JP2001276830A - Bathtub water circulating and cleaning device - Google Patents
Bathtub water circulating and cleaning deviceInfo
- Publication number
- JP2001276830A JP2001276830A JP2000100871A JP2000100871A JP2001276830A JP 2001276830 A JP2001276830 A JP 2001276830A JP 2000100871 A JP2000100871 A JP 2000100871A JP 2000100871 A JP2000100871 A JP 2000100871A JP 2001276830 A JP2001276830 A JP 2001276830A
- Authority
- JP
- Japan
- Prior art keywords
- bath
- bath water
- circulation
- fuel cell
- heater
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Landscapes
- Fuel Cell (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、浴室内に設置し
て、浴槽内の浴水を循環ポンプにより循環流路内に循環
し、この循環流路に装着した濾過手段により浴水を浄化
する浴水循環浄化装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is arranged in a bathroom, in which bath water in a bath tub is circulated in a circulation passage by a circulation pump, and the bath water is purified by a filtering means mounted in the circulation passage. The present invention relates to a bath water circulation purification device.
【０００２】[0002]
【従来の技術】浴槽内の浴水を循環ポンプで吸い上げて
循環流路内を循環させ、この循環流路に設けた濾過手段
により浴水を濾過したり、同じく循環流路に設けた加熱
器によって浴水を入浴に適した温度に加熱・保温するこ
とで、２４時間いつでも入浴出来る様にした浴水循環浄
化装置が販売されている。2. Description of the Related Art Bath water in a bathtub is sucked up by a circulating pump and circulated in a circulation channel. The bath water is filtered by a filtering means provided in the circulation channel, or a heater provided in the circulation channel. A bath water circulation / purification device that allows bath water to be bathed at any time for 24 hours by heating and keeping the bath water at a temperature suitable for bathing is on the market.
【０００３】又、上記浴水循環浄化装置では、例えば特
開平１０−２２５６９３号公報で示される様に、紫外線
ランプや、電気分解槽により浴水で発生する細菌を殺菌
する種々の殺菌装置が用いられている。In the bath water circulation purifying apparatus, for example, as shown in Japanese Patent Application Laid-Open No. 10-225693, an ultraviolet lamp or various sterilizing apparatuses for sterilizing bacteria generated in the bath water by an electrolytic bath are used. ing.
【０００４】一方、上記電気分解槽では、浴水の電気分
解により生成される塩素化合物を細菌の殺菌に利用して
いるが、同時に不要な水素ガスと酸素ガスも生成される
という問題がある。On the other hand, in the above-mentioned electrolysis tank, a chlorine compound generated by electrolysis of bath water is used for sterilizing bacteria, but there is a problem that unnecessary hydrogen gas and oxygen gas are also generated at the same time.
【０００５】[0005]
【発明が解決しようとする課題】そこで本発明は、浴水
の電気分解により生成される水素ガスと酸素ガスを有効
利用する事を目的とするものである。SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to effectively utilize hydrogen gas and oxygen gas generated by electrolysis of bath water.
【０００６】[0006]
【課題を解決するための手段】本発明は、浴槽内の浴水
を循環ポンプで吸い上げて循環流路内を循環した後、浴
槽内に装着した浴槽内ユニットを介して浴槽に戻し、循
環流路の途中に設けた濾過手段により浴水を濾過すると
共に、循環流路の途中に設けた加熱器により浴水を所定
温度に加熱するものにおいて、循環流路の途中に電気分
解により塩素化合物を生成する電解殺菌器を設けると共
に、この電解殺菌器の電極部で生成される水素ガスと酸
素ガスを燃料電池に供給して成るものである。According to the present invention, the bath water in a bath tub is sucked up by a circulating pump, circulated in a circulating flow path, and then returned to the bath tub through a unit in the bath tub mounted in the bath tub. While filtering the bath water by a filtration means provided in the middle of the passage and heating the bath water to a predetermined temperature by a heater provided in the middle of the circulation passage, the chlorine compound is electrolyzed in the middle of the circulation passage by electrolysis. In addition to providing an electrolytic sterilizer for generation, hydrogen gas and oxygen gas generated at the electrode section of the electrolytic sterilizer are supplied to a fuel cell.
