chlorine), and sterilize the water. I have. That is, in a state where the pump 21 is stopped, the pump 37 is operated, and the salt solution in the salt tank 34 is discharged from the salt channel 35 through the electrolysis means 23.
Between the electrodes 32 and 33. Then, the electrodes 32, 3
A direct current is applied to 3 to perform electrolysis. In electrolysis, not only electrolyzed water but also oxygen and hydrogen bubbles are generated. The air bubbles generated here pass through the bypass passage 31 above the electrode 32.
And water flows upward in the bypass passage 31. By this flow, a circulating flow is generated between the hollow portion 39 on the downstream side of the filter 22 and the bypass passage 31, and electrolysis is performed while circulating in a space formed by the hollow portion 39 and the bypass passage 31. Thereby, the generation efficiency of the electrolyzed water is improved. After generating the electrolyzed water, the valves 25, 2
By switching 6 and starting the pump 21, the electrolyzed water stored in the bypass 31 and the hollow portion 39 is sent to the bath 18, and sterilization is performed. At this time, since the electrolyzed water has a water circuit that does not pass through the chlorine compound removing means 27,
Since a chlorine compound having a sterilizing property such as hypochlorous acid in the electrolyzed water generated by the electrolysis can be supplied to the bath 18 without being removed, the electrolyzed water can be effectively used, and the sterilizing performance can be improved. .

【0035】このようにして、浴槽18内の水の殺菌を
行っているが、水中の細菌は水の電解水濃度、(特に残
留塩素濃度)が低下すると直ちに増殖を開始し、浴槽1
8内の水が濁りを生じる。従って、浴槽水中の細菌数が
目標レベル以下に低下しても水中の残留塩素濃度を一定
レベル(具体的には、全残留塩素濃度を0.2ppm以
上、好ましくは0.3ppm以上に保つ)に制御する必要
がある。しかし、浴槽水(入浴水)に電解水を添加し、
添加直後の残留塩素濃度が1.0〜2.0ppmになるよ
うに調整しても、添加後数時間で0.2ppm以下にまで
低下してしまう。従って、1日に2回以上(好ましくは
3回程度)電解水の添加が必要となる。しかし、残留塩
素濃度が常に0.2ppm以上になるように電解水を添加
した場合、水質の違いまたは入浴負荷の違いによって入
浴時間帯の浴槽水中の残留塩素濃度が1.0ppm近くに
なる場合が有る。1.0ppmの残留塩素濃度では、入浴
者は容易に塩素臭を感じ、塩素臭を嫌がる入浴者は不快
に感じたり、皮膚に「チクチク」とした刺激を感じる入
浴者が出てくる場合が有る。電解水で殺菌しているの
で、衛生的な問題は無いにせよ、ニオイや刺激感を好ま
ない入浴者のことを考慮すれば、制御手段で入浴時間帯
が設定されている時間帯は水中の残留塩素濃度を除去す
ることが好ましい。そこで、設定されている入浴時間帯
以前に浴槽18内の水の残留塩素濃度を低下させるため
以下の動作を行うようにプログラムしておく。すなわ
ち、入浴時間帯開始前に弁25、26を切換え、ポンプ
21で循環流路19に送り込まれた水が、塩素化合物除
去手段27を通り、弁25を通ってアダプター20から
再び浴槽18内に戻る構成とする。塩素化合物除去手段
27の詳細な構成は図2Aに示したように、ポンプ42
の働きにより、タンク41内のアスコルビン酸の一定量
(2mg/L以上、20mg/L以下)を循環流路19に注
入する。この動作により、浴槽18内の水の残留塩素濃
度は0.2ppm以下(場合によっては0.1ppm以下)ま
で低下させることができ、入浴中の塩素臭やチクチクと
した皮膚刺激を低減または無くすことができる。
In this manner, the water in the bathtub 18 is sterilized. Bacteria in the water start to proliferate immediately when the concentration of electrolyzed water in the water (particularly, the residual chlorine concentration) is reduced.
The water in 8 causes turbidity. Therefore, even if the number of bacteria in the bathtub water falls below the target level, the residual chlorine concentration in the water is kept at a constant level (specifically, the total residual chlorine concentration is kept at 0.2 ppm or more, preferably 0.3 ppm or more). You need to control. However, adding electrolyzed water to the bath water (bathing water)
Even if the residual chlorine concentration immediately after the addition is adjusted to be 1.0 to 2.0 ppm, the concentration will be reduced to 0.2 ppm or less within several hours after the addition. Therefore, it is necessary to add electrolytic water twice or more (preferably about three times) a day. However, when electrolyzed water is added so that the residual chlorine concentration is always 0.2 ppm or more, the residual chlorine concentration in the bath water during the bathing time may be close to 1.0 ppm due to a difference in water quality or a difference in bathing load. Yes. At a residual chlorine concentration of 1.0 ppm, bathers easily feel a chlorine odor, and bathers who do not like the chlorine odor may feel uncomfortable, or some bathers may feel a tingling sensation on the skin . Because it is sterilized with electrolyzed water, there is no hygienic problem, but considering bathers who do not like smell or irritation, the time period when the bathing time period is set by the control means is underwater. It is preferable to remove the residual chlorine concentration. Therefore, the following operation is programmed to reduce the residual chlorine concentration of the water in the bathtub 18 before the set bathing time period. That is, before the start of the bathing time, the valves 25 and 26 are switched, and the water sent to the circulation flow path 19 by the pump 21 passes through the chlorine compound removing means 27, passes through the valve 25, and returns to the bathtub 18 from the adapter 20. Return to the configuration. The detailed structure of the chlorine compound removing means 27 is as shown in FIG.
A certain amount (2 mg / L or more and 20 mg / L or less) of ascorbic acid in the tank 41 is injected into the circulation flow channel 19 by the action of (1). By this operation, the residual chlorine concentration of the water in the bathtub 18 can be reduced to 0.2 ppm or less (in some cases, 0.1 ppm or less) to reduce or eliminate chlorine odor and tingling skin irritation during bathing. Can be.

