JP2000334458A - Device for changing water quality of bathtub water - Google Patents
Device for changing water quality of bathtub waterInfo
- Publication number
- JP2000334458A JP2000334458A JP11147329A JP14732999A JP2000334458A JP 2000334458 A JP2000334458 A JP 2000334458A JP 11147329 A JP11147329 A JP 11147329A JP 14732999 A JP14732999 A JP 14732999A JP 2000334458 A JP2000334458 A JP 2000334458A
- Authority
- JP
- Japan
- Prior art keywords
- water
- bathtub
- path
- bath
- valve
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 958
- 150000003839 salts Chemical class 0.000 claims abstract description 179
- 230000002378 acidificating effect Effects 0.000 claims abstract description 123
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 118
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims abstract description 60
- 239000012528 membrane Substances 0.000 claims abstract description 47
- 239000011780 sodium chloride Substances 0.000 claims abstract description 30
- 238000001914 filtration Methods 0.000 claims description 209
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 82
- HWLDNSXPUQTBOD-UHFFFAOYSA-N platinum-iridium alloy Chemical compound [Ir].[Pt] HWLDNSXPUQTBOD-UHFFFAOYSA-N 0.000 claims description 44
- 229910052697 platinum Inorganic materials 0.000 claims description 41
- 238000005406 washing Methods 0.000 claims description 33
- 239000000203 mixture Substances 0.000 claims description 27
- 238000007599 discharging Methods 0.000 claims description 24
- 238000007865 diluting Methods 0.000 claims description 7
- 239000012510 hollow fiber Substances 0.000 claims description 7
- 239000003792 electrolyte Substances 0.000 claims 2
- 230000002708 enhancing effect Effects 0.000 abstract 1
- 150000002500 ions Chemical class 0.000 description 104
- 238000012937 correction Methods 0.000 description 60
- 238000011144 upstream manufacturing Methods 0.000 description 45
- 238000000034 method Methods 0.000 description 42
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 39
- 239000000460 chlorine Substances 0.000 description 39
- 229910052801 chlorine Inorganic materials 0.000 description 39
- 238000004140 cleaning Methods 0.000 description 14
- 238000010586 diagram Methods 0.000 description 13
- 238000000746 purification Methods 0.000 description 12
- 230000001954 sterilising effect Effects 0.000 description 8
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 7
- 241000894006 Bacteria Species 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 230000007423 decrease Effects 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 6
- 230000007935 neutral effect Effects 0.000 description 5
- 101150114468 TUB1 gene Proteins 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000003287 bathing Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000004659 sterilization and disinfection Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 3
- 102000004310 Ion Channels Human genes 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 238000011109 contamination Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- -1 dirt Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229910001415 sodium ion Inorganic materials 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
Landscapes
- 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、浴槽水のpHを調
整する浴槽水の水質改変装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a bathtub water quality modifying device for adjusting the pH of bathtub water.
【0002】[0002]
【従来の技術】浴槽内の温水を電気分解して循環させ、
酸性イオン水の有する温水を殺菌する効果やアストリン
ゼン効果、あるいはアルカリ性イオン水が有するトリー
トメント効果を享受するための装置は、従来種々のもの
が提案されており、例えば特開平4−312461号公
報に開示されているものがある。この公報に開示されて
いる装置においては、浴槽の温水を加熱保温する保温手
段と、水を電気分解して酸性イオン水とアルカリ性イオ
ン水とを生成する電気分解手段とを備えており、酸性イ
オン水とアルカリ性イオン水とを適宜浴槽内に還流でき
るようにしていた。2. Description of the Related Art Hot water in a bathtub is electrolyzed and circulated,
Various devices have been proposed as devices for enjoying the effect of sterilizing hot water having acidic ionized water, the astringent effect, or the treatment effect of alkaline ionized water. There are things that are. The apparatus disclosed in this publication includes a heat retaining means for heating and retaining hot water in a bathtub, and an electrolytic means for electrolyzing water to generate acidic ionized water and alkaline ionized water. Water and alkaline ionized water could be appropriately refluxed in the bathtub.
【0003】[0003]
【発明が解決しようとする課題】しかしこのような従来
技術においては、下記のような問題があった。 (1) 電気伝導度の低い浴槽水を電気分解しているた
め、電気分解に必要な電流を流すためには電極間に高い
電圧を印可しなければならず、電力コストが高いもので
あった。 (2) 浴槽に送り込まれないイオン水は、浴槽外に連
続的に排出されるため、排水量が多くなり、浴槽水の減
少が激しいものであった。 (3) アルカリ性イオン水を浴槽に供給している間
は、アルカリ性イオン水には塩素が含まれないため、浴
槽の湯を殺菌することができず、衛生上問題があった。 (4) 酸性イオン水を排水する場合、この酸性イオン
水中の有害で有臭の塩素ガスが気化し、雰囲気中に放出
されるという問題があった。However, such a conventional technique has the following problems. (1) Since bathtub water with low electric conductivity is electrolyzed, a high voltage must be applied between the electrodes in order to flow the current necessary for electrolysis, and the power cost is high. . (2) Since the ionized water that is not fed into the bathtub is continuously discharged out of the bathtub, the amount of drainage increases, and the bathtub water decreases sharply. (3) While the alkaline ionized water is being supplied to the bathtub, the alkaline ionized water does not contain chlorine, so that the hot water in the bathtub cannot be sterilized, and there is a hygiene problem. (4) When draining the acidic ionized water, there is a problem that harmful and odorous chlorine gas in the acidic ionized water is vaporized and released into the atmosphere.
【0004】本発明は上記の点に鑑みてなされたもので
あり、上記課題を解決することができる浴槽水の水質改
変装置を提供することを目的とするものである。[0004] The present invention has been made in view of the above points, and has as its object to provide a bathtub water quality modifying apparatus which can solve the above-mentioned problems.
【0005】[0005]
【課題を解決するための手段】本発明の請求項1に係る
浴槽水の水質改変装置は、有隔膜電解槽2と、有隔膜電
解槽2内の隔膜45にて隔てられた一方の電解室内に塩
化ナトリウムを供給する塩水供給槽4と、電気分解に供
される浴槽水31を浴槽1から有隔膜電解槽2に供給
し、有隔膜電解槽2にて電気分解により生成するアルカ
リ性イオン水と酸性イオン水のうち一方のイオン水を浴
槽1に供給すると共に他方のイオン水を浴槽1外に排出
する浴槽水の流路と、この浴槽水の流路に水流を発生さ
せる循環ポンプ5とを具備して成ることを特徴とするも
のである。According to the first aspect of the present invention, there is provided an apparatus for modifying water quality of bath water, comprising: an electrolytic cell separated from a diaphragm electrolytic cell 2 and a diaphragm 45 in the electrolytic cell 2; A salt water supply tank 4 for supplying sodium chloride to the tank, and a bath water 31 to be subjected to electrolysis are supplied from the bath 1 to the diaphragm electrolysis tank 2, and alkaline ionized water generated by electrolysis in the diaphragm electrolysis tank 2. A bath water channel for supplying one of the acidic ion water to the bath 1 and discharging the other ion water out of the bath 1 and a circulation pump 5 for generating a water flow in the bath water flow. It is characterized by comprising.
