JPH09327407A - Circulation warming bath - Google Patents
Circulation warming bathInfo
- Publication number
- JPH09327407A JPH09327407A JP8152052A JP15205296A JPH09327407A JP H09327407 A JPH09327407 A JP H09327407A JP 8152052 A JP8152052 A JP 8152052A JP 15205296 A JP15205296 A JP 15205296A JP H09327407 A JPH09327407 A JP H09327407A
- Authority
- JP
- Japan
- Prior art keywords
- bath
- water
- tank
- circulating
- electrolysis
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/4618—Devices therefor; Their operating or servicing for producing "ionised" acidic or basic water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/4612—Controlling or monitoring
- C02F2201/4615—Time
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Landscapes
- Details Of Fluid Heaters (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、浴槽内の浴槽水を
循環して再利用するための濾過装置を備えた循環温浴器
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a circulating hot water bath equipped with a filtering device for circulating and reusing bath water in a bath.
【0002】[0002]
【従来の技術】従来より、浴槽水を循環ポンプを利用し
て,濾過タンク、活性化タンク等を経て循環させ、湯の
汚れの除去と活性化を行うことが家庭用の風呂において
も行われており、近年さらに機能を向上させたものとし
て、単に湯の汚れを除去し活性化するだけでなく、保温
用ヒータを利用して温度制御を行い、24時間何時でも
入浴できるようにしたいわゆる24時間風呂の開発も行
われている。2. Description of the Related Art Conventionally, bath water is circulated through a filtration tank, an activation tank, etc. using a circulation pump to remove dirt and activate hot water even in a domestic bath. In recent years, as a further improved function, the so-called "24" that not only simply removes and activates the dirt in the hot water but also controls the temperature using a heater for warming so that the user can take a bath 24 hours a day An hour bath is being developed.
【0003】さらに、浴槽水の汚れの除去のほかに悪臭
や大腸菌の発生を防ぐことを目的とし、殺菌処理を行う
ための紫外線殺菌装置を備えたものや、また小型のオゾ
ン発生装置を設けてオゾン処理を行う機種も開発されて
いる。Further, in addition to removing dirt from the bath water, the one equipped with an ultraviolet sterilizer for sterilization is also provided for the purpose of preventing the generation of foul odor and Escherichia coli, and a small ozone generator is provided. Models that perform ozone treatment have also been developed.
【0004】また、浴槽水の殺菌とは別方向からの開発
で、浴槽にマッサージ効果をもたせることを目的とし、
浴槽水に空気を吸い込ませつつ浴槽内にジエット噴出さ
せて気泡を発生させる技術も開発され、このような機能
も循環温浴器に付加されるようになった。[0004] In addition, it is developed from a direction different from the sterilization of bath water so that the bathtub has a massage effect.
A technology has been developed in which air is drawn into the bathtub and air is jetted out into the bathtub to generate bubbles, and such a function has also been added to the circulating warm bath.
【0005】図4はこのような各機能をもつ従来の循環
温浴器を示す概略図で、同図において、循環ポンプ4が
駆動すると、浴槽1内の浴槽水が吸い込み口2より吸い
上げ、循環路を通じて循環ポンプ4に入る。循環ポンプ
4より送出された浴槽水は、まず濾過タンク5により濾
過される。濾過された浴槽水は活性化タンク19に送ら
れ、中に詰められた麦飯石などにより活性化される。こ
こで汚れを取り除かれた浴槽水は、紫外線又はオゾン等
を利用した殺菌器20により殺菌される。こうして浄化
された浴槽水は保温用ヒータ7により温度コントロール
されて吐き出し口3より浴槽1内に戻される。この際空
気を混ぜてジェット噴流を出すこともある。FIG. 4 is a schematic view showing a conventional circulating hot water bath having such functions. In FIG. 4, when the circulating pump 4 is driven, the bath water in the bath 1 is sucked up from the suction port 2 and the circulation path is formed. Through the circulation pump 4. The bath water sent from the circulation pump 4 is first filtered by the filtration tank 5. The filtered bath water is sent to the activation tank 19 and activated by the barley stone etc. packed therein. The bath water from which the dirt has been removed is sterilized by the sterilizer 20 using ultraviolet rays, ozone, or the like. The bath water purified in this way is returned to the bath 1 through the outlet 3 with its temperature controlled by the heater 7 for heat retention. At this time, air may be mixed to produce a jet jet.