【0036】また、湯はり直後の水には水道水中に含ま
れる残留塩素のため、塩素臭や皮膚刺激が有る。従っ
て、湯はり中、また湯はり直後に弁25、26及びポン
プ21、42の動作を制御し、浴槽18内の水にアスコ
ルビン酸を添加することで、湯はり直後でもの塩素臭や
チクチクとした皮膚刺激を低減または無くすことができ
る。
The water immediately after the hot water has chlorine odor and skin irritation due to residual chlorine contained in tap water. Therefore, the operation of the valves 25 and 26 and the pumps 21 and 42 is controlled during and immediately after the hot water is added, and ascorbic acid is added to the water in the bathtub 18 to reduce chlorine odor and tingling immediately after the hot water. The reduced skin irritation can be reduced or eliminated.

【0037】なお、本実施例では、電極32、33間に
隔膜40を配置し、電極33の上流に弁24を設置して
いるので、浴槽18内の水のpH(水素イオン濃度)を低
下させ、酸性水を生成可能である。すなわち、制御手段
38で、弁24を切換え、ポンプ21で送り込まれた水
が、弁24、流路30を通過し、電解手段23から循環
流路19を介して浴槽18に戻る水回路を形成し、水を
循環させながら、電極33を陽極とし、電気分解を行
う。電気分解により陽極側ではpHが低下し、酸性水が得
られるので、浴槽18内の水のpHが低下し、酸性水で入
浴可能となる。一方、陰極32側では、pHが高いアルカ
リ水ができるので、フィルター22に堆積した有機物の
汚れを分解することができるので、フィルター22の寿
命を延長することができる。そして、電解終了後は、弁
24、25、26を切換え、ポンプ21を始動し、排水
路28からフィルター22の下流側の空間39及びバイ
パス路31に溜まったアルカリ水を排出し、再び弁2
4、25、26を切換え、通常の濾過運転に戻る。
In this embodiment, since the diaphragm 40 is arranged between the electrodes 32 and 33 and the valve 24 is installed upstream of the electrode 33, the pH (hydrogen ion concentration) of the water in the bathtub 18 is lowered. To produce acidic water. That is, the control means 38 switches the valve 24 to form a water circuit in which the water fed by the pump 21 passes through the valve 24 and the flow path 30 and returns from the electrolytic means 23 to the bathtub 18 via the circulation flow path 19. Then, while circulating water, electrolysis is performed using the electrode 33 as an anode. Since the pH is lowered on the anode side by the electrolysis and acidic water is obtained, the pH of the water in the bathtub 18 is lowered, and the bath can be bathed with acidic water. On the other hand, since alkaline water having a high pH is produced on the cathode 32 side, organic dirt deposited on the filter 22 can be decomposed, so that the life of the filter 22 can be extended. After the electrolysis is completed, the valves 24, 25, and 26 are switched, the pump 21 is started, the alkaline water accumulated in the space 39 on the downstream side of the filter 22 and the bypass passage 31 is discharged from the drainage passage 28, and the valve 2 is turned on again.
Switch between 4, 25 and 26 and return to normal filtration operation.

【0038】また、この操作で得られたアルカリ水を用
いてフィルター22の逆流洗浄を行うとフィルター22
の寿命の更なる延長が可能となる。
When the backwash of the filter 22 is performed using the alkaline water obtained by this operation,
Can be further extended.

【0039】また、電気分解で得られる酸性水には残留
塩素が含まれるので、電解後は、弁24、25、26を
切換え、再び水を塩素化合物除去手段27に通過させる
ことで、アスコルビン酸で水中の残留塩素を除去するこ
とで、酸性水によるアストリンゼン効果とアスコルビン
酸による残留塩素除去効果により快適かつ美容に良い入
浴が可能になる。
Since the acidic water obtained by the electrolysis contains residual chlorine, after electrolysis, the valves 24, 25, and 26 are switched, and the water is passed again through the chlorine compound removing means 27, so that the ascorbic acid is removed. By removing the residual chlorine in the water, the astringent effect by the acidic water and the residual chlorine removing effect by the ascorbic acid make it possible to take a comfortable and beauty bath.