【0006】また本発明の請求項2に係る浴槽水の水質
改変装置は、請求項1の構成に加えて、有隔膜電解槽2
における電気分解の進行中に、有隔膜電解槽2にて電気
分解により生成するアルカリ性イオン水と酸性イオン水
のうち一方のイオン水を連続的に浴槽1に供給し、有隔
膜電解槽2における電気分解の終了後に他方のイオン水
を浴槽1外に排出する浴槽水の流路を具備して成ること
を特徴とするものである。According to a second aspect of the present invention, there is provided an apparatus for modifying water quality of bathtub water, wherein
During the electrolysis in the above, one of the alkaline ionic water and the acidic ionic water generated by the electrolysis in the diaphragm electrolyzer 2 is continuously supplied to the bath 1, and the electricity in the diaphragm electrolyzer 2 is supplied. It is characterized by comprising a bathtub water flow path for discharging the other ion water out of the bathtub 1 after the decomposition is completed.
【0007】また本発明の請求項3に係る浴槽水の水質
改変装置は、有隔膜電解槽2と、有隔膜電解槽2内の隔
膜45にて隔てられた両方の電解室内に塩化ナトリウム
を供給する塩水供給槽4と、電気分解に供される浴槽水
31を浴槽1から有隔膜電解槽2に供給し、有隔膜電解
槽2における電気分解終了後に、有隔膜電解槽2にて電
気分解により生成するアルカリ性イオン水と酸性イオン
水のうち一方のイオン水を浴槽1に供給すると共に他方
のイオン水を浴槽1外に排出する浴槽水の流路と、この
浴槽水の流路に水流を発生させる循環ポンプ5とを具備
して成ることを特徴とするものである。Further, according to a third aspect of the present invention, there is provided an apparatus for modifying water quality of bathtub water, wherein sodium chloride is supplied to both the electrolytic chamber 2 and both electrolytic chambers separated by the diaphragm 45 in the electrolytic bath 2. The salt water supply tank 4 and the bath water 31 to be subjected to the electrolysis are supplied from the bath 1 to the diaphragm electrolysis tank 2, and after the electrolysis in the diaphragm electrolysis tank 2 is completed, the electrolysis is performed in the diaphragm electrolysis tank 2. One of the generated alkaline ionized water and the acidic ionized water is supplied to the bathtub 1 and the other ionized water is discharged out of the bathtub 1, and a water flow is generated in the bathtub water flow path. And a circulating pump 5 for performing the operation.
【0008】また本発明の請求項4に係る浴槽水の水質
改変装置は、請求項1乃至3のいずれかの構成に加え
て、有隔膜電解槽2にて電気分解により生成するアルカ
リ性イオン水と酸性イオン水のうちのアルカリ性イオン
水を浴槽1に供給すると共に酸性イオン水を浴槽1外に
排出する動作と、電気分解により生成するアルカリ性イ
オン水と酸性イオン水の両方を浴槽1に供給する動作と
を一回ずつ交互に行うか、あるいは一方の動作を複数回
行うのに対して他方の動作を一回行うことを特徴とする
ものである。According to a fourth aspect of the present invention, there is provided an apparatus for modifying water quality of bath water, in addition to the constitution of any one of the first to third aspects, wherein alkaline ionic water generated by electrolysis in the diaphragm electrolyzer 2 is used. An operation of supplying alkaline ionized water of the acidic ionized water to the bathtub 1 and discharging the acidic ionized water out of the bathtub 1 and an operation of supplying both the alkaline ionized water and the acidic ionized water generated by electrolysis to the bathtub 1. Are alternately performed once each, or one operation is performed a plurality of times, while the other operation is performed once.
【0009】また本発明の請求項5に係る浴槽水の水質
改変装置、請求項1乃至4のいずれかの構成に加えて、
表面が白金−イリジウム混合物にて形成された白金−イ
リジウム混合物電極3aを有する第一電解室2a及び表
面が白金にて形成された白金電極3bを有する第二電解
室2bが設けられた有隔膜電解槽2と、白金−イリジウ
ム混合物電極3aを陰極、白金電極3bを陽極として電
気分解を行ったときに有隔膜電解槽2にて生成されるア
ルカリ性イオン水を浴槽1に供給すると共に酸性イオン
水を浴槽1外に排出し、白金電極3bを陰極、白金−イ
リジウム混合物電極3aを陽極として電気分解を行った
ときに有隔膜電解槽2にて生成されるアルカリ性イオン
水と酸性イオン水の両方を浴槽1に供給する浴槽水の流
路を具備してなることを特徴とするものである。[0009] Further, in addition to the apparatus for modifying water quality of bathtub water according to claim 5 of the present invention,
Membrane electrolysis provided with a first electrolysis chamber 2a having a platinum-iridium mixture electrode 3a whose surface is formed of a platinum-iridium mixture and a second electrolysis chamber 2b having a platinum electrode 3b whose surface is formed of platinum. A tank 2 and an alkaline ionized water generated in the diaphragm electrolyzer 2 when electrolysis is performed using the platinum-iridium mixture electrode 3a as a cathode and the platinum electrode 3b as an anode, and supplying the acidic ionized water to the bath 1. It is discharged out of the bathtub 1 and both the alkaline ionized water and the acidic ionized water generated in the diaphragm electrolyzer 2 when the electrolysis is performed using the platinum electrode 3b as the cathode and the platinum-iridium mixture electrode 3a as the anode are used as the bath. 1 is provided with a flow path of bathtub water to be supplied to 1.
【0010】また本発明の請求項6に係る浴槽水の水質
改変装置は、請求項1乃至5のいずれかの構成に加え
て、表面が白金−イリジウム混合物にて形成された白金
−イリジウム混合物電極3aを有する第一電解室2a及
び表面が白金にて形成された白金電極3bを有する第二
電解室2bが設けられた有隔膜電解槽2と、白金−イリ
ジウム混合物電極3aを陰極、白金電極3bを陽極とし
て電気分解を行ったときに有隔膜電解槽2にて生成され
るアルカリ性イオン水を浴槽1に供給すると共に酸性イ
オン水を浴槽1外に排出し、白金電極3bを陰極、白金
−イリジウム混合物電極3aを陽極として電気分解を行
ったときに有隔膜電解槽2にて生成されるアルカリ性イ
オン水を浴槽1外に排出すると共に酸性イオン水を浴槽
1に供給する浴槽水の流路を具備して成ることを特徴と
するものである。According to a sixth aspect of the present invention, there is provided an apparatus for modifying water quality of bathtub water according to any one of the first to fifth aspects, further comprising a platinum-iridium mixture electrode whose surface is formed of a platinum-iridium mixture. A separated electrolytic cell 2 provided with a first electrolytic chamber 2a having a first electrolytic chamber 3a and a second electrolytic chamber 2b having a platinum electrode 3b having a surface formed of platinum, a platinum-iridium mixture electrode 3a serving as a cathode, a platinum electrode 3b Is supplied to the bathtub 1 while the alkaline ionized water generated in the electrolytic cell 2 when the electrolysis is performed is discharged to the bathtub 1 and the acidic ionized water is discharged out of the bathtub 1. The platinum electrode 3 b is used as a cathode, and platinum-iridium is used as a cathode. Bath tub water for discharging alkaline ionic water generated in the diaphragm electrolyzer 2 when electrolysis is performed using the mixture electrode 3a as an anode and supplying acidic ionic water to the bath tub 1 It is characterized in that formed by including the flow path.