【０００７】又本発明は、燃料電池で発電された電力を
加熱器のヒータや電解殺菌器等に供給して成るものであ
る。[0007] Further, the present invention is to supply electric power generated by a fuel cell to a heater of a heater, an electrolytic sterilizer, and the like.
【０００８】そして又本発明は、電解殺菌器を濾過手段
に並列接続して成るものである。Further, the present invention comprises an electrolytic sterilizer connected in parallel to a filtering means.
【０００９】更に本発明は、燃料電池の電極部で生成さ
れる水を循環流路に供給して成るものである。Further, the present invention supplies water generated at the electrode section of the fuel cell to the circulation channel.
【００１０】[0010]
【発明の実施の形態】本発明の実施例を先ず図１に基づ
き説明すると、１は一般家庭の浴室等に設置される浴水
循環浄化装置本体で、浴槽２内の浴水３を循環ポンプ４
により浴槽内ユニット５の吸水口６から吸い上げて循環
し、同じく浴槽内ユニット５の吐水口７から噴出する循
環流路８と、この循環流路の上記循環ポンプ４の上流に
接続した加熱器９と、上記循環ポンプ４の下流に接続し
た濾過手段を構成する濾過ユニット１０と、この濾過ユ
ニットに並列接続した電解殺菌器１１とから主に構成し
ている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, an embodiment of the present invention will be described with reference to FIG.
And a circulating flow path 8 which is drawn up from the water suction port 6 of the unit 5 in the bathtub and circulates, and is also ejected from the water discharge port 7 of the unit 5 in the bathtub. And a filtration unit 10 constituting filtration means connected downstream of the circulation pump 4, and an electrolytic sterilizer 11 connected in parallel to the filtration unit.
【００１１】又上記循環流路８の濾過ユニット１０下流
には切換弁１２を接続し、濾過ユニット１０内に収納し
た凝集用の複数の電極板１３・・が汚れた場合には、濾
過ユニット１０を図示しないモータにより回転して電極
板１３・・同士を衝突させて洗浄すると共に、上記切換
弁１２を排水通路１４に接続することで、上記循環ポン
プ４により浴槽２内から吸い上げた浴水３を濾過ユニッ
ト１０に循環して電極板１３・・を洗浄した後、切換弁
１２より上記排水通路１４を経て外部に排水する。A switching valve 12 is connected to the circulation flow path 8 downstream of the filtration unit 10. If a plurality of aggregating electrode plates 13 housed in the filtration unit 10 become dirty, the filtration unit 10 Are rotated by a motor (not shown) to cause the electrode plates 13 to collide with each other to wash them, and the switching valve 12 is connected to the drain passage 14 so that the circulating pump 4 sucks up the bath water 3 from the bathtub 2. Are circulated through the filtration unit 10 to wash the electrode plates 13... And then drained to the outside through the drainage passage 14 from the switching valve 12.
【００１２】尚、上記実施例の電極板１３・・は、例え
ば銅とアルミニウム等の標準電極電位の異なる異種金属
を適当な間隔を置いて、かつ電気的に導通した状態に配
置し、上記異種金属によるボルタ電池作用によりアルミ
ニウムの表面に浴水３中の不純物を凝集させて除去する
様に構成している。In the electrode plate 13 of the above embodiment, dissimilar metals having different standard electrode potentials, such as copper and aluminum, are arranged at appropriate intervals and in an electrically conductive state. The configuration is such that impurities in the bath water 3 are aggregated and removed from the surface of the aluminum 3 by the voltaic cell action of the metal.