【0040】また、塩素化合物除去手段で還元剤として
アスコルビン酸を浴槽水に添加することで、次亜塩素酸
を還元(または分解)できると同時に、アスコルビン酸
は太陽光線(紫外線)によってダメージをうけ、皮膚表
面に形成された酸化脂質を還元できるので、美容にもよ
いという特有の効果を持っている。そして、アスコルビ
ン酸は天然植物(果物、野菜など)に含まれる物質であ
り、安全性がきわめて高い。同様にして、ビタミン類で
還元作用を有する物質(例えば、ビタミンA、B、D、
Eなど)や、植物抽出物(カテキンエキス、クロロフィ
ルのようなお茶の抽出物など)をアスコルビン酸の代用
に用いることでも同様の効果を得ることができる。ま
た、天然物質以外であれば、亜硫酸カルシウム、チオ硫
酸ナトリウムなどを用いてもよい。これらを用いる場合
は、図2のBのように、亜硫酸カルシウムまたはチオ硫
酸ナトリウムを粒状体45に成型し、これを流失防止体
46を有するケーシング47内に充填し、循環流路19
に配置し、矢印の様に水を流すことで水がケーシング内
の粒状体45と接触し、残留塩素が除去できる。
By adding ascorbic acid as a reducing agent to bath water by means of a chlorine compound removing means, hypochlorous acid can be reduced (or decomposed) and at the same time ascorbic acid is damaged by sunlight (ultraviolet rays). Since it can reduce oxidized lipids formed on the skin surface, it has a unique effect that it is good for beauty. Ascorbic acid is a substance contained in natural plants (fruits, vegetables, etc.) and is extremely safe. Similarly, substances having a reducing action with vitamins (for example, vitamins A, B, D,
E) or a plant extract (eg, a tea extract such as catechin extract or chlorophyll) can be used in place of ascorbic acid to obtain the same effect. In addition, other than natural substances, calcium sulfite, sodium thiosulfate and the like may be used. When these are used, as shown in FIG. 2B, calcium sulfite or sodium thiosulfate is formed into granules 45, which are filled in a casing 47 having a flow-off preventing body 46, and
And flowing water as shown by the arrow, the water comes into contact with the granular material 45 in the casing, and residual chlorine can be removed.

【0041】また、アスコルビン酸等のビタミン類や亜
硫酸カルシウム、チオ硫酸ナトリウム等の物質を粉末状
で使用したい場合は、図2のCのように、上流及び下流
側(少なくとも下流側は必須)に不織布48を装着した
薬品収納部49に粉末薬品50を入れ、これをケーシン
グ51内に収める。循環してきた水は、この塩素化合物
除去手段内で矢印に示したように通過する。すなわち、
循環水の一部が不織布を通過し、粉末薬品50の一部と
接触(物質によっては溶解)することで、水中の残留塩
素を除去可能となる。この方法は不織布48の材質、開
孔径、不織布48の面積、や、ケーシング51と薬品収
納部50との隙間(距離)を任意に変えることで薬品と
の接触、または溶解条件を容易に変えることができる。
なお、一方向だけに不織布を用いる場合は、上流または
下流に逆止弁設置することで、粉末薬品49の漏出を防
止できる。
When it is desired to use vitamins such as ascorbic acid and substances such as calcium sulfite and sodium thiosulfate in powder form, as shown in FIG. A powdered medicine 50 is put in a medicine container 49 to which a nonwoven fabric 48 is attached, and this is housed in a casing 51. The circulated water passes through the chlorine compound removing means as shown by the arrow. That is,
Part of the circulating water passes through the nonwoven fabric and contacts (dissolves depending on the substance) a part of the powder chemical 50, thereby enabling the residual chlorine in the water to be removed. In this method, the contact with the medicine or the dissolution condition can be easily changed by arbitrarily changing the material of the nonwoven fabric 48, the opening diameter, the area of the nonwoven fabric 48, and the gap (distance) between the casing 51 and the medicine storage section 50. Can be.
When the nonwoven fabric is used only in one direction, the check valve can be installed upstream or downstream to prevent leakage of the powdered chemical 49.

【0042】なお、本実施例において、電極32、33
の間に隔膜40を配置し、電気分解で電解水をつくると
同時に酸性水をつくることができる構成としたが、浴槽
18に酸性水を供給したい場合以外は、隔膜40は必要
なく、従って、酸性水を造るための流路29、30及び
弁24を省くことができる。
In this embodiment, the electrodes 32, 33
The diaphragm 40 is disposed between the electrodes, and the electrolytic water is produced by electrolysis, and at the same time, the acidic water can be produced. However, the diaphragm 40 is not necessary except when it is desired to supply the acidic water to the bath 18. The flow paths 29, 30 and the valve 24 for producing acidic water can be omitted.