【0011】また本発明の請求項7に係る水質改変装置
は、請求項1乃至6のいずれかの構成に加えて、有隔膜
電解槽2にて生成されるアルカリ性イオン水と酸性イオ
ン水のうち一方のイオン水を浴槽1に供給すると共に他
方のイオン水を浴槽水にて希釈した後に浴槽1外に排出
する浴槽水の流路を具備して成ることを特徴とするもの
である。A water quality modifying device according to a seventh aspect of the present invention, in addition to the configuration according to any one of the first to sixth aspects, further comprises an alkaline ionized water and an acidic ionized water generated in the diaphragm electrolyzer 2. It is characterized by comprising a bath water flow path for supplying one ionized water to the bathtub 1 and diluting the other ionized water with the bathtub water and then discharging the diluted water out of the bathtub 1.
【0012】また本発明の請求項8に係る浴槽水の水質
改変装置は、請求項1乃至7のいずれかの構成に加え
て、浴槽水31を浄化する濾過槽7と、濾過槽7に濾過
槽の洗浄用水として浴槽水31を供給し、有隔膜電解槽
2にて生成されるアルカリ性イオン水と酸性イオン水の
うち一方のイオン水を浴槽1に供給すると共に他方のイ
オン水を濾過槽7の洗浄後の浴槽水31にて希釈した後
に浴槽1外に排出する浴槽水の流路を具備して成ること
を特徴とするものである。According to an eighth aspect of the present invention, in addition to the constitution of any one of the first to seventh aspects, the apparatus for modifying water quality of bathtub water further comprises a filter tank 7 for purifying the bathtub water 31 and a filter tank 7 for filtering the bathtub water 31. A bath water 31 is supplied as washing water for the tank, and one of alkaline ionized water and acidic ionized water generated in the diaphragm electrolyzer 2 is supplied to the bath 1 and the other ionized water is filtered into the filter tank 7. And a bath water channel for discharging the bath water after diluting with the bath water 31 after washing.
【0013】また本発明の請求項9に係る浴槽水の水質
改変装置は、請求項1乃至8のいずれかの構成に加え
て、浴槽水31を浄化する濾過槽7を具備して成ること
を特徴とするものである。According to a ninth aspect of the present invention, there is provided an apparatus for modifying water quality of bathtub water, which further comprises a filtration tank 7 for purifying the bathtub water 31 in addition to any one of the first to eighth aspects. It is a feature.
【0014】また本発明の請求項10に係る水質改変装
置は、請求項9の構成に加えて、濾過膜46として中空
糸膜を備える濾過槽7と、濾過槽7に濾過槽7の洗浄用
水として有隔膜電解槽2にて生成された酸性イオン水を
供給する浴槽水の流路とを具備して成ることを特徴とす
るものである。According to a tenth aspect of the present invention, in addition to the constitution of the ninth aspect, the filter tank 7 provided with a hollow fiber membrane as the filtration membrane 46, and the water for washing the filtration tank 7 is provided in the filtration tank 7. And a bath water channel for supplying the acidic ion water generated in the diaphragm electrolyzer 2.
【0015】[0015]
【発明の実施の形態】以下、本発明の実施の形態を説明
する。Embodiments of the present invention will be described below.
【0016】図1に本発明に係る浴槽水の水質改変装置
の一例を示す。この浴槽水の水質改変装置には、後述す
る浴槽水31の流路に水流を発生させて流路中の浴槽水
を移送する循環ポンプ5、有隔膜電解槽2及び内部に塩
化ナトリウムが収容されている塩水供給槽4が配設され
ている。ここで有隔膜電解槽2は内部に隔膜45で隔て
られた第一電極室2aと第二電極室2bが設けられ、こ
の第一電極室2aと第二電極室2bにはそれぞれ不溶性
電極板3が配設されている。第一電極室2aに配設され
ている不溶性電極板3は、基材がチタン、表面の電解面
が白金−イリジウム混合物で形成された白金−イリジウ
ム混合電極3aである。また第二電極室2bに配設され
ている不溶性電極板3は、基材がチタン、表面の電解面
が白金で形成された白金電極3bである。また塩水供給
槽4は、二重円筒構造を有し、内側の筒体である内筒4
aに塩化ナトリウムを収納するようになっている。この
内筒4aは上面が開口すると共に、側面が格子状に開口
し、この開口部をメッシュにて覆っている。一方、外側
の筒体である外筒4bは、蓋体4cが設けられており、
蓋体4cを開くことにより、内部に内筒4aを収容し、
あるいは脱離できる。塩水供給槽4に接続される流路の
うち、塩水供給槽4に浴槽水31等を供給する流路はこ
の外筒4b内に、外筒4bの下部に設けられた流入口4
dにて接続され、流路から外筒4b内に浴槽水31等が
供給されると、内筒4a内の塩化ナトリウムがこの浴槽
水31等に溶解して塩水が生成される。塩水供給槽4に
て生成された塩水を導出する流路はこの外筒4bに、外
筒4bの上部に設けられた流出口4eにて接続される。FIG. 1 shows an example of a bathtub water quality modifying apparatus according to the present invention. The bathtub water quality modifying device includes a circulating pump 5 for generating a water flow in a flow path of a bathtub water 31 to be described later to transfer the bathtub water in the flow path, a diaphragm electrolyzer 2 and sodium chloride therein. A salt water supply tank 4 is provided. Here, the diaphragm electrolyzer 2 is provided therein with a first electrode chamber 2a and a second electrode chamber 2b which are separated by a diaphragm 45, and the first electrode chamber 2a and the second electrode chamber 2b have insoluble electrode plates 3 respectively. Are arranged. The insoluble electrode plate 3 provided in the first electrode chamber 2a is a platinum-iridium mixed electrode 3a in which a base material is titanium and a surface electrolytic surface is formed of a platinum-iridium mixture. The insoluble electrode plate 3 disposed in the second electrode chamber 2b is a platinum electrode 3b having a base material made of titanium and a surface electrolytic surface made of platinum. The salt water supply tank 4 has a double cylindrical structure, and has an inner cylinder 4 as an inner cylinder.
a is designed to store sodium chloride. The inner cylinder 4a has an upper surface opened and side surfaces opened in a lattice, and this opening is covered with a mesh. On the other hand, the outer cylinder 4b, which is the outer cylinder, is provided with a lid 4c,
By opening the lid 4c, the inner cylinder 4a is housed inside,
Alternatively, it can be detached. Among the flow paths connected to the salt water supply tank 4, the flow path for supplying the bath water 31 and the like to the salt water supply tank 4 is provided inside the outer cylinder 4 b with an inflow port 4 provided below the outer cylinder 4 b.
When the bathtub water 31 and the like are supplied from the flow path into the outer cylinder 4b, the sodium chloride in the inner cylinder 4a is dissolved in the bathtub water 31 and the like to generate salt water. A flow path for discharging the salt water generated in the salt water supply tank 4 is connected to the outer cylinder 4b through an outlet 4e provided at an upper portion of the outer cylinder 4b.
【0017】また更に浴槽水31が通る流路、及びこれ
らの流路の流通を開閉する、電磁弁等からなる開閉弁が
配設されている。ここでいう浴槽水31には、浴槽水3
1に塩化ナトリウムを溶解して得られる塩水、並びにこ
の塩水や浴槽水31を電気分解して得られる酸性イオン
水やアルカリ性イオン水が含まれる。Further, a flow path through which the bathtub water 31 passes and an on-off valve such as a solenoid valve for opening and closing the flow of these flow paths are provided. The bathtub water 31 here is a bathtub water 3
1 includes salt water obtained by dissolving sodium chloride, and acidic ion water or alkaline ion water obtained by electrolyzing this salt water or bath water 31.