【0006】[0006]
【発明が解決しようとする課題】上記従来の循環温浴器
においては、濾過タンク5により浴槽水中に混入された
汚れや油分等を除去して浴槽水を浄化し、さらに活性化
タンク19中の麦飯石等により水質をミネラル化するな
どの効果がある。しかしながら、24時間連続で使用し
ているため、濾床や麦飯石等の濾材の目づまりや、微生
物の発生による濾床や濾材の固着が問題となる。In the conventional circulating hot water bath, the filtration tank 5 removes dirt, oil and the like mixed in the bath water to purify the bath water, and further the cooked rice in the activation tank 19. It has the effect of mineralizing water quality with stones. However, since it is used continuously for 24 hours, clogging of filter media such as filter beds and barley stones and sticking of filter media and filter media due to generation of microorganisms become a problem.
【0007】この対策としては、濾床をカートリッジ式
にして定期的に交換したり、ユーザ自身により濾床を洗
浄する必要がある。また、濾過タンクの下部から水流を
通し、濾過タンク上部から排水を行う自動逆洗法もある
が、濾床の固着が激しいときは徐々に洗浄の効果が下が
り、フィルターの通水寿命が短い。As a countermeasure against this, it is necessary to make the filter bed into a cartridge type and periodically replace it, or to wash the filter bed by the user himself. There is also an automatic backwashing method in which a water flow is passed from the lower part of the filtration tank and drainage is performed from the upper part of the filtration tank. However, when the filter bed is strongly stuck, the effect of washing is gradually reduced, and the water passing life of the filter is short.
【0008】循環温浴器のメリットとして、24時間い
つでも風呂に入れることのほかに、浴槽の掃除が不要に
なることがあげるられるが、循環温浴器自体も、メンテ
ナンスの間隔をできるだけ長くするために、フィルター
の寿命を長くすることが望まれている。One of the merits of the circulating hot water bath is that it is not necessary to clean the bath in addition to taking a bath 24 hours a day. However, the circulating hot water bath itself needs to have a maintenance interval as long as possible. It is desired to extend the life of the filter.
【0009】本発明は、このような循環温浴器におい
て、メンテナンスをより容易に行えるようにすることを
目的とする。It is an object of the present invention to make maintenance easier in such a circulating hot water bath.
【0010】[0010]
【課題を解決するための手段】本発明は、浴槽内の浴槽
水を循環して再利用するための濾過装置を備えた循環温
浴器において、電気分解された前記浴槽水を前記浴槽内
及び濾過装置のいずれかまたは双方に循環させるように
したことを特徴とする。DISCLOSURE OF THE INVENTION The present invention relates to a circulating hot water bath equipped with a filtering device for circulating and reusing the bath water in the bathtub, wherein the electrolyzed bath water is filtered in the bath and in the bath. It is characterized in that it is circulated to either or both of the devices.
【0011】この発明によれば、浴槽水中に溶け込んだ
有機物の濾過効率をpH値変化による有機物の凝集効果
を利用して向上させることができ、また電気分解で生成
される強アルカリ性電解浴槽水又は強酸性浴槽水により
濾過装置内が殺菌され、メンテナンスがより容易に行え
る。According to the present invention, the filtration efficiency of the organic matter dissolved in the bath water can be improved by utilizing the agglomeration effect of the organic matter due to the change in pH value, and the strongly alkaline electrolysis bath water produced by electrolysis or The inside of the filtration device is sterilized by the strongly acidic bath water, and maintenance can be performed more easily.
【0012】[0012]
【発明の実施の形態】本発明の請求項1、2記載の発明
は、浴槽内の浴槽水を循環して再利用するための濾過装
置を備えた循環温浴器において、電気分解された前記浴
槽水を前記浴槽内及び濾過装置のいずれかまたは双方に
循環させるようにしたもので、これによって、浴槽水中
に溶け込んだ有機物の濾過効率をpH値変化による有機
物の凝集効果を利用して向上させることができ、また電
気分解で生成される強アルカリ性電解浴槽水又は強酸性
浴槽水により濾過装置内が殺菌される。BEST MODE FOR CARRYING OUT THE INVENTION The invention according to Claims 1 and 2 of the present invention is a circulating hot water bath equipped with a filtering device for circulating and reusing the bath water in the bathtub, wherein the bath is electrolyzed. Water is circulated in either or both of the bath and the filtration device, thereby improving the filtration efficiency of the organic matter dissolved in the bath water by utilizing the aggregation effect of the organic matter due to the pH value change. In addition, the inside of the filtration device is sterilized by the strongly alkaline electrolytic bath water or the strongly acidic bath water produced by electrolysis.