【0043】(実施例2)図3A、Bは本発明の実施例
2の水浄化装置の塩素化合物除去手段を示す構成図であ
る。
(Embodiment 2) FIGS. 3A and 3B are configuration diagrams showing a chlorine compound removing means of a water purification apparatus according to Embodiment 2 of the present invention.

【0044】本実施例2において、実施例1と異なる点
は触媒で残留塩素を分解除去する構成としている点に有
り、触媒52を含有する粒状体53をケーシング54に
充填、流出防止体55でケーシング54内に保持する、
または、触媒52を担持したハニカム状担体56を内蔵
している点にある。
The second embodiment is different from the first embodiment in that a residual chlorine is decomposed and removed by a catalyst. A granular material 53 containing a catalyst 52 is filled in a casing 54, and an outflow preventing member 55 is used. Held in the casing 54,
Alternatively, a honeycomb carrier 56 carrying the catalyst 52 is incorporated.

【0045】なお、実施例1と同一符号のものは同一構
造を有し、説明は省略する。
The components having the same reference numerals as those of the first embodiment have the same structure, and the description is omitted.

【0046】次に動作、作用を説明すると、浴槽18内
の水の残留塩素を除去する場合、実施例1と同様にして
弁25、26を切換え、ポンプ21を動かし、水が塩素
化合物除去手段27に入り、再び浴槽18へ戻る水回路
を形成する。図3のAの構成では、塩素化合物除去手段
27に入った水は、粒状体53の触媒52と接触するこ
とで、溶存している残留塩素が分解除去される。また、
図3のBの様にハニカム状担体56表面(両側)に触媒
52を担持することで、効果を維持しながら塩素化合物
除去手段27の圧力損失を低下することができる。
Next, the operation and action will be described. When removing residual chlorine in water in the bathtub 18, the valves 25 and 26 are switched and the pump 21 is operated in the same manner as in the first embodiment, so that the water is removed by the chlorine compound removing means. A water circuit is formed to enter the bath 27 and return to the bath 18 again. In the configuration shown in FIG. 3A, the water that has entered the chlorine compound removing means 27 comes into contact with the catalyst 52 of the granular material 53, so that dissolved residual chlorine is decomposed and removed. Also,
By supporting the catalyst 52 on the surfaces (both sides) of the honeycomb carrier 56 as shown in FIG. 3B, the pressure loss of the chlorine compound removing means 27 can be reduced while maintaining the effect.

【0047】なお、触媒52としては金属系のものが望
ましく、Au、Ag、Pd、Pt、Fe、Mn、W、T
i、Mo系が望ましい。
The catalyst 52 is desirably a metal-based catalyst such as Au, Ag, Pd, Pt, Fe, Mn, W, T
i, Mo system is desirable.

【0048】(実施例3)図4A、Bは本発明の実施例
3の塩素化合物除去手段27を示す構成図である。本実
施例3において、実施例1または2と異なる点は、ケー
シング57内に吸着手段の粒状活性炭58と流出防止板
59または、吸着手段の繊維状活性炭60を備えている
ところである。
(Embodiment 3) FIGS. 4A and 4B are block diagrams showing a chlorine compound removing means 27 according to Embodiment 3 of the present invention. The third embodiment is different from the first or second embodiment in that a granular activated carbon 58 and an outflow prevention plate 59 as an adsorbing unit or a fibrous activated carbon 60 as an adsorbing unit are provided in a casing 57.

【0049】なお、実施例1と同一符号のものは同一構
造を有し、説明は省略する。
The components having the same reference numerals as in the first embodiment have the same structure, and the description is omitted.

【0050】次に動作、作用を説明すると、浴槽18の
水の残留塩素を除去する場合、実施例1と同様にして、
弁25、26を切換え、塩素化合物除去手段27を通過
する水回路を形成する。その後、ポンプ21を始動し、
塩素化合物除去手段27に水を通水する。図4のAにお
いては、塩素化合物除去手段27に入った水は、粒状活
性炭58と接触することで、溶解している残留塩素は吸
着除去されるので、ポンプ21の循環を続けることで浴
槽18内の残留塩素濃度を低下させることができる。ま
た、図4のBの様にケーシング57内に繊維状活性炭6
0を装着することで、圧損は上昇するものの、残留塩素
除去率は向上する。
Next, the operation and the operation will be described. When the residual chlorine in the water in the bathtub 18 is removed, as in the first embodiment,
By switching the valves 25 and 26, a water circuit passing through the chlorine compound removing means 27 is formed. After that, the pump 21 is started,
Water is passed through the chlorine compound removing means 27. In FIG. 4A, the water that has entered the chlorine compound removing means 27 comes into contact with the granular activated carbon 58, and the dissolved residual chlorine is adsorbed and removed. The residual chlorine concentration in the inside can be reduced. Further, as shown in FIG.
By mounting 0, the pressure loss increases, but the residual chlorine removal rate improves.