【0018】浴槽水31が通る流路のうち、流入路11
は上流側が浴槽1中の浴槽水31に配設されて、その上
流側の端部が流入口43として開口しており、下流側が
循環ポンプ5に接続されている。電解導入路12は上流
側が循環ポンプ5に接続され、下流側において塩水槽路
13と電解槽路30に分岐している。塩水槽路13の下
流側は塩水供給槽4の流入口4dに接続されている。電
解槽路30の下流側は第一電極室路14と第二電極室路
15に分岐され、第一電極室路14の下流側は有隔膜電
解槽2の第一電極室2aに、第二電極室路15の下流側
は有隔膜電解槽2の第二電極室2bにそれぞれ接続され
ている。第一電極室導出路22の上流側は有隔膜電解槽
2の第一電極室2aに接続され、下流側は流出路16の
上流側に接続されている。流出路16の下流側は浴槽1
内の浴槽水31に接続され、下流側の端部は流出口44
として開口されている。また塩供給路17は上流側が塩
水供給槽4の流出口4eに接続され、下流側は第二電極
室路15の流路の途中に、第二電極室路15と合流する
ように接続されている。第二電極室導出路21の上流側
は有隔膜電解槽2の第二電極室2bに接続され、下流側
は排水導入路19の上流側に接続されている。排水導入
路19の下流側は排水路18の上流側に接続されてい
る。また浴槽水バイパス路20の上流側は電解導入路1
2の配管の途中に、電解導入路12から分岐するように
接続され、下流側は排水路18の上流側に接続されてい
る。排水路18の下流側は浴槽1外に導出されている。Of the flow paths through which bath water 31 passes, inflow path 11
The upstream side is disposed in the bathtub water 31 in the bathtub 1, the upstream end thereof is opened as an inflow port 43, and the downstream side is connected to the circulation pump 5. The upstream side of the electrolysis introduction path 12 is connected to the circulation pump 5, and the downstream side is branched into a salt water tank path 13 and an electrolysis tank path 30. The downstream side of the salt water tank path 13 is connected to the inlet 4 d of the salt water supply tank 4. The downstream side of the electrolytic cell path 30 is branched into a first electrode chamber path 14 and a second electrode chamber path 15, and the downstream side of the first electrode chamber path 14 is connected to the first electrode chamber 2 a of the diaphragm electrolyzer 2. The downstream side of the electrode chamber path 15 is connected to the second electrode chamber 2 b of the diaphragm electrolyzer 2. The upstream side of the first electrode chamber lead-out channel 22 is connected to the first electrode chamber 2 a of the diaphragm electrolyzer 2, and the downstream side is connected to the upstream side of the outflow channel 16. The bathtub 1 is located downstream of the outflow channel 16.
Is connected to the bathtub water 31 inside, and the downstream end is an outlet 44.
It is opened as. Further, the upstream side of the salt supply path 17 is connected to the outlet 4 e of the salt water supply tank 4, and the downstream side is connected to the middle of the second electrode chamber path 15 so as to join the second electrode chamber path 15. I have. The upstream side of the second electrode chamber outlet path 21 is connected to the second electrode chamber 2 b of the diaphragm electrolyzer 2, and the downstream side is connected to the upstream side of the drainage introduction path 19. The downstream side of the drainage introduction channel 19 is connected to the upstream side of the drainage channel 18. The upstream side of the bathtub water bypass 20 is an electrolysis introduction channel 1.
In the middle of the second pipe, it is connected so as to branch off from the electrolysis introduction path 12, and the downstream side is connected to the upstream side of the drainage path 18. The downstream side of the drainage channel 18 is led out of the bathtub 1.
【0019】また開閉弁のうち、第1弁32は塩水槽路
13に、第2弁33は第二電極室路15における塩供給
路17の接続位置よりも上流側に、第3弁34は排水導
入路19に、第4弁35は浴槽水バイパス路20にそれ
ぞれ設けられ、各流路の流通を、この開閉弁の配設位置
において開閉する。Among the on-off valves, the first valve 32 is connected to the salt water tank passage 13, the second valve 33 is connected to the second electrode chamber passage 15 upstream of the connection position of the salt supply passage 17, and the third valve 34 is connected to the salt water supply passage 17. In the drainage introduction path 19, the fourth valve 35 is provided in the bathtub water bypass path 20, respectively, and opens and closes the flow of each flow path at the position where the on-off valve is disposed.
【0020】ここで、上記の塩水供給槽4の構成は、上
記のようなものに限られるものではなく、例えは塩水を
貯蔵したタンクとして設け、この塩水供給槽4と有隔膜
電解槽2の第二電極室2bを接続して、上記の循環ポン
プ5とは別のポンプにて塩水供給槽4中の塩水を第二電
極室2bに供給するようにしても良い。また開閉弁の設
置方法も上記のものに限るものではなく、例えば三方弁
を用いることができる。Here, the configuration of the salt water supply tank 4 is not limited to the above-described one. For example, the salt water supply tank 4 is provided as a tank for storing salt water. The second electrode chamber 2b may be connected, and the salt water in the salt water supply tank 4 may be supplied to the second electrode chamber 2b by a pump different from the circulation pump 5 described above. Also, the method of installing the on-off valve is not limited to the above, and for example, a three-way valve can be used.
【0021】この浴槽水の水質改変装置の動作を図2〜
4を示して説明する。ここでこれらの図面中で白抜きで
示されている開閉弁は開状態の弁を、黒く塗りつぶして
示されている開閉弁は閉状態の弁をそれぞれ示し、また
流路中の矢印は各流路における浴槽水31の流れの向き
を示す。The operation of the bath water quality modifying device is shown in FIGS.
4 will be described. Here, the open / closed valves shown in white in these drawings indicate open valves, the open / closed valves shown in black represent closed valves, and the arrows in the flow passages indicate the respective valves. The direction of the flow of the bathtub water 31 in the road is shown.
【0022】浴槽水31をアルカリ性に水質改変する場
合、まず図2に示すように、第1弁32、第2弁33、
第3弁34、第4弁35が閉状態となり、この状態で循
環ポンプ5が作動する。このとき循環ポンプ5の働きに
より浴槽水31は流入路11、電解導入路12、電解槽
路30、第一電極室路14、第一電極室導出路22、流
出路16からなる循環流路を循環し、またそれに伴って
有隔膜電解槽2の第一電極室2aに浴槽水31が供給さ
れ、第一電極室2a中の余剰の浴槽水31は第一電極室
導出路22、流出路16を経由して浴槽1に返送され
る。When the water quality of the bathtub water 31 is changed to alkaline, first, as shown in FIG. 2, a first valve 32, a second valve 33,
The third valve 34 and the fourth valve 35 are closed, and the circulating pump 5 operates in this state. At this time, the bath pump water 31 is circulated by the operation of the circulation pump 5 so that the bath water 31 flows through the circulation flow path composed of the inflow path 11, the electrolysis introduction path 12, the electrolysis tank path 30, the first electrode chamber path 14, the first electrode chamber outlet path 22, and the outflow path 16. Bath water 31 is circulated and the bath water 31 is supplied to the first electrode chamber 2a of the diaphragm electrolyzer 2, and excess bath water 31 in the first electrode chamber 2 a is discharged from the first electrode chamber lead-out channel 22 and the outflow channel 16. Is returned to the bathtub 1 via.