【0013】請求項4に記載の発明は、前記電解装置内
をそれぞれに電極を有し隔膜により区画された吐水槽及
び滞留槽により構成し、前記吐水槽を前記浴槽内に循環
させる流路に接続し、前記滞留槽を前記濾過装置に接続
したものである。According to a fourth aspect of the present invention, the inside of the electrolysis device is constituted by a water discharge tank and a retention tank each having an electrode and partitioned by a diaphragm, and the water discharge tank is provided in a flow path for circulating the water in the bath. And the retention tank is connected to the filtration device.
【0014】これによって、隔膜で隔てられた滞留槽に
は、吐水槽側で酸性電解を行う場合は強アルカリ性電解
浴槽水が生成され、吐水槽側でアルカリ電解を行う場合
は強酸性浴槽水が生成される。この滞留水を定期的に濾
過装置内に通水させることにより、濾過装置内の細菌を
定期的に殺菌することができる。この結果、濾過装置内
に設置された濾過フィルターもしくは濾材での有害微生
物の発生を防ぎ、濾材中での細菌の繁殖による濾材の目
詰まりを防ぎ、濾過寿命を延ばすことができる。また逆
洗により濾材の洗浄を行う場合にも濾材の微生物の繁殖
による濾材の固着がないため、少ない浴槽水により効率
的に行うことができる。As a result, in the retention tank separated by the diaphragm, strong alkaline electrolytic bath water is generated when acidic electrolysis is performed on the discharge tank side, and strong acidic bath water is generated when alkaline electrolysis is performed on the discharge tank side. Is generated. Bacteria in the filtration device can be regularly sterilized by periodically passing the accumulated water through the filtration device. As a result, it is possible to prevent the generation of harmful microorganisms in the filter or the filter medium installed in the filter device, to prevent clogging of the filter medium due to the growth of bacteria in the filter medium, and to extend the filtration life. Further, even when the filter medium is washed by backwashing, the filter medium is not fixed due to the propagation of microorganisms in the filter medium, so that it can be efficiently performed with a small amount of bath water.
【0015】請求項5に記載の発明は、前記電解装置内
の電極の極性を変換可能としたもので、これによって、
滞留槽および吐水槽にそれぞれアルカリ性電解浴槽水又
は強酸性浴槽水を任意に得ることができる。According to a fifth aspect of the present invention, the polarities of the electrodes in the electrolysis device can be changed.
Alkaline electrolytic bath water or strongly acidic bath water can be arbitrarily obtained in the retention tank and the water discharge tank, respectively.
【0016】請求項6に記載の発明は、前記電解装置内
に発生する気体を排出する気体排出機構を備えたもの
で、これによって、通水される水量が気体発生による通
水量変化に左右されることの無い、安定した水量及びp
H値で浴槽への通水を行うことができる。The invention according to claim 6 is provided with a gas discharge mechanism for discharging the gas generated in the electrolysis apparatus, whereby the amount of water to be passed is influenced by the change in the amount of water passed due to the generation of gas. Stable water volume and p
Water can be passed through the bath at the H value.
【0017】請求項7に記載の発明は、装置運転開始時
又は電極の極性切り替え時に前記電解装置内の隔膜に付
着した気泡を排出するように作動させるようにしたもの
で、これによって、さらにメンテナンスが容易になる。According to a seventh aspect of the present invention, when the operation of the apparatus is started or when the polarities of the electrodes are switched, the air bubbles adhering to the diaphragm in the electrolysis apparatus are discharged so that further maintenance is performed. Will be easier.
【0018】以下、本発明の実施の形態について図1な
いし図3を参照しながら説明する。図1は本発明の実施
の形態における風呂用循環温浴器の概略構成図、図2は
図1に示す電解槽の概略構成図、図3は電解生成時の制
御を示すブロック図である。Embodiments of the present invention will be described below with reference to FIGS. 1 to 3. FIG. 1 is a schematic configuration diagram of a circulating hot bath for bath according to an embodiment of the present invention, FIG. 2 is a schematic configuration diagram of the electrolytic cell shown in FIG. 1, and FIG. 3 is a block diagram showing control during electrolysis generation.