【００１３】上記電解殺菌器１１は、図２にても示す様
に隔膜１５により陰極室１６と陽極室１７を区画形成し
てこれらの室に上記浴水３を循環すると共に、上記陰極
室１６と陽極室１７内に各々陰極板１８と陽極板１９を
配置し、かつ上記陰極室１６と陽極室１７の上部には、
上記陰極板１８と陽極板１９の表面より発生する水素ガ
ス２０・・と酸素ガス２１・・を取り出すガス管２２、
２３を各々接続している。In the electrolytic sterilizer 11, as shown in FIG. 2, a cathode chamber 16 and an anode chamber 17 are defined by a diaphragm 15, and the bath water 3 is circulated in these chambers. And a cathode plate 18 and an anode plate 19 are respectively disposed in the anode chamber 17, and above the cathode chamber 16 and the anode chamber 17,
A gas pipe 22 for taking out hydrogen gas 20... And oxygen gas 21... Generated from the surfaces of the cathode plate 18 and the anode plate 19,
23 are connected to each other.
【００１４】尚、上記電解殺菌器１１は、浴水３を電気
分解して次亜塩素酸等の塩素化合物を生成し、この塩素
化合物により浴水３中の細菌を殺菌するものである。The electrolytic sterilizer 11 electrolyzes the bath water 3 to generate a chlorine compound such as hypochlorous acid, and sterilizes bacteria in the bath water 3 with the chlorine compound.
【００１５】２４は周知の固体高分子形燃料電池で、電
解質としての高分子イオン交換膜２５を、アノード２６
（水素極）とカソード２７（酸素極）で挟んで構成して
いると共に、上記アノード２６とカソード２７に各々ガ
ス管２２、２３を接続することで、上記電解殺菌器１１
で発生した水素ガス２０・・と酸素ガス２１・・をアノ
ード２６とカソード２７に供給する様に構成している。Reference numeral 24 denotes a well-known polymer electrolyte fuel cell, which comprises a polymer ion exchange membrane 25 as an electrolyte and an anode 26.
(Hydrogen electrode) and cathode 27 (oxygen electrode), and gas tubes 22 and 23 are connected to the anode 26 and cathode 27, respectively.
Are supplied to the anode 26 and the cathode 27.
【００１６】これにより、アノード２６に水素が供給さ
れると、水素は電子を放出して水素イオンとなって高分
子イオン交換膜２５の中を移動し、移動した水素イオン
はカソード２７に到達して酸素と反応し、水２８を生成
する。As a result, when hydrogen is supplied to the anode 26, the hydrogen emits electrons to become hydrogen ions and moves through the polymer ion exchange membrane 25, and the transferred hydrogen ions reach the cathode 27. Reacts with oxygen to produce water 28.
【００１７】又上記生成された水２８は、給水路２９を
介して上記循環流路８の切換弁１２上流に給水され、浴
水として利用される。The generated water 28 is supplied to the upstream side of the switching valve 12 of the circulation flow path 8 through a water supply passage 29, and is used as bath water.
【００１８】更に、上記燃料電池２４への水素ガス２０
・・と酸素ガス２１・・の供給によって、アノード２６
とカソード２７間に直流電力が発電されるが、これらの
電力は電力線３０、３１より取り出され、上記電解殺菌
器１１の陰極板１８と陽極板１９や、上記循環ポンプ
４、加熱器９内に設けられた図示しないヒータ等に供給
される。Further, the hydrogen gas 20 is supplied to the fuel cell 24.
.. and the supply of oxygen gas 21.
DC power is generated between the power supply and the cathode 27. These powers are taken out from the power lines 30 and 31, and are supplied to the cathode plate 18 and the anode plate 19 of the electrolytic sterilizer 11, the circulation pump 4, and the heater 9. It is supplied to a heater (not shown) provided.
【００１９】尚、上記実施例では電解殺菌器１１を隔膜
１５により陰極室１６と陽極室１７に区画して構成して
いるが、これに限定されることなく、例えば図３にて示
す様に電解槽３２内に所定の間隔を置いて陰極板１８と
陽極板１９を互いに対向して配置し、かつ電解槽３２の
上部にこれら電極板の表面より発生した水素ガス２０・
・と酸素ガス２１・・を取り出すガス管３３を接続し、
更にこのガス管の途中から、水素ガス２０・・を燃料電
池２４のアノード２６に導くガス管３４と、酸素ガス２
１・・を同じくカソード２７に導くガス管３５を分岐し
て構成しても良い。In the above embodiment, the electrolytic sterilizer 11 is divided into a cathode chamber 16 and an anode chamber 17 by a diaphragm 15, but the invention is not limited to this. For example, as shown in FIG. A cathode plate 18 and an anode plate 19 are arranged facing each other at a predetermined interval in an electrolytic cell 32, and hydrogen gas 20.