【0023】次に図3に示すように、第1弁32、第3
弁34が開状態、第2弁33、第4弁35が閉状態とな
り、この状態で引き続き循環ポンプ5が作動する。この
とき、図2に示す循環流路の水流に加えて、電解導入路
12から塩水槽路13を通って塩水供給槽4に導入さ
れ、塩水供給槽4から塩供給路17を通って有隔膜電解
槽2の第二電極室2bに導入され、第二電極室2bから
第二電極室導出路21、排水導入路19を経由して排水
路18から浴槽1外に排出される水流が形成される。こ
のとき塩水供給槽4内の塩化ナトリウムが、塩水槽路1
3から塩水供給槽4に供給された浴槽水31に溶解して
塩水が生成し、この塩水が塩供給路17を通って第二電
極室2bに供給され、第二電極室2b内の余剰の塩水は
第二電極室導出路21、排水導入路19、排水路18を
経由して浴槽1外に排出される。Next, as shown in FIG.
The valve 34 is in the open state, the second valve 33 and the fourth valve 35 are in the closed state, and the circulating pump 5 is continuously operated in this state. At this time, in addition to the water flow in the circulation flow path shown in FIG. 2, the water is introduced from the electrolysis introduction path 12 through the salt water tank path 13 into the salt water supply tank 4, and from the salt water supply tank 4 through the salt supply path 17, the diaphragm. A water flow is introduced into the second electrode chamber 2b of the electrolytic cell 2 and discharged from the second electrode chamber 2b to the outside of the bathtub 1 from the drainage channel 18 via the second electrode chamber lead-out channel 21 and the drainage channel 19. You. At this time, the sodium chloride in the salt water supply tank 4 is
3 dissolves in the bath water 31 supplied to the salt water supply tank 4 to generate salt water, and the salt water is supplied to the second electrode chamber 2b through the salt supply path 17 and excess salt water in the second electrode chamber 2b. The salt water is discharged out of the bathtub 1 through the second electrode chamber lead-out passage 21, the drain introduction passage 19, and the drain passage 18.
【0024】次に第1弁32、第2弁33、第3弁3
4、第4弁35が閉状態となって、再び図2に示すよう
な状態となり、この状態で白金−イリジウム混合電極3
aが陰極、白金電極3bが陽極となるように、この電極
間に電圧が印可され、有隔膜電解槽2において電気分解
により第一電極室2aにアルカリ性イオン水が、第二電
極室2bに酸性イオン水が生成する。このとき有隔膜電
解槽2において電気分解される浴槽水31には、塩化ナ
トリウムが添加されているので、浴槽水31の導電性が
向上され、電気分解に必要な電力が低減されているもの
であり、また、有隔膜電解槽2内の浴槽水31中の塩化
物イオン及びナトリウムイオンの濃度が向上されて、電
気分解により陰極側で水酸化ナトリウム濃度の高いアル
カリ性イオン水を生成すると共に、陽極側で塩酸濃度の
高い酸性イオン水を生成するものである。ここで第一電
極室2aには浴槽水が連続的に供給されると共に、余剰
の浴槽水が浴槽1へ返送されているので、第一電極室2
aにてアルカリ性イオン水となった浴槽水が浴槽1内に
連続的に供給されることとなる。一方、第二電極室2b
内には、酸性イオン水が保持される。第二電極室2bに
設けられた白金電極3bは酸素発生効率が高いため、こ
の酸性イオン水中では塩素の発生が抑制されている。Next, the first valve 32, the second valve 33, the third valve 3
4. The fourth valve 35 is closed and returns to the state shown in FIG. 2, and in this state, the platinum-iridium mixed electrode 3
A voltage is applied between these electrodes so that a becomes a cathode and the platinum electrode 3b becomes an anode. In the diaphragm electrolyzer 2, alkaline ionized water is supplied to the first electrode chamber 2a by electrolysis and acidic water is supplied to the second electrode chamber 2b. Ionized water is generated. At this time, since sodium chloride is added to the bath water 31 which is electrolyzed in the diaphragm electrolyzer 2, the conductivity of the bath water 31 is improved, and the electric power required for the electrolysis is reduced. In addition, the concentration of chloride ions and sodium ions in the bath water 31 in the diaphragm electrolyzer 2 is improved, so that alkaline ionic water having a high sodium hydroxide concentration is generated on the cathode side by electrolysis, and It generates acidic ion water with high hydrochloric acid concentration on the side. Here, bathtub water is continuously supplied to the first electrode chamber 2a, and excess bathtub water is returned to the bathtub 1.
The bathtub water that has become the alkaline ionized water at a is continuously supplied into the bathtub 1. On the other hand, the second electrode chamber 2b
Inside, acidic ionized water is retained. Since the platinum electrode 3b provided in the second electrode chamber 2b has a high oxygen generation efficiency, the generation of chlorine in the acidic ionic water is suppressed.
【0025】次に電気分解の終了後、図4に示すよう
に、第2弁33、第3弁34、第4弁35が開状態、第
1弁32が閉状態となり、この状態で引き続き循環ポン
プ5が作動する。このとき、循環流路の水流に加えて、
電解槽路30から第二電極室路15を通って第二電極室
2bに導入され、更に第二電極室2bから第二電極室導
出路21、排水導入路19、排水路18を通って浴槽1
外に排出される水流と、電解導入路12から分岐して浴
槽水バイパス路20を経由し、排水路18に合流する水
流が形成される。このとき第二電極室2b内の酸性イオ
ン水は、第二電極室路15を経由して第二電極室2b内
に導入される浴槽水31に押し出されて、第二電極室導
出路21、排水導入路19、排水路18を経由して浴槽
1外に排出される。このとき、浴槽水バイパス路20を
経由して排水路18に、アルカリ性に水質改変された浴
槽水31が供給されているので、酸性イオン水はこの浴
槽水31により中和されると共に希釈された状態で排出
される。この排水中の塩素濃度は低く抑えられており、
有害で有臭の塩素ガスの発生が抑制され、また排出され
る酸性イオン水は、一旦第二電極室2b内に保持された
後、中和及び希釈するために必要なだけの浴槽水31を
混合して排出することができ、装置からの排水量が抑制
され、浴槽水31の減少が抑制されている。Next, after the electrolysis is completed, as shown in FIG. 4, the second valve 33, the third valve 34, and the fourth valve 35 are opened, and the first valve 32 is closed. The pump 5 operates. At this time, in addition to the water flow in the circulation channel,
The bath is introduced from the electrolytic cell passage 30 to the second electrode chamber 2b through the second electrode chamber passage 15, and further from the second electrode chamber 2b to the second electrode chamber outlet passage 21, the drain introduction passage 19, and the drain passage 18. 1
A water flow that is discharged to the outside and a water flow that branches off from the electrolysis introduction path 12 and passes through the bathtub water bypass path 20 to join the drainage path 18 are formed. At this time, the acidic ionized water in the second electrode chamber 2b is pushed out into the bath water 31 introduced into the second electrode chamber 2b via the second electrode chamber path 15, and the second electrode chamber outlet path 21, The water is discharged out of the bathtub 1 through the drainage introduction channel 19 and the drainage channel 18. At this time, since the bath water 31 whose alkaline water quality has been modified is supplied to the drain 18 via the bath water bypass 20, the acidic ion water is neutralized and diluted by the bath water 31. It is discharged in a state. The chlorine concentration in this wastewater is kept low,
The generation of harmful and odorous chlorine gas is suppressed, and the discharged acidic ionized water is once held in the second electrode chamber 2b, and then the bath water 31 necessary for neutralization and dilution is removed. The water can be mixed and discharged, the amount of drainage from the device is suppressed, and the decrease in bath water 31 is suppressed.