【0019】図1に示すように浴槽1には浴槽水が満た
されている。装置内部には、循環ポンプ4、濾過タンク
5(メンブレンフィルター:開口径5ミクロン、10イ
ンチモジュール)、保温用ヒータ7(消費電力:800
W)及び電解装置6がそれぞれ備えられている。浴槽1
内の浴槽水は、浴槽1中に設置された吸い込み口2から
循環ポンプ4により矢印Aで示す主循環路に導かれ、濾
過タンク5、電解装置6への分岐口を経て、保温用ヒー
タ7を通り吐き出し口3から浴槽1内へ戻り、これによ
って、浴槽水の循環浄化を繰り返す。また、主循環路中
の分岐口から分岐された浴槽水は、矢印Bで示す副循環
路を通り電解装置6へと導かれる。As shown in FIG. 1, the bathtub 1 is filled with bathtub water. Inside the device, a circulation pump 4, a filtration tank 5 (membrane filter: opening diameter 5 micron, 10 inch module), a heater for heat insulation 7 (power consumption: 800
W) and an electrolysis device 6 are provided respectively. Bathtub 1
The bath water in the bath is introduced from a suction port 2 installed in the bath 1 to a main circulation path indicated by an arrow A by a circulation pump 4, and passes through a branching port to a filtration tank 5 and an electrolyzer 6, and then a heat retaining heater 7 Through the discharge port 3 to return to the inside of the bathtub 1, whereby the circulation purification of the bath water is repeated. In addition, the bath water branched from the branch port in the main circulation path is guided to the electrolysis device 6 through the sub circulation path indicated by the arrow B.
【0020】図2に示すように、この電解装置6には一
定時間後に陽極、陰極の切り替えが可能な2枚の白金メ
ッキチタン電極12、13(電極面積:25−、メッキ
厚:0.5〜2ミクロン)が設置してあり、その間に隔
膜16(RF−250)が設置され、吐水槽14(容積
2リットル)と滞留槽15(容積2.5リットル)に2
分割されている。ここで、滞留槽15の体積は濾過タン
ク5の容積を基準として設定されるが、電流値に比例す
るイオン泳動による水位増加が起こるため、滞留槽15
の体積を吐水槽14よりも大きくとる必要がある。副循
環路はこの吐水槽14側へ通水され、電解装置6内で電
解を受け、pH値を変化させられて吐き出し口3を経て
浴槽1へと循環される。As shown in FIG. 2, in the electrolysis device 6, two platinum-plated titanium electrodes 12 and 13 (electrode area: 25-, plating thickness: 0.5) capable of switching between an anode and a cathode after a predetermined time. ~ 2 microns) is installed, the diaphragm 16 (RF-250) is installed between them, and the discharge tank 14 (volume 2 liters) and the retention tank 15 (volume 2.5 liters) 2
Has been split. Here, the volume of the retention tank 15 is set with reference to the volume of the filtration tank 5, but since the water level increases due to iontophoresis in proportion to the current value, the retention tank 15
It is necessary to make the volume of the above larger than that of the water discharge tank 14. Water is passed through the sub-circulation path to the water discharge tank 14 side, electrolyzed in the electrolysis device 6, the pH value is changed, and the water is circulated to the bath 1 through the discharge port 3.
【0021】電解装置6内において、吐水槽14で酸性
電解を行う場合、浴槽水中の陰イオンはイオン泳動によ
り隔膜16を通過して滞留槽15の陽極電極13へ移動
し、また陽イオンは吐水槽14の陰極電極12へと移動
していく。同時に電極12、13表面では、陰極電極1
2上では水素ガスが、陽極電極13上では酸素ガスと一
部塩素ガスが発生する。その結果、吐水槽14では酸性
浴槽水として循環を繰り返し、滞留槽15中は強いアル
カリ性浴槽水となる。When performing acidic electrolysis in the water discharge tank 14 in the electrolysis device 6, anions in the bath water pass through the diaphragm 16 by iontophoresis to move to the anode electrode 13 of the retention tank 15, and cations are discharged. It moves to the cathode electrode 12 of the water tank 14. At the same time, on the surfaces of the electrodes 12 and 13, the cathode electrode 1
Hydrogen gas is generated on 2 and oxygen gas and a part of chlorine gas are generated on the anode electrode 13. As a result, the water in the water discharge tank 14 is repeatedly circulated as acidic bath water, and the water in the retention tank 15 becomes strong alkaline bath water.
【0022】また、吐水槽14でアルカリ電解を行う場
合は、浴槽水中の陽イオンが滞留槽15へ、陰イオンが
吐水槽14へとイオン泳動により移動し、滞留槽15に
強い酸性浴槽水を、吐水槽14はアルカリ性浴槽水を生
成し循環することとなる。When performing alkaline electrolysis in the water discharge tank 14, cations in the bath water move to the retention tank 15 and anions move to the water discharge tank 14 by ion migration, so that the strong acid bath water is stored in the retention tank 15. The water discharge tank 14 generates and circulates alkaline bath water.