And a gas pipe 33 for taking out oxygen gas 21.
Further, a gas pipe 34 for leading the hydrogen gas 20... To the anode 26 of the fuel cell 24 and a oxygen gas 2.
Alternatively, the gas pipe 35 that leads 1... To the cathode 27 may be branched.
【００２０】これにより隔膜が不要となり、部品点数の
削減を計る事が出来ると同時に、電解効率が向上し、陰
極板１８と陽極板１９への印加電流を低減する事が出
来、消費電力の節減を計る事が出来るものである。This eliminates the necessity of a diaphragm, thereby reducing the number of parts. At the same time, the electrolysis efficiency is improved, the current applied to the cathode plate 18 and the anode plate 19 can be reduced, and power consumption can be reduced. Can be measured.
【００２１】又、図４は本発明の更に他の実施例を示す
もので、上記燃料電池２４の電池槽３６の上部に高分子
イオン交換膜２５を配設すると共に、このイオン交換膜
の下側の左右にアノード２６とカソード２７を配設した
もので、水素ガス２０・・と酸素ガス２１・・が電池槽
３６内を確実に上昇して高分子イオン交換膜２５に吸収
され、これにより発電効率を向上する事が出来るもので
ある。FIG. 4 shows still another embodiment of the present invention, in which a polymer ion exchange membrane 25 is provided above a cell tank 36 of the fuel cell 24, and a polymer ion exchange membrane 25 is provided below the ion exchange membrane. The anode 26 and the cathode 27 are disposed on the left and right sides of the battery. The hydrogen gas 20... And the oxygen gas 21... Surely rise in the battery tank 36 and are absorbed by the polymer ion exchange membrane 25. The power generation efficiency can be improved.
【００２２】尚、上記図４にて示す実施例では、電解殺
菌器１１の陰極板１８と陽極板１９の間に隔膜１５を配
置しているが、例えば図３にて示す様に無隔膜の構成に
しても良い。In the embodiment shown in FIG. 4, the diaphragm 15 is disposed between the cathode plate 18 and the anode plate 19 of the electrolytic sterilizer 11, but, for example, as shown in FIG. It may be configured.
【００２３】而して、本発明の動作を図１に基づいて説
明すると、先ず上記浴槽２内の浴水３を入浴に適した温
度に加熱したり、浄化する場合には、循環ポンプ４によ
り浴槽２内の浴水３を吸い上げて循環流路８に循環し、
例えばこの循環流路の加熱器９上流部分に装着した図示
しないサーミスタ等の温度センサーにより浴水３の温度
を検出しながら加熱器９内のヒータへの通電を制御し、
浴水３を入浴に適した温度に保温すると共に、濾過ユニ
ット１０により浴水３を浄化する。The operation of the present invention will be described with reference to FIG. 1. First, when the bath water 3 in the bathtub 2 is heated to a temperature suitable for bathing or purified, the circulation pump 4 is used. The bath water 3 in the bath tub 2 is sucked up and circulated through the circulation channel 8,
For example, the power supply to the heater in the heater 9 is controlled while the temperature of the bath water 3 is detected by a temperature sensor such as a thermistor (not shown) mounted on the upstream portion of the heater 9 in the circulation channel,
The bath water 3 is kept at a temperature suitable for bathing, and the filtration unit 10 purifies the bath water 3.