【0026】次に、浴槽水31のアルカリ性への水質改
変を停止する場合は循環ポンプが停止される。また浴槽
水31を更に強いアルカリ性に水質改変する場合は、上
記の動作が繰り返し行われる。Next, the circulation pump is stopped when the water quality of the bathtub water 31 is changed to alkaline. When the water quality of the bathtub water 31 is changed to be more alkaline, the above operation is repeatedly performed.
【0027】また浴槽水31を酸性に水質改変する場
合、流路の切り替えはアルカリ性に水質改変する場合と
同様であるが、有隔膜電解槽2における電圧の印可の向
きが逆になる。すなわち、まず図2に示すように、第1
弁32、第2弁33、第3弁34、第4弁35が閉状態
となり、この状態で循環ポンプ5が作動する。このとき
循環ポンプ5の働きにより浴槽水31は流入路11、電
解導入路12、電解槽路30、第一電極室路14、第一
電極室導出路22、流出路16からなる循環流路を循環
し、またそれに伴って有隔膜電解槽2の第一電極室2a
に浴槽水31が供給され、第一電極室2a中の余剰の浴
槽水31は第一電極室導出路22、流出路16を経由し
て浴槽1に返送される。When the bath tub water 31 is modified to have an acidic water quality, the switching of the flow path is similar to the case where the water quality is modified to be alkaline, but the direction of application of the voltage in the diaphragm electrolyzer 2 is reversed. That is, first, as shown in FIG.
The valve 32, the second valve 33, the third valve 34, and the fourth valve 35 are closed, and the circulation pump 5 operates in this state. At this time, the bath pump water 31 is circulated by the operation of the circulation pump 5 so that the bath water 31 flows through the circulation flow path composed of the inflow path 11, the electrolysis introduction path 12, the electrolysis tank path 30, the first electrode chamber path 14, the first electrode chamber outlet path 22, and the outflow path 16. Circulates, and accordingly, the first electrode chamber 2a of the diaphragm electrolyzer 2
The bathtub water 31 is supplied to the first electrode chamber 2a, and the excess bathtub water 31 in the first electrode chamber 2a is returned to the bathtub 1 via the first electrode chamber lead-out passage 22 and the outflow passage 16.
【0028】次に図3に示すように、第1弁32、第3
弁34が開状態、第2弁33、第4弁35が閉状態とな
り、この状態で引き続き循環ポンプ5が作動する。この
とき、図2に示す循環流路の水流に加えて、電解導入路
12から塩水槽路13を通って塩水供給槽4に導入さ
れ、塩水供給槽4から塩供給路17を通って有隔膜電解
槽2の第二電極室2bに導入され、第二電極室2bから
第二電極室導出路21、排水導入路19を経由して排水
路18から浴槽1外に排出される水流が形成される。こ
のとき塩水供給槽4内の塩化ナトリウムが、塩水槽路1
3から塩水供給槽4に供給された浴槽水31に溶解して
塩水が生成し、この塩水が塩供給路17を通って第二電
極室2bに供給され、第二電極室2b内の余剰の塩水は
第二電極室導出路21、排水導入路19、排水路18を
経由して浴槽1外に排出される。Next, as shown in FIG.
The valve 34 is in the open state, the second valve 33 and the fourth valve 35 are in the closed state, and the circulating pump 5 is continuously operated in this state. At this time, in addition to the water flow in the circulation flow path shown in FIG. 2, the water is introduced from the electrolysis introduction path 12 through the salt water tank path 13 into the salt water supply tank 4, and from the salt water supply tank 4 through the salt supply path 17, the diaphragm. A water flow is introduced into the second electrode chamber 2b of the electrolytic cell 2 and discharged from the second electrode chamber 2b to the outside of the bathtub 1 from the drainage channel 18 via the second electrode chamber lead-out channel 21 and the drainage channel 19. You. At this time, the sodium chloride in the salt water supply tank 4 is
3 dissolves in the bath water 31 supplied to the salt water supply tank 4 to generate salt water, and the salt water is supplied to the second electrode chamber 2b through the salt supply path 17 and excess salt water in the second electrode chamber 2b. The salt water is discharged out of the bathtub 1 through the second electrode chamber lead-out passage 21, the drain introduction passage 19, and the drain passage 18.
【0029】次に第1弁32、第2弁33、第3弁3
4、第4弁35が閉状態となって、再び図2に示すよう
な状態となり、この状態で白金−イリジウム混合電極3
aが陽極、白金電極3bが陰極となるように、この電極
間に電圧が印可され、有隔膜電解槽2において電気分解
により第一電極室2aに酸性イオン水が、第二電極室2
bにアルカリ性イオン水が生成する。このとき第一電極
室2aには浴槽水が連続的に供給されると共に、余剰の
浴槽水31が浴槽1へ返送されているので、第一電極室
2aにて酸性イオン水となった浴槽水31が浴槽1内に
連続的に供給されることとなる。一方、第二電極室2b
内には、アルカリ性イオン水が保持される。ここで第一
電極室2aに設けられた白金−イリジウム混合電極3a
は塩素発生効率が高いため、この酸性イオン水中では塩
素が効率よく発生し、殺菌効果の高い酸性イオン水が生
成される。Next, the first valve 32, the second valve 33, the third valve 3
4. The fourth valve 35 is closed and returns to the state shown in FIG. 2, and in this state, the platinum-iridium mixed electrode 3
a is an anode and a platinum electrode 3b is a cathode. A voltage is applied between these electrodes, and in the diaphragm electrolyzer 2, acid ion water is supplied to the first electrode chamber 2a by electrolysis, and the second electrode chamber 2
The alkaline ionized water is generated in b. At this time, bathtub water is continuously supplied to the first electrode chamber 2a, and excess bathtub water 31 is returned to the bathtub 1. Therefore, bathtub water that has become acidic ionized water in the first electrode chamber 2a. 31 will be continuously supplied into the bathtub 1. On the other hand, the second electrode chamber 2b
Inside, alkaline ionized water is held. Here, a platinum-iridium mixed electrode 3a provided in the first electrode chamber 2a
Since chlorine has a high chlorine generation efficiency, chlorine is generated efficiently in the acidic ionic water, and acidic ionic water having a high sterilizing effect is generated.