【0023】このとき発生したそれぞれのガスは、それ
ぞれの槽14、15内にて上昇し分離され、槽上部より
排出される。気体排出口には気体分解のための気体分解
装置17(ハニカム活性炭5×5×10cm)が取り付け
てある。ここで、吐水槽14内で発生した気体の一部は
浴槽水と同時に吐水により循環する。この浴槽水に混合
される気体を分離するために吐水槽14出口に設置され
た排気用電磁弁11を開放することにより、気体は浴槽
水と分離され、電磁弁11、気体分解装置17を経て、
大気中へ排出される。The respective gases generated at this time rise in the respective tanks 14 and 15 to be separated and discharged from the upper portion of the tanks. A gas decomposing device 17 (honeycomb activated carbon 5 × 5 × 10 cm) for decomposing a gas is attached to the gas outlet. Here, a part of the gas generated in the water discharge tank 14 is circulated by the water discharge at the same time as the bath water. The gas is separated from the bath water by opening the exhaust electromagnetic valve 11 installed at the outlet of the water discharge tank 14 in order to separate the gas mixed with the bath water, and the gas is separated from the bath water through the electromagnetic valve 11 and the gas decomposing device 17. ,
Emitted into the atmosphere.
【0024】また、これとは別に、電磁弁11は、電極
の極性の切り替え時や機器停止後の運転開始時に閉動作
を行うと、吐水槽14内は閉区間となり、吐水槽14内
圧力は低下して水位が低下する。このことにより、電解
による気体発生に伴い隔膜16に付着した気体及び、電
気泳動により隔膜16に付着したゴミ等を排出すること
が可能となる。また、機器停止等により電解装置6内へ
空気が混入したときにも、同様の動作を行うことにより
空気の排出を行うことができる。Separately from this, when the solenoid valve 11 is closed at the time of switching the polarities of the electrodes or at the start of the operation after the device is stopped, the inside of the water discharge tank 14 becomes a closed section, and the pressure in the water discharge tank 14 becomes It lowers and the water level lowers. This makes it possible to discharge the gas attached to the diaphragm 16 as the gas is generated by electrolysis, and the dust and the like attached to the diaphragm 16 by electrophoresis. Further, even when air is mixed into the electrolysis device 6 due to the stop of the device or the like, the air can be discharged by performing the same operation.
【0025】また、滞留槽15は、滞留槽15下部に設
置された通水路により濾過タンク5へと電磁弁9を経て
接続されており、一定周期で滞留槽15内に生成された
強アルカリ性浴槽水もしくは、強酸性浴槽水を濾過タン
ク5へ通水し、タンク内を殺菌することができる構造と
なっている。Further, the retention tank 15 is connected to the filtration tank 5 via a solenoid valve 9 by a water passage installed in the lower portion of the retention tank 15, and a strong alkaline bath generated in the retention tank 15 at regular intervals. Water or strongly acidic bath water is passed through the filtration tank 5 to sterilize the inside of the tank.
【0026】次いで図1及び図2を参照して、上記構成
の循環温浴器における動作を説明する。循環ポンプ4を
駆動させることにより吸い込み口2から吸い込まれた浴
槽水は、循環ポンプ4を通って濾過タンク5に供給され
る。このとき浴槽水の一部は分岐口より分岐され、矢印
Bで示す副循環路へと循環される。主循環路での浴槽水
は濾過タンク5内に設置されたフィルターにより濾過浄
化され、その後に設置された保温用ヒータ7により加熱
保温され浴槽1へと循環される。Next, referring to FIGS. 1 and 2, the operation of the circulating hot water bath having the above construction will be described. The bath water sucked from the suction port 2 by driving the circulation pump 4 is supplied to the filtration tank 5 through the circulation pump 4. At this time, part of the bath water is branched from the branch port and circulated to the auxiliary circulation path indicated by arrow B. The bath water in the main circulation path is filtered and purified by a filter installed in the filtration tank 5, and then heated and kept warm by a heat-retaining heater 7 provided therein and circulated to the bath 1.