【0051】なお、吸着剤として粒状活性炭58または
繊維状活性炭60を用いることで、水中の残留塩素だけ
でなく入浴によって混入する臭気を発する有機物の除去
も可能となるので、入浴人数が増えた場合でも臭気の少
ない快適な入浴を実現できるという特有の効果を有す
る。
The use of granular activated carbon 58 or fibrous activated carbon 60 as an adsorbent makes it possible to remove not only residual chlorine in water but also organic substances that emit odors mixed in during bathing. However, it has a unique effect that a comfortable bath with little odor can be realized.

【0052】また、本実施例では、吸着手段として粒状
活性炭58または繊維状活性炭60を用いたが、粒状ま
たは膜状のイオン交換樹脂を用いても同等の効果を得る
ことができる。
In this embodiment, the granular activated carbon 58 or the fibrous activated carbon 60 is used as the adsorbing means. However, the same effect can be obtained by using a granular or membrane ion exchange resin.

【0053】(実施例4)図5は本発明の実施例4の塩
素化合物除去手段27の構成図である。本実施例4にお
いて、実施例1、2または3と異なる点は、循環流路1
9に超音波発生手段として超音波発信素子61を備えて
いるところである。
(Embodiment 4) FIG. 5 is a block diagram of a chlorine compound removing means 27 according to Embodiment 4 of the present invention. The fourth embodiment is different from the first, second or third embodiment in that
9 is provided with an ultrasonic transmitting element 61 as ultrasonic generating means.

【0054】なお、実施例1と同一符号のものは同一構
造を有し、説明は省略する。
The components having the same reference numerals as in the first embodiment have the same structure, and a description thereof will be omitted.

【0055】次に動作、作用を説明すると、浴槽18の
水の残留塩素を除去する場合、実施例1と同様にして、
弁25、26を切換え、塩素化合物除去手段27を通過
する水回路を形成する。その後、ポンプ21を始動し、
塩素化合物除去手段27に水を通水する。その後、制御
手段38で超音波発信素子61の動作を制御し、循環し
てきた水に超音波を照射する。超音波により水中の残留
塩素は分解されるので、ポンプ21で水の循環を続ける
ことで浴槽18内の水の残留塩素濃度を低下させること
ができる。
Next, the operation and the operation will be described. When the residual chlorine in the water in the bathtub 18 is removed, as in the first embodiment,
By switching the valves 25 and 26, a water circuit passing through the chlorine compound removing means 27 is formed. After that, the pump 21 is started,
Water is passed through the chlorine compound removing means 27. Thereafter, the operation of the ultrasonic wave transmitting element 61 is controlled by the control means 38, and the circulating water is irradiated with ultrasonic waves. Since the residual chlorine in the water is decomposed by the ultrasonic wave, the residual chlorine concentration of the water in the bathtub 18 can be reduced by continuing the circulation of the water by the pump 21.

【0056】なお、本実施例のように塩素化合物除去手
段27として超音波発信素子61を用いることで、超音
波発信素子61に通電しているとき以外は残留塩素を分
解しないので、電解手段23と直列につなぐことが可能
になるので、装置の簡素化、流路切換えのための弁を減
らすことができるという効果も有している。
Since the ultrasonic transmitting element 61 is used as the chlorine compound removing means 27 as in this embodiment, the residual chlorine is not decomposed except when the ultrasonic transmitting element 61 is energized. Since it is possible to connect in series with the apparatus, there are also effects that the apparatus can be simplified and the number of valves for switching the flow path can be reduced.

【0057】(実施例5)図6に本発明の実施例5の塩
素化合物除去手段27の構成図を示した。実施例1から
4と異なる点は、塩素化合物除去手段27としてケーシ
ング62内に紫外線照射手段の紫外線ランプを備えてい
るところにある。矢印は水の流れを示す。
(Embodiment 5) FIG. 6 shows a configuration diagram of the chlorine compound removing means 27 of Embodiment 5 of the present invention. The difference from the first to fourth embodiments is that an ultraviolet lamp as an ultraviolet irradiation means is provided in the casing 62 as the chlorine compound removing means 27. Arrows indicate the flow of water.

【0058】なお、実施例1と同一符号のものは同一構
造を有し、説明は省略する。
The components having the same reference numerals as in the first embodiment have the same structure, and a description thereof will be omitted.

【0059】次に動作、作用を説明すると、浴槽18の
水の残留塩素を除去する場合、実施例1と同様にして、
弁25、26を切換え、塩素化合物除去手段27を通過
する水回路を形成する。その後、ポンプ21を始動し、
塩素化合物除去手段27に水を通水する。その後、制御
手段38で紫外線ランプ63に通電し、ケーシング62
内の水に紫外線を照射させる。この動作により、水中の
残留塩素が光化学的に分解され、ポンプ21で水の循環
を続けることにより浴槽18内の残留塩素濃度を低下さ
せる粉tができる。
Next, the operation and the operation will be described. When the residual chlorine in the water in the bathtub 18 is removed, the same operation as in the first embodiment is performed.
By switching the valves 25 and 26, a water circuit passing through the chlorine compound removing means 27 is formed. After that, the pump 21 is started,
Water is passed through the chlorine compound removing means 27. Thereafter, the control unit 38 supplies electricity to the ultraviolet lamp 63, and the casing 62
The water inside is irradiated with ultraviolet rays. By this operation, the residual chlorine in the water is photochemically decomposed, and powder t that reduces the residual chlorine concentration in the bathtub 18 is produced by continuing the circulation of the water by the pump 21.