【0030】次に電気分解の終了後、図4に示すよう
に、第2弁33、第3弁34、第4弁35が開状態、第
1弁32が閉状態となり、この状態で引き続き循環ポン
プ5が作動する。このとき、循環流路の水流に加えて、
電解槽路30から第二電極室路15を通って第二電極室
2bに導入され、更に第二電極室2bから第二電極室導
出路21、排水導入路19、排水路18を通って浴槽1
外に排出される水流と、電解導入路12から分岐して浴
槽水バイパス路20を経由し、排水路18に合流する水
流が形成される。このとき第二電極室2b内のアルカリ
性イオン水は、第二電極室路15を経由して第二電極室
2b内に導入される浴槽水31に押し出されて、第二電
極室導出路21、排水導入路19、排水路18を経由し
て浴槽1外に排出される。このとき、浴槽水バイパス路
20を経由して排水路18に、酸性に水質改変された浴
槽水31が供給されているので、アルカリ性イオン水は
この浴槽水31により有る程度中和されると共に希釈さ
れた状態で排出される。ここで排出されるアルカリ性イ
オン水は、一旦第二電極室2b内に保持された後、必要
な分だけ中和、希釈されて排出されるものであり、浴槽
1からの排水量が抑制され、浴槽水31の減少が抑制さ
れている。Next, after the electrolysis is completed, as shown in FIG. 4, the second valve 33, the third valve 34, and the fourth valve 35 are opened, and the first valve 32 is closed. The pump 5 operates. At this time, in addition to the water flow in the circulation channel,
The bath is introduced from the electrolytic cell passage 30 to the second electrode chamber 2b through the second electrode chamber passage 15, and further from the second electrode chamber 2b to the second electrode chamber outlet passage 21, the drain introduction passage 19, and the drain passage 18. 1
A water flow that is discharged to the outside and a water flow that branches off from the electrolysis introduction path 12 and passes through the bathtub water bypass path 20 to join the drainage path 18 are formed. At this time, the alkaline ionized water in the second electrode chamber 2b is pushed out to the bath water 31 introduced into the second electrode chamber 2b via the second electrode chamber path 15, and the second electrode chamber outlet path 21, The water is discharged out of the bathtub 1 through the drainage introduction channel 19 and the drainage channel 18. At this time, the bath water 31 whose acidic quality has been modified is supplied to the drain 18 through the bath water bypass 20, so that the alkaline ionized water is neutralized to some extent by the bath water 31 and diluted. It is discharged in the state where it was done. The alkaline ionized water discharged here is, once held in the second electrode chamber 2b, neutralized and diluted by a necessary amount and then discharged. The amount of drainage from the bathtub 1 is suppressed, The decrease of the water 31 is suppressed.
【0031】次に、浴槽水31の酸性への水質改変を停
止する場合は循環ポンプが停止される。また浴槽水31
を更に強い酸性に水質改変する場合は、上記の動作が繰
り返し行われる。Next, when stopping the change of the bathtub water 31 to an acidic water quality, the circulation pump is stopped. In addition, bathtub water 31
When the water quality is further modified to be more acidic, the above operation is repeated.
【0032】図5に本発明に係る浴槽水の水質改変装置
の他例を示す。この浴槽水の水質改変装置には、図1と
同様の循環ポンプ5、有隔膜電解槽2及び塩水供給槽4
が配設されているほか、ヒータ6及び濾過槽7が配設さ
れている。濾過槽7には、濾過槽7内を通る浴槽水31
を濾過する、中空糸膜からなる濾過膜46が内装されて
いる。この濾過膜46は濾過槽7内を水流の上流側と下
流側とに仕切るように配置されている。濾過槽7内の、
濾過膜46の上流側には、複数の吐水口10を有するノ
ズル9が設けられている。このノズル9は、モータ8の
働きにより濾過膜46の上流側の外周を回転するように
構成され、この回転と同時に吐水口10から水流を濾過
膜46の上流側の表面に吐出して濾過膜46を上流側に
おいて洗浄できるようになっている。また濾過槽7に接
続される流路のうち、濾過槽7内に浴槽水31等を供給
する流路は上記のノズル9に、濾過槽7内の濾過された
浴槽水31等を導出する流路は、濾過槽7の下流側の上
部に設けられた濾過水排出口7aにおいて、濾過膜46
の洗浄に使用された後の水を濾過槽7外に導出する流路
は、濾過槽7の上流側の下部に設けられた洗浄水排出口
7bにおいて、それぞれ接続される。FIG. 5 shows another example of the bathtub water quality modifying apparatus according to the present invention. This bath water quality modifying device includes a circulation pump 5, a diaphragm electrolyzer 2 and a salt water supply tank 4 similar to those shown in FIG.
Are provided, and a heater 6 and a filtration tank 7 are provided. The tub water 31 passing through the inside of the filtration tank 7 is provided in the filtration tank 7.
A filtration membrane 46 made of a hollow fiber membrane for filtering water is provided. The filtration membrane 46 is arranged so as to partition the inside of the filtration tank 7 into an upstream side and a downstream side of the water flow. In the filtration tank 7,
A nozzle 9 having a plurality of water outlets 10 is provided upstream of the filtration membrane 46. The nozzle 9 is configured to rotate the outer periphery on the upstream side of the filtration membrane 46 by the action of the motor 8, and simultaneously with this rotation, discharges a water flow from the water discharge port 10 to the surface on the upstream side of the filtration membrane 46, and 46 can be cleaned on the upstream side. Among the flow paths connected to the filtration tank 7, a flow path for supplying the bath water 31 and the like into the filtration tank 7 is a flow for leading the filtered bath water 31 and the like in the filtration tank 7 to the nozzle 9. The passage is provided with a filtration membrane 46 at a filtered water discharge port 7a provided at the upper portion on the downstream side of the filtration tank 7.
The flow paths for leading the water used for washing out of the filtration tank 7 out of the filtration tank 7 are connected at washing water discharge ports 7b provided at the lower portion on the upstream side of the filtration tank 7, respectively.
【0033】また更に浴槽水の水流が通る流路、及びこ
れらの流路の流通を開閉する、電磁弁等からなる開閉弁
が配設されている。ここでいう浴槽水31には、浴槽水
31に塩化ナトリウムを溶解して得られる塩水、並びに
この塩水や浴槽水31を電気分解して得られる酸性イオ
ン水やアルカリ性イオン水が含まれる。Further, there are provided a flow path through which the bathtub water flows, and an on-off valve such as an electromagnetic valve for opening and closing the flow of these flow paths. The bath water 31 referred to here includes salt water obtained by dissolving sodium chloride in the bath water 31, and acidic ion water and alkaline ion water obtained by electrolyzing the salt water and the bath water 31.
【0034】浴槽水の流路のうち、流路流入路11は下
流側が浴槽1中の浴槽水31に配設されて、その下流側
の端部が流入口43として開口しており、上流側が循環
ポンプ5に接続されている。電解導入路12は上流側が
循環ポンプ5に接続され、下流側において塩水槽路13
と電解槽路30に分岐している。塩水槽路13の下流側
は塩水供給槽4の流入口4dに接続されている。電解槽
路30の下流側は第一電極室路14と第二電極室路15
に分岐され、第一電極室路14の下流側は有隔膜電解槽
2の第一電極室2aに、第二電極室路15の下流側は有
隔膜電解槽2の第二電極室2bにそれぞれ接続されてい
る。第一電極室導出路22の上流側は有隔膜電解槽2の
第一電極室2aに接続され、下流側はイオン水路26の
上流側に接続され、イオン水路26の下流側は流出路1
6の上流側に接続されている。流出路16の下流側は浴
槽1内の浴槽水31に接続され、下流側の端部は流出口
44として開口されている。この流出路16にはヒータ
6が配設されており、ヒータ6が作動している場合は流
出路16を通る水流はヒータ6にて加熱される。また塩
供給路17は上流側が塩水供給槽4の流出口4eに接続
され、下流側は電解槽路30の流路の途中に、電解槽路
30と合流するように接続されている。第二電極室導出
路21の上流側は有隔膜電解槽2の第二電極室2bに接
続され、下流側は排水導入路19の上流側に接続されて
いる。排水導入路19の下流側は排水路18の上流側に
接続されている。排水路18の下流側は浴槽1外に導出
されている。洗浄水排出路23の上流側は濾過槽7の洗
浄水排出口7bに接続され、下流側は排水路18の上流
側に、排水導入路19と共に接続されている。またイオ
ン水バイパス路24は第二電極室導出路21の下流側と
第一電極室導出路22の下流側とを接続している。Of the bathtub water flow path, the downstream side of the flow path inflow path 11 is disposed in the bathtub water 31 in the bathtub 1, the downstream end thereof is open as an inlet 43, and the upstream side is upstream. It is connected to the circulation pump 5. The upstream of the electrolysis introduction path 12 is connected to the circulation pump 5, and the downstream of the electrolysis introduction path 12 is a salt water tank path 13.