【００２４】この時浴水３は、浴槽内ユニット５の吸水
口６から吸い上げられて循環流路８内を循環し、加熱器
９−循環ポンプ４−濾過ユニット１０及び電解殺菌器１
１−切換弁１２を経て浴槽内ユニット５の吐水口７から
浴槽２内に噴出する。At this time, the bath water 3 is sucked up from the water inlet 6 of the unit 5 in the bath tub, circulates in the circulation flow path 8, and is heated 9-circulation pump 4-filtration unit 10 and electrolytic sterilizer 1
1-Squirt into the bathtub 2 from the water discharge port 7 of the unit 5 in the bathtub via the switching valve 12.
【００２５】[0025]
【発明の効果】本発明の構成により、浴水を電気分解し
て塩素化合物を生成する電解殺菌器の電極から発生する
水素ガスと酸素ガスを、燃料電池に供給して発電するこ
とで、電解殺菌器により浴水内に生成される不要な水素
ガスと酸素ガスを除去出来ると同時に発電することが出
来るものである。According to the constitution of the present invention, the hydrogen gas and the oxygen gas generated from the electrode of the electrolytic sterilizer for generating the chlorine compound by electrolyzing the bath water are supplied to the fuel cell to generate electric power. Unnecessary hydrogen gas and oxygen gas generated in the bath water can be removed by the sterilizer, and power can be generated at the same time.
【００２６】又本発明の構成により、燃料電池で発電さ
れた電力を浴水循環浄化装置の加熱器や電解殺菌器に供
給することで、浴水循環浄化装置の消費電力を大幅に低
減する事が出来るものである。Further, according to the configuration of the present invention, the power generated by the fuel cell is supplied to the heater and the electrolytic sterilizer of the bath water circulation purifying apparatus, so that the power consumption of the bath water circulation purifying apparatus can be greatly reduced. Things.
【００２７】そして又本発明の構成により、電解殺菌器
を、浴水を濾過する濾過手段に並列接続したことで、浴
水の循環流量を低減することなく電解殺菌器を通過する
浴水の流速を落とすことができ、これにより、電極から
発生する水素ガスと酸素ガスを効率的に取り出して、燃
料電池に供給する事が出来るものである。Further, according to the structure of the present invention, the electrolytic sterilizer is connected in parallel to the filtering means for filtering the bath water, so that the flow rate of the bath water passing through the electrolytic sterilizer without reducing the circulation flow rate of the bath water. Thus, hydrogen gas and oxygen gas generated from the electrode can be efficiently extracted and supplied to the fuel cell.
【００２８】更に本発明の構成により、燃料電池の電極
部で生成される純粋な水を浴水として供給する様に構成
したことで、特別な排水手段を設ける必要がないと同時
に、浴水の純度を向上する事が出来るものである。Further, according to the structure of the present invention, pure water generated at the electrode portion of the fuel cell is supplied as bath water, so that it is not necessary to provide a special drain means, and at the same time, the bath water is not required. Purity can be improved.
【図１】本発明による浴水循環浄化装置の概略構成図で
ある。FIG. 1 is a schematic configuration diagram of a bath water circulation purification device according to the present invention.
【図２】同じく要部の概略構成図である。FIG. 2 is a schematic configuration diagram of a main part of the same.
【図３】本発明の他の実施例を示す概略構成図である。FIG. 3 is a schematic configuration diagram showing another embodiment of the present invention.
【図４】同じく更に他の実施例を示す概略構成図であ
る。FIG. 4 is a schematic configuration diagram showing still another embodiment.