【0060】なお、本実施例では、塩素化合物除去手段
として紫外線照射手段の紫外線ランプ62を用い、紫外
線を水に照射しているので、水中の残留塩素の分解除去
ができると同時に紫外線で水中の細菌を殺菌できるの
で、殺菌性能を維持したまま水中の残留塩素除去ができ
るという特有の効果を有している。
In this embodiment, the ultraviolet lamp 62 of the ultraviolet irradiation means is used to irradiate the water with the ultraviolet lamp 62 as the chlorine compound removing means. Since the bacterium can be sterilized, it has a specific effect that residual chlorine in water can be removed while maintaining the bactericidal performance.

【0061】[0061]

【発明の効果】以上説明したように本発明の請求項1に
係る水浄化装置は、電気分解により電解水を生成可能な
電解手段と、水中の塩素化合物を除去可能な塩素化合物
除去手段とを有し、制御手段の制御により殺菌中一定時
間だけ水中の塩素化合物の濃度を低下させることで、入
浴時以外の浴槽水には殺菌効果を有する電解水を常に一
定レベル以上の濃度で維持できるので、水中の細菌など
の微生物に常に酸性物質でダメージを与えることができ
るので、少量の電解水で最大の殺菌(または増殖抑制)
効果を得ることができるという効果がある。
As described above, the water purifying apparatus according to the first aspect of the present invention comprises an electrolytic means capable of generating electrolyzed water by electrolysis and a chlorine compound removing means capable of removing chlorine compounds in water. Since the concentration of the chlorine compound in the water is reduced for a certain period of time by the control of the control means during the sterilization, electrolyzed water having a sterilizing effect can always be maintained at a concentration equal to or higher than a certain level in bath water other than bathing. Because it can always damage microorganisms such as bacteria in water with acidic substances, maximum sterilization (or growth suppression) with a small amount of electrolyzed water
There is an effect that an effect can be obtained.

【0062】また、請求項3に係る水浄化装置は、前記
電解手段と塩素化合物除去手段を並列に設置したことを
特徴としているので、電解水を浴槽内に注入する際、電
解水を塩素化合物除去手段に通過させず電解水を有効に
使用できる。
Further, the water purifying apparatus according to claim 3 is characterized in that the electrolytic means and the chlorine compound removing means are installed in parallel, so that when the electrolytic water is injected into the bathtub, the electrolytic water is converted into the chlorine compound. Electrolyzed water can be used effectively without passing through the removing means.

【0063】また、請求項4にかかる水浄化装置は、浴
槽内への注水中または注水後のいずれかの時点で塩素化
合物除去手段により水中の塩素化合物を除去する制御を
行うので、注水直後(注湯も含む)に存在する水道水中
の塩素化合物の除去も可能となり、注水直後から快適な
入浴ができる。
Further, the water purifying apparatus according to the fourth aspect controls the removal of the chlorine compound in the water by the chlorine compound removing means at any point after the water injection into the bathtub or after the water injection. It is also possible to remove chlorine compounds in tap water existing in tap water (including pouring water), so that comfortable bathing can be performed immediately after pouring.

【0064】また、請求項5にかかる水浄化装置は、還
元剤を貯溜し、電解水または被処理水に接触可能な構成
としているので、安価かつ効果的な塩素化合物の除去が
可能となる。
Further, since the water purifying apparatus according to the fifth aspect stores the reducing agent and is configured to be able to come into contact with the electrolyzed water or the water to be treated, the chlorine compound can be inexpensively and effectively removed.

【0065】また、請求項6にかかる水浄化装置は、電
解水中の塩素化合物を分解可能な触媒をしようしている
ので、長期間塩素化合物の除去性能を維持できるので、
安定した塩素化合物除去性能を得ることができる。
Further, the water purifying apparatus according to claim 6 uses a catalyst capable of decomposing the chlorine compound in the electrolytic water, so that the performance of removing the chlorine compound can be maintained for a long time.
Stable chlorine compound removal performance can be obtained.

【0066】また、請求項7にかかる水浄化装置は、塩
素化合物除去手段は、電解水中の塩素化合物を吸着可能
な吸着材であることを特徴としているので、塩素化合物
だけでなく、塩素化合物と同時の水中の有機物も除去可
能なのでこれら由来の臭気を減少させることができる。
In the water purifying apparatus according to the present invention, the chlorine compound removing means is an adsorbent capable of adsorbing the chlorine compound in the electrolytic water. At the same time, organic substances in water can be removed, so that the odor derived from these substances can be reduced.