【0027】ここで予め設定された時間に図3に示すフ
ローチャートに従い一連の動作を行う。タイマーにより
電磁弁8が開放され、主循環路から分岐された副循環路
への浴槽水は電解装置6に導かれる。電解装置6の槽1
4、15内に浴槽水が満たされた後、気体排出動作のた
めに電磁弁11の閉動作を数度行う。Here, at a preset time, a series of operations are performed according to the flowchart shown in FIG. The solenoid valve 8 is opened by the timer, and the bath water from the main circulation path to the auxiliary circulation path is guided to the electrolysis device 6. Tank 1 of electrolysis device 6
After the bath water is filled in the chambers 4 and 15, the electromagnetic valve 11 is closed several times for the gas discharging operation.
【0028】その後、電極12、13に通電を行い電解
が開始される(電解条件:電圧30V、電流1〜3
A)。始めに吐水槽14中で酸性電解を行い、滞留槽1
5中でアルカリ電解を行う。この結果、浴槽1中には吐
水槽14より弱酸性浴槽水が循環し、滞留槽15中には
強アルカリ性浴槽水が蓄積される(循環時間3時間)。
その後、循環ポンプ4を停止し、濾過タンク5内の水抜
きのために排水用電磁弁10を開放し濾過タンク5内の
排水を行う。After that, the electrodes 12 and 13 are energized to start electrolysis (electrolysis conditions: voltage 30 V, current 1 to 3).
A). First, acidic electrolysis is performed in the water discharge tank 14, and the retention tank 1
Alkaline electrolysis is performed in 5. As a result, weakly acidic bath water circulates in the bath 1 from the water discharge tank 14, and strong alkaline bath water accumulates in the retention tank 15 (circulation time 3 hours).
Then, the circulation pump 4 is stopped, and the drainage solenoid valve 10 is opened to drain the water in the filtration tank 5 to drain the water in the filtration tank 5.
【0029】その後、滞留槽15下部に取り付けられた
電磁弁9を開放することにより滞留槽15中の強アルカ
リ性浴槽水を濾過タンク5内へ注ぎ込む。このとき、強
アルカリ性浴槽水により濾過タンク5内、及び濾過タン
ク5内のフィルターは殺菌され、同時に付着した有機物
は一部分解される。このことにより、本来フィルター上
で濾過された有機物に繁殖する微生物の発生を防ぐと同
時に、洗浄による有機物の分離を容易に達成することが
できる。After that, the solenoid valve 9 attached to the lower part of the retention tank 15 is opened so that the strongly alkaline bath water in the retention tank 15 is poured into the filtration tank 5. At this time, the strong alkaline bath water sterilizes the filter in the filtration tank 5 and the filter in the filtration tank 5, and at the same time, the attached organic substances are partially decomposed. As a result, it is possible to prevent the generation of microorganisms that propagate in the organic matter originally filtered on the filter, and at the same time, to easily achieve separation of the organic matter by washing.
【0030】また、この後に電磁弁10を開放し、流路
切り替え弁18を切り替えて、浴槽水により濾過タンク
5内を洗浄し排水(5リットル)する。このとき、濾過
によりフィルター上に残された有機物と共に分解された
有機物も一緒に排出する。After this, the solenoid valve 10 is opened, the flow path switching valve 18 is switched, and the inside of the filtration tank 5 is washed with bath water and drained (5 liters). At this time, the decomposed organic matter is discharged together with the organic matter left on the filter by filtration.
【0031】また、この後同様に、吐水槽14中をアル
カリ性電解、滞留槽15中を酸性電解とする電解を実施
するために、電解槽中への給水を行う。この後同様に、
吐水槽14と滞留槽15の間に設置された隔膜16に付
着した電解により発生した気体を除去するため、気体排
動作を行う。また、同様に吐水槽14で酸性電解を開始
し(循環時間2時間)、タンク内排水、滞留水給水(保
持時間1時間)、逆洗洗浄動作(排水5リットル)を行
う。Similarly, after this, in order to carry out the electrolysis in which the discharge tank 14 is alkaline electrolyzed and the retention tank 15 is acidic electrolyzed, water is supplied to the electrolytic tank. Similarly after this,
In order to remove the gas generated by electrolysis attached to the diaphragm 16 installed between the water discharge tank 14 and the retention tank 15, a gas discharging operation is performed. Similarly, acidic electrolysis is started in the water discharge tank 14 (circulation time 2 hours), tank drainage, accumulated water supply (holding time 1 hour), and backwash cleaning operation (drainage 5 liters) are performed.
【0032】この一連の動作を繰り返すことにより、フ
ィルターの目詰まりを防止する効果を得ると同時に、濾
過フィルターの濾過寿命を延ばすことができる。By repeating this series of operations, the effect of preventing clogging of the filter can be obtained, and at the same time, the filtration life of the filtration filter can be extended.