２ 浴槽 ３ 浴水 ４ 循環ポンプ ５ 浴槽内ユニット ８ 循環流路 ９ 加熱器 １０ 濾過ユニット １１ 電解殺菌器 １８ 陰極板 １９ 陽極板 ２４ 燃料電池 2 Bathtub 3 Bathwater 4 Circulation pump 5 Unit in bathtub 8 Circulation channel 9 Heater 10 Filtration unit 11 Electrolytic sterilizer 18 Cathode plate 19 Anode plate 24 Fuel cell
───────────────────────────────────────────────────── 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 1/50 ５１０ Ｃ０２Ｆ 1/50 ５３１Ｍ ５２０ ５４０Ｂ ５３１ ５５０Ｄ ５４０ ５６０Ａ ５５０ ５６０Ｆ ５６０ ５６０Ｚ 9/00 ５０２Ａ ５０２Ｄ 9/00 ５０２ ５０２Ｍ ５０３Ａ Ｈ０１Ｍ 8/00 Ｚ ５０３ 8/06 Ｒ Ｈ０１Ｍ 8/00 Ｋ 8/06 Ｗ 8/10 Ｃ０２Ｆ 1/46 １０２ 8/10 (72)発明者 志賀 寿 鳥取県鳥取市南吉方３丁目201番地 鳥取 三洋電機株式会社内 (72)発明者 松村 則美 鳥取県鳥取市南吉方３丁目201番地 鳥取 三洋電機株式会社内 (72)発明者 大杉 和也 鳥取県鳥取市南吉方３丁目201番地 鳥取 三洋電機株式会社内 (72)発明者 山本 奈津恵 鳥取県鳥取市南吉方３丁目201番地 鳥取 三洋電機株式会社内 Ｆターム(参考） 4D061 DA07 DB01 DB10 EA02 EA06 EB12 EB19 EB27 EB31 FA01 FA14 5H026 AA06 CX05 5H027 AA06 BA11 BC01 DD00 DD09──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/50 510 C02F 1/50 531M 520 540B 531 550D 540 560A 550 560F 560 560Z 9/00 502A 502D 9 / 00 502 502M 503A H01M 8/00 Z 503 8/06 R H01M 8/00 K 8/06 W 8/10 C02F 1/46 102 8/10 (72) Inventor: Hisashi Shiga 3-201 Minamiyoshikata, Tottori City, Tottori Prefecture Address: Sanyo Tottori Electric Co., Ltd. (72) Noriyoshi Matsumura, 3-201 Minamiyoshikata, Tottori City, Tottori Prefecture, Japan Sanyo Electric Co., Ltd. Sanyo Electric Co., Ltd. (72) Inventor Natsue Yamamoto 3 Minamiyoshikata, Tottori City, Tottori Prefecture No. 201 Tottori Sanyo Electric Co., Ltd. F term (reference) 4D061 DA07 DB01 DB10 EA02 EA06 EB12 EB19 EB27 EB31 FA01 FA14 5H026 AA06 CX05 5H027 AA06 BA11 BC01 DD00 DD09
Claims (4)
循環流路内を循環した後、上記浴槽内に装着した浴槽内
ユニットを介して浴槽に戻し、上記循環流路の途中に設
けた濾過手段により浴水を濾過すると共に、上記循環流
路の途中に設けた加熱器により浴水を所定温度に加熱す
るものにおいて、上記循環流路の途中に電気分解により
塩素化合物を生成する電解殺菌器を設けると共に、この
電解殺菌器の電極部で生成される水素ガスと酸素ガスを
燃料電池に供給する事を特徴とする浴水循環浄化装置。1. A bath in a bath tub is sucked up by a circulation pump, circulated in a circulation passage, and then returned to the bath tub through a unit in the bath tub mounted in the bath tub, and provided in the middle of the circulation passage. A method in which the bath water is filtered by a filtration means and the bath water is heated to a predetermined temperature by a heater provided in the middle of the circulation channel. A bath water circulating purification apparatus characterized in that a bath is provided and hydrogen gas and oxygen gas generated at the electrode section of the electrolytic sterilizer are supplied to a fuel cell.
熱器のヒータや電解殺菌器等に供給する事を特徴とす
る、上記請求項１に記載の浴水循環浄化装置。2. The bath water circulation purifying apparatus according to claim 1, wherein the electric power generated by the fuel cell is supplied to a heater of the heater, an electrolytic sterilizer, and the like.
続した事を特徴とする、上記請求項１〜２に記載の浴水
循環浄化装置。3. The bath water circulation purifying apparatus according to claim 1, wherein said electrolytic sterilizer is connected in parallel to said filtering means.
上記循環流路に供給する事を特徴とする、上記請求項１
〜３に記載の浴水循環浄化装置。4. The fuel cell according to claim 1, wherein water generated at the electrode section of the fuel cell is supplied to the circulation channel.