【0067】また、請求項8にかかる水浄化装置は、塩
素化合物除去手段は、超音波を発生可能な超音波発生手
段であり、超音波により塩素化合物を分解することを特
徴としているので、塩素化合物除去手段の構成の簡素化
が図れるだけでなく、水のクラスターを小さくすること
ができるので、肌に優しい水での入浴を可能となる。
Further, in the water purifying apparatus according to the present invention, the chlorine compound removing means is an ultrasonic wave generating means capable of generating ultrasonic waves, and is characterized by decomposing chlorine compounds by ultrasonic waves. Not only can the structure of the compound removing means be simplified, but also the cluster of water can be reduced, so that bathing with water that is gentle on the skin becomes possible.

【0068】また、請求項9にかかる水浄化装置は、紫
外線によって塩素化合物を分解しているので、紫外線で
塩素化合物を分解できると同時に水中の細菌を紫外線で
殺菌できるので効果的な殺菌ができる。
Further, in the water purifying apparatus according to the ninth aspect, since the chlorine compound is decomposed by the ultraviolet ray, the chlorine compound can be decomposed by the ultraviolet ray and the bacteria in the water can be sterilized by the ultraviolet ray, so that the effective sterilization can be performed. .

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

【図1】本発明の実施例1における水浄化装置の構成図FIG. 1 is a configuration diagram of a water purification device according to a first embodiment of the present invention.

【図2】A、B、Cは同水浄化装置の塩素化合物除去手
段の構成図
FIGS. 2A, 2B, and 2C are configuration diagrams of a chlorine compound removing unit of the water purification apparatus.

【図3】A、Bは本発明の実施例2における塩素化合物
除去手段の構成図
FIGS. 3A and 3B are configuration diagrams of a chlorine compound removing unit in Embodiment 2 of the present invention.

【図4】A、Bは本発明の実施例3における塩素化合物
除去手段の構成図
FIGS. 4A and 4B are configuration diagrams of a chlorine compound removing unit in Embodiment 3 of the present invention.

【図5】本発明の実施例4における塩素化合物除去手段
の構成図
FIG. 5 is a configuration diagram of a chlorine compound removing unit according to a fourth embodiment of the present invention.

【図6】本発明の実施例5における塩素化合物除去手段
の構成図
FIG. 6 is a configuration diagram of a chlorine compound removing unit according to a fifth embodiment of the present invention.

【図7】従来の水浄化装置の構成図FIG. 7 is a configuration diagram of a conventional water purification device.

【符号の説明】[Explanation of symbols]

18 浴槽 19 循環流路 21 ポンプ 23 電解手段 24、25、26 弁 27 塩素化合物除去手段 30 流路 32、33 電極 38 制御手段 44 アスコルビン酸水溶液 45 粒状体 50 薬品粉末 52 触媒 58 粒状活性炭 60 繊維状活性炭 61 超音波発信素子 63 紫外線ランプ Reference Signs List 18 bathtub 19 circulation channel 21 pump 23 electrolytic means 24, 25, 26 valve 27 chlorine compound removing means 30 flow path 32, 33 electrode 38 control means 44 ascorbic acid aqueous solution 45 granular material 50 chemical powder 52 catalyst 58 granular activated carbon 60 fibrous Activated carbon 61 Ultrasonic transmitter 63 Ultraviolet lamp

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/50 520 C02F 1/50 520L 531 531M 1/70 1/70 Z (72)発明者 松本 朋秀 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 4D024 AA06 AB11 BA02 BB01 BB02 BC01 DA03 DB03 DB09 DB10 DB22 4D037 AA09 AB14 BA18 BA26 BB01 CA02 CA04 CA09 4D050 AA10 AB45 AB46 BA06 BA07 BA12 BD02 BD03 BD06 BD08 CA06 CA07 CA10 CA15 4D061 DA03 DA07 DB01 DB10 EA03 EB39 ED13 FA06 FA07 FA13 FA17 FA20 GC01 GC02 GC12 GC18 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/50 520 C02F 1/50 520L 531 531M 1/70 1/70 Z (72) Inventor Tomohide Matsumoto Osaka 1006 Omon Kadoma, Fumonma-shi Matsushita Electric Industrial Co., Ltd.F-term (reference) CA06 CA07 CA10 CA15 4D061 DA03 DA07 DB01 DB10 EA03 EB39 ED13 FA06 FA07 FA13 FA17 FA20 GC01 GC02 GC12 GC18