【0033】[0033]
【発明の効果】請求項1、2記載の発明によれば、浴槽
水中に溶け込んだ有機物の濾過効率をpH値変化による
有機物の凝集効果を利用して向上させることができ、ま
た電気分解で生成される強アルカリ性電解浴槽水又は強
酸性浴槽水により濾過装置内が殺菌され、これによって
メンテナンスをより容易に行うことができる。According to the first and second aspects of the present invention, the filtration efficiency of the organic matter dissolved in the bath water can be improved by utilizing the aggregation effect of the organic matter due to the change in pH value, and is produced by electrolysis. The inside of the filtering device is sterilized by the strongly alkaline electrolytic bath water or the strongly acidic bath water, which facilitates maintenance.
【0034】請求項4に記載の発明によれば、隔膜で隔
てられた滞留槽には、吐水槽側で酸性電解を行う場合は
強アルカリ性電解浴槽水が生成され、吐水槽側でアルカ
リ電解を行う場合は強酸性浴槽水が生成される。この滞
留水を定期的に濾過装置内に通水させることにより、濾
過装置内の細菌を定期的に殺菌することができる。この
結果、濾過装置内に設置された濾過フィルターもしくは
濾材での有害微生物の発生を防ぎ、濾材中での細菌の繁
殖による濾材の目詰まりを防ぎ、濾過寿命を延ばすこと
ができる。また逆洗により濾材の洗浄を行う場合に濾材
の微生物の繁殖による濾材の固着がないため、少ない浴
槽水により効率的に行うことができる。According to the fourth aspect of the present invention, in the retention tank separated by the diaphragm, when acidic electrolysis is performed on the water discharge tank side, strong alkaline electrolytic bath water is generated, and alkaline electrolysis is performed on the water discharge tank side. When performed, strongly acidic bath water is produced. Bacteria in the filtration device can be regularly sterilized by periodically passing the accumulated water through the filtration device. As a result, it is possible to prevent the generation of harmful microorganisms in the filter or the filter medium installed in the filter device, to prevent clogging of the filter medium due to the growth of bacteria in the filter medium, and to extend the filtration life. In addition, when the filter medium is washed by backwashing, the filter medium is not fixed due to the growth of microorganisms in the filter medium, so that it can be efficiently performed with a small amount of bath water.
【0035】請求項5に記載の発明によって、滞留槽お
よび吐水槽にそれぞれアルカリ性電解浴槽水又は強酸性
浴槽水を任意に得ることができる。According to the fifth aspect of the invention, alkaline electrolysis bath water or strongly acidic bath water can be arbitrarily obtained in the retention tank and the water discharge tank, respectively.
【0036】請求項6に記載の発明によって、通水され
る水量が気体発生による通水量変化に左右されることの
無い、安定した水量及びpH値で浴槽への通水を行うこ
とができる。According to the sixth aspect of the present invention, it is possible to carry out the water flow to the bathtub with a stable water amount and pH value without the water flow amount being influenced by the change in the water flow amount due to the generation of gas.
【0037】請求項7に記載の発明によって、さらにメ
ンテナンスが容易になる。The invention according to claim 7 further facilitates maintenance.
【図1】本発明の実施の形態における風呂用循環温浴器
の概略構成図FIG. 1 is a schematic configuration diagram of a bath circulating warm bath according to an embodiment of the present invention.
【図2】図1に示す電解槽の概略構成図FIG. 2 is a schematic configuration diagram of the electrolytic cell shown in FIG.
【図3】電解生成時の制御を示すブロック図FIG. 3 is a block diagram showing control during electrolysis generation.
【図4】従来の循環温浴器を示す概略図FIG. 4 is a schematic view showing a conventional circulating warm bath.
1 浴槽 2 吸い込み口 3 吐き出し口 4 循環ポンプ 5 濾過タンク 6 電解装置 7 保温用ヒータ 8 電磁弁(電解槽給水用) 9 電磁弁(滞留水給水用) 10 電磁弁(排水用) 11 電磁弁(排気用) 12 電極(吐水側) 13 電極(滞留側) 14 吐水槽 15 滞留槽 16 隔膜 17 気体分解装置 18 流路切り替え弁 19 活性化タンク 20 殺菌器 1 Bathtub 2 Suction port 3 Discharge port 4 Circulation pump 5 Filtration tank 6 Electrolysis device 7 Heat-retaining heater 8 Electromagnetic valve (for electrolytic tank water supply) 9 Electromagnetic valve (for accumulated water supply) 10 Electromagnetic valve (for drainage) 11 Electromagnetic valve ( Exhaust) 12 Electrode (water discharge side) 13 Electrode (retention side) 14 Water discharge tank 15 Retention tank 16 Diaphragm 17 Gas decomposition device 18 Flow path switching valve 19 Activation tank 20 Sterilizer
───────────────────────────────────────────────────── フロントページの続き (72)発明者 北川 孝典 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 末松 真二 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 井浦 征英 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Takanori Kitagawa 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Shinji Suematsu 1006 Kadoma, Kadoma City, Osaka Matsushita Electric Industrial Co., Ltd. (72) Inventor Seiei Iura 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.