4. The bath water circulation purifying apparatus according to any one of items 1 to 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000100871A JP2001276830A (en) | 2000-04-03 | 2000-04-03 | Bathtub water circulating and cleaning device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000100871A JP2001276830A (en) | 2000-04-03 | 2000-04-03 | Bathtub water circulating and cleaning device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2001276830A true JP2001276830A (en) | 2001-10-09 |
Family
ID=18615016
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000100871A Pending JP2001276830A (en) | 2000-04-03 | 2000-04-03 | Bathtub water circulating and cleaning device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2001276830A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003041204A1 (en) * | 2001-11-09 | 2003-05-15 | Hydrogenics Corporation | Combination of fuel cell and water electrolyzer with bidirectional heat exchange |
| WO2004046042A3 (en) * | 2002-11-19 | 2004-09-02 | Xogen Power Inc | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| JP4497558B1 (en) * | 2009-05-15 | 2010-07-07 | 中国電機製造株式会社 | Bathing facilities |
| JP2013004171A (en) * | 2011-06-10 | 2013-01-07 | Omega:Kk | Fuel cell |
| JP2014522309A (en) * | 2011-06-06 | 2014-09-04 | アクシン ウォーター テクノロジーズ インコーポレイテッド | Efficient treatment of wastewater using electrochemical cells |
| US9187347B2 (en) | 2002-11-19 | 2015-11-17 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| JP2016507354A (en) * | 2012-12-02 | 2016-03-10 | アクシン ウォーター テクノロジーズ インコーポレイテッドＡｘｉｎｅ Ｗａｔｅｒ Ｔｅｃｈｎｏｌｏｇｉｅｓ Ｉｎｃ． | Method for imparting filtration capacity in electrolytic cells for wastewater treatment |
| US9296629B2 (en) | 2002-11-19 | 2016-03-29 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
-
2000
- 2000-04-03 JP JP2000100871A patent/JP2001276830A/en active Pending
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2003041204A1 (en) * | 2001-11-09 | 2003-05-15 | Hydrogenics Corporation | Combination of fuel cell and water electrolyzer with bidirectional heat exchange |
| WO2004046042A3 (en) * | 2002-11-19 | 2004-09-02 | Xogen Power Inc | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| JP2006506221A (en) * | 2002-11-19 | 2006-02-23 | エクソジェン・テクノロジーズ・インコーポレイテッド | Waste fluid treatment through generation and utilization of oxyhydrogen gas |
| US7160472B2 (en) | 2002-11-19 | 2007-01-09 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| JP2011016129A (en) * | 2002-11-19 | 2011-01-27 | Xogen Technologies Inc | Treatment of waste stream through production and utilization of oxyhydrogen gas |
| US9187347B2 (en) | 2002-11-19 | 2015-11-17 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| US9296629B2 (en) | 2002-11-19 | 2016-03-29 | Xogen Technologies Inc. | Treatment of a waste stream through production and utilization of oxyhydrogen gas |
| JP4497558B1 (en) * | 2009-05-15 | 2010-07-07 | 中国電機製造株式会社 | Bathing facilities |
| JP2010284504A (en) * | 2009-05-15 | 2010-12-24 | Chugoku Electric Manufacture Co Ltd | Bathing equipment |
| JP2014522309A (en) * | 2011-06-06 | 2014-09-04 | アクシン ウォーター テクノロジーズ インコーポレイテッド | Efficient treatment of wastewater using electrochemical cells |
| JP2013004171A (en) * | 2011-06-10 | 2013-01-07 | Omega:Kk | Fuel cell |
| JP2016507354A (en) * | 2012-12-02 | 2016-03-10 | アクシン ウォーター テクノロジーズ インコーポレイテッドＡｘｉｎｅ Ｗａｔｅｒ Ｔｅｃｈｎｏｌｏｇｉｅｓ Ｉｎｃ． | Method for imparting filtration capacity in electrolytic cells for wastewater treatment |
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