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】循環流路に浴槽水の循環手段と、内部に少
なくとも一対の電極を有し、電気分解により塩素化合物
を含む電解水を生成可能な電解手段と、水の塩素化合物
を除去可能な塩素化合物除去手段とを備え、前記電解水
を水に添加することで連続的に浴槽内の水の殺菌・浄化
を行う構成において、制御手段により循環手段、電解手
段、塩素化合物除去手段のうち少なくとも一つの動作を
制御することで殺菌中一定時間だけ水中の塩素化合物の
濃度を低下させる動作制御を行う水浄化装置。
1. A bath water circulation means in a circulation flow path, an electrolysis means having at least a pair of electrodes therein and capable of producing electrolyzed water containing a chlorine compound by electrolysis, and a water chlorine compound being removable. And a sterilizing / purifying water in the bathtub by continuously adding the electrolyzed water to the water, wherein the controlling means includes a circulating means, an electrolytic means, and a chlorine compound removing means. A water purification device for controlling at least one operation to reduce the concentration of chlorine compounds in water for a certain period of time during sterilization.
【請求項2】塩素供給手段への水の流入出を制御可能な
流路切換手段を有する請求項1記載の水浄化装置。
2. The water purifying apparatus according to claim 1, further comprising a flow path switching means capable of controlling inflow and outflow of water to and from the chlorine supply means.
【請求項3】電解手段と塩素化合物除去手段を並列にし
た請求項2記載の水浄化装置。
3. The water purifying apparatus according to claim 2, wherein said electrolytic means and said chlorine compound removing means are arranged in parallel.
【請求項4】制御手段により、浴槽内への注水中または
注水後のいずれかの時点で塩素化合物除去手段により水
中の塩素化合物を除去する制御を行う請求項1ないし3
のいずれか1項記載の水浄化装置。
4. The control means for controlling the removal of chlorine compounds in water by the chlorine compound removing means at any time after or after injection into the bathtub.
The water purification device according to any one of claims 1 to 4.
【請求項5】塩素化合物除去手段は、内部に還元剤を貯
溜し、電解水または被処理水に接触可能な構成とした請
求項2ないし4のいずれか1項記載の水浄化装置。
5. The water purifying apparatus according to claim 2, wherein the chlorine compound removing means stores a reducing agent therein and is configured to be able to contact the electrolyzed water or the water to be treated.
【請求項6】塩素化合物除去手段が、電解水中の塩素化
合物を分解可能な触媒であることを特徴とした請求項2
ないし4のいずれか1項記載の水浄化装置。
6. The chlorine compound removing means is a catalyst capable of decomposing a chlorine compound in electrolytic water.
The water purification device according to any one of claims 4 to 4.
【請求項7】塩素化合物除去手段が、電解水中の塩素化
合物を吸着可能な吸着材であることを特徴とする請求項
2ないし4のいずれか1項記載の水浄化装置。
7. The water purification apparatus according to claim 2, wherein the chlorine compound removing means is an adsorbent capable of adsorbing a chlorine compound in the electrolytic water.
【請求項8】塩素化合物除去手段が、超音波を発生可能
な超音波発生手段であり、超音波により塩素化合物を分
解することを特徴とした請求項1または4記載の水浄化
装置。
8. The water purification apparatus according to claim 1, wherein the chlorine compound removing means is an ultrasonic wave generating means capable of generating ultrasonic waves, and decomposes the chlorine compound by ultrasonic waves.
【請求項9】塩素化合物除去手段が、紫外線を照射する
紫外線照射手段であり、紫外線によって塩素化合物を分
解することを特徴とした請求項1または4項記載の水浄
化装置。
9. The water purification apparatus according to claim 1, wherein the chlorine compound removing means is an ultraviolet ray irradiating means for irradiating ultraviolet rays, and decomposes the chlorine compound by the ultraviolet rays.
JP35428899A 1999-12-14 1999-12-14 Water cleaning device Pending JP2001170636A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35428899A JP2001170636A (en) 1999-12-14 1999-12-14 Water cleaning device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35428899A JP2001170636A (en) 1999-12-14 1999-12-14 Water cleaning device

Publications (1)

Publication Number Publication Date
JP2001170636A true JP2001170636A (en) 2001-06-26

Family

ID=18436541

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2001170636A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008012497A (en) * 2006-07-10 2008-01-24 Japan Organo Co Ltd Water treatment apparatus and water treatment method
JP2008100191A (en) * 2006-10-20 2008-05-01 Sanyo Electric Co Ltd Scale removal system
JP2012210556A (en) * 2011-03-30 2012-11-01 Panasonic Corp Water purifier
JP2015112554A (en) * 2013-12-12 2015-06-22 株式会社ウェルシィ Water treatment method and system
CN106854025A (en) * 2016-12-14 2017-06-16 安徽华塑股份有限公司 A kind of processing method of chlor-alkali industrial waste water

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008012497A (en) * 2006-07-10 2008-01-24 Japan Organo Co Ltd Water treatment apparatus and water treatment method
JP2008100191A (en) * 2006-10-20 2008-05-01 Sanyo Electric Co Ltd Scale removal system
JP2012210556A (en) * 2011-03-30 2012-11-01 Panasonic Corp Water purifier
JP2015112554A (en) * 2013-12-12 2015-06-22 株式会社ウェルシィ Water treatment method and system
CN106854025A (en) * 2016-12-14 2017-06-16 安徽华塑股份有限公司 A kind of processing method of chlor-alkali industrial waste water

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