Claims (7)
の濾過装置を備えた循環温浴器において、電気分解され
た前記浴槽水を前記浴槽内及び濾過装置のいずれかまた
は双方に循環させるようにしたことを特徴とする循環温
浴器。1. A circulating hot water bath equipped with a filtration device for circulating and reusing the bath water in the bathtub, wherein the electrolyzed bathwater is circulated in either or both of the bath device and the filtration device. A circulating warm bath characterized by being adapted to.
の濾過装置を備えた循環温浴器において、前記浴槽水の
循環流路に、前記浴槽水を電気分解する電解装置と、電
気分解された浴槽水を前記浴槽内に循環させる流路とを
備えたことを特徴とする循環温浴器。2. A circulating hot water bath equipped with a filtering device for circulating and reusing the bath water in the bathtub, wherein an electrolytic device for electrolyzing the bath water is provided in a circulation passage of the bath water, and an electric device. A circulating hot water bath, comprising: a flow path for circulating decomposed bath water in the bath.
たことを特徴とする請求項2記載の循環温浴器。3. The circulating hot water bath according to claim 2, further comprising a heater for heating the circulating water.
膜により区画された吐水槽及び滞留槽により構成し、前
記吐水槽を前記浴槽内に循環させる流路に接続し、前記
滞留槽を前記濾過装置に接続したことを特徴とする請求
項2、3記載の循環温浴器。4. The inside of the electrolyzer is composed of a water discharge tank and a retention tank, each of which has an electrode and is partitioned by a diaphragm, and the water discharge tank is connected to a flow path circulating in the bath, and the retention tank is The circulating hot water bath according to claim 2, wherein the circulating hot bath is connected to the filtration device.
あることを特徴とする請求項2、3、4記載の循環温浴
器。5. The circulating hot water bath according to claim 2, wherein the electrodes in the electrolysis device are capable of converting polarities.
気体排出機構を備えたことを特徴とする請求項2、3、
4、5記載の循環温浴器。6. A gas discharge mechanism for discharging gas generated in the electrolyzer, wherein the gas discharge mechanism is provided.
Circulating warm bath described in 4, 5.
前記電解装置内の隔膜に付着した気泡を排出するように
作動させるようにしたことを特徴とする請求項4、5、
6記載の循環温浴器。7. The device according to claim 4, wherein the device is operated so as to discharge bubbles adhering to the diaphragm in the electrolyzer at the time of starting the operation of the device or switching the electrolysis polarity.
The circulating warm bath described in 6.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8152052A JPH09327407A (en) | 1996-06-13 | 1996-06-13 | Circulation warming bath |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8152052A JPH09327407A (en) | 1996-06-13 | 1996-06-13 | Circulation warming bath |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09327407A true JPH09327407A (en) | 1997-12-22 |
Family
ID=15532002
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8152052A Pending JPH09327407A (en) | 1996-06-13 | 1996-06-13 | Circulation warming bath |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09327407A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6627073B2 (en) | 1999-12-16 | 2003-09-30 | Sanyo Electric Co, Ltd. | Water treatment device |
JP2007271099A (en) * | 2006-03-30 | 2007-10-18 | Matsushita Electric Ind Co Ltd | Water heater |
JP2012187250A (en) * | 2011-03-10 | 2012-10-04 | Panasonic Corp | Hot water supply apparatus |
-
1996
- 1996-06-13 JP JP8152052A patent/JPH09327407A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6627073B2 (en) | 1999-12-16 | 2003-09-30 | Sanyo Electric Co, Ltd. | Water treatment device |
JP2007271099A (en) * | 2006-03-30 | 2007-10-18 | Matsushita Electric Ind Co Ltd | Water heater |
JP2012187250A (en) * | 2011-03-10 | 2012-10-04 | Panasonic Corp | Hot water supply apparatus |
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