And an electrolytic cell path 30. The downstream side of the salt water tank path 13 is connected to the inlet 4 d of the salt water supply tank 4. The first electrode chamber path 14 and the second electrode chamber path 15 are located downstream of the electrolytic cell path 30.
The downstream side of the first electrode chamber path 14 is connected to the first electrode chamber 2a of the diaphragm electrolyzer 2, and the downstream side of the second electrode chamber path 15 is connected to the second electrode chamber 2b of the diaphragm electrolyzer 2. It is connected. The upstream side of the first electrode chamber lead-out channel 22 is connected to the first electrode chamber 2a of the diaphragm electrolyzer 2, the downstream side is connected to the upstream side of the ion water channel 26, and the downstream side of the ion water channel 26 is the outflow channel 1.
6 upstream. The downstream side of the outflow channel 16 is connected to bath water 31 in the bathtub 1, and the downstream end is opened as an outlet 44. The heater 6 is disposed in the outflow passage 16, and when the heater 6 is operating, the water flow passing through the outflow passage 16 is heated by the heater 6. Further, the upstream side of the salt supply path 17 is connected to the outlet 4 e of the salt water supply tank 4, and the downstream side is connected to the middle of the flow path of the electrolytic tank path 30 so as to merge with the electrolytic tank path 30. The upstream side of the second electrode chamber outlet path 21 is connected to the second electrode chamber 2 b of the diaphragm electrolyzer 2, and the downstream side is connected to the upstream side of the drainage introduction path 19. The downstream side of the drainage introduction channel 19 is connected to the upstream side of the drainage channel 18. The downstream side of the drainage channel 18 is led out of the bathtub 1. The upstream side of the cleaning water discharge path 23 is connected to the cleaning water discharge port 7 b of the filtration tank 7, and the downstream side is connected to the upstream side of the drainage path 18 together with the drainage introduction path 19. In addition, the ion water bypass passage 24 connects the downstream side of the second electrode chamber outlet passage 21 and the downstream side of the first electrode chamber outlet passage 22.
【0035】また開閉弁のうち、第1弁32は塩水槽路
13に、第3弁34は排水導入路19に、第4弁35は
電解槽路30に、第5弁36はイオン水バイパス路24
に、第6弁37は洗浄水排出路23にそれぞれ設けら
れ、各流路の流通を、この開閉弁の配設位置において開
閉する。Of the on-off valves, the first valve 32 is connected to the salt water tank passage 13, the third valve 34 is connected to the drainage introduction passage 19, the fourth valve 35 is connected to the electrolytic tank passage 30, and the fifth valve 36 is connected to the ionic water bypass. Road 24
The sixth valve 37 is provided in each of the washing water discharge passages 23, and opens and closes the flow of each flow passage at the position where the on-off valve is provided.
【0036】ここで、上記の塩水供給槽4の構成は、上
記のようなものに限られるものではなく、例えは塩水を
貯蔵したタンクとして設け、この塩水供給槽4と有隔膜
電解槽2の第二電極室2bを接続して、上記の循環ポン
プ5とは別のポンプにて塩水供給槽4中の塩水を第二電
極室2bに供給するようにしても良い。またイオン水路
26の下流側は濾過槽7の上流側において濾過流路27
や流入路11の途中に合流するように接続してもよく、
浴槽1内に直接接続してもよい。Here, the configuration of the salt water supply tank 4 is not limited to the above-described one. For example, the salt water supply tank 4 is provided as a tank storing salt water. The second electrode chamber 2b may be connected, and the salt water in the salt water supply tank 4 may be supplied to the second electrode chamber 2b by a pump different from the circulation pump 5 described above. The downstream side of the ion water channel 26 is upstream of the filtration tank 7 and the filtration channel 27
Or may be connected so as to merge in the middle of the inflow path 11,
It may be connected directly in the bathtub 1.
【0037】この浴槽水の水質改変装置の動作を図6〜
11を示して説明する。ここでこれらの図面中で白抜き
で示されている開閉弁は開状態の弁を、黒く塗りつぶし
て示されている開閉弁は閉状態の弁をそれぞれ示し、ま
た流路中の矢印は各流路における浴槽水31の流れの向
きを示す。The operation of the bath water quality modifying device is shown in FIGS.
11 will be described. Here, the open / closed valves shown in white in these drawings indicate open valves, the open / closed valves shown in black represent closed valves, and the arrows in the flow passages indicate the respective valves. The direction of the flow of the bathtub water 31 in the road is shown.
【0038】浴槽水31を濾過槽7にて浄化する場合
は、図6に示すように、第1弁32、第3弁34、第4
弁35、第5弁36、第6弁37が閉状態となり、この
状態で循環ポンプ5が作動する。このとき循環ポンプ5
の働きにより浴槽水31は流入路11、濾過流路27、
濾過水路25、流出路16で構成される循環流路を循環
する。このとき濾過流路27から濾過槽7に供給される
浴槽水31は、ノズル9の吐水口10から濾過槽7の上
流側に供給され、更に濾過膜46を通過して濾過槽7の
下流側に導入されるものであり、濾過槽7にて入浴等に
より浴槽水31に混入した垢、埃、細菌等を濾過し、浴
槽水31が浄化されて清潔に保つことができるものであ
る。またこのとき流出路16を通過する浴槽水31の温
度が所定の設定温度よりも低い場合は、ヒータ6が作動
して浴槽水31が加熱される。When purifying the bath water 31 in the filtration tank 7, the first valve 32, the third valve 34, and the fourth valve 32 are used as shown in FIG.
The valve 35, the fifth valve 36, and the sixth valve 37 are closed, and the circulation pump 5 operates in this state. At this time, the circulation pump 5
By the action of the bathtub water 31, the inflow channel 11, the filtration channel 27,
It circulates through a circulation channel composed of the filtration water channel 25 and the outflow channel 16. At this time, the bath water 31 supplied from the filtration channel 27 to the filtration tank 7 is supplied from the water discharge port 10 of the nozzle 9 to the upstream side of the filtration tank 7, further passes through the filtration membrane 46, and is downstream of the filtration tank 7. The dirt, dust, bacteria, and the like mixed in the bathtub water 31 by bathing or the like in the filter tank 7 are filtered, and the bathtub water 31 is purified and can be kept clean. Further, at this time, when the temperature of the bathtub water 31 passing through the outflow passage 16 is lower than a predetermined set temperature, the heater 6 is operated to heat the bathtub water 31.
【0039】浴槽水31をアルカリ性に水質改変する場
合は、まず図7に示すように、第1弁32、第5弁36
が開状態、第3弁34、第4弁35、第6弁37が閉状
態となり、この状態で循環ポンプ5が作動する。このと
き循環ポンプ5の働きにより浴槽水31は流入路11、
電解導入路12、塩水槽路13、塩供給路17、電解槽
路30、第一電極室路14、第二電極室路15、第一電
極室導出路、第一電極室導出路22、イオン水バイパス
路24、イオン水路26、流出路16にて構成される循
環流路と、流入路11、濾過流路27、濾過水路25、
流出路16で構成される循環流路の、二系統の循環流路
を循環する。流入路11、濾過流路27、濾過水路2
5、流出路16で構成される循環流路においては、図6
の場合と同様に、濾過槽7において浴槽水31の浄化が
行われる。また塩水供給槽4内の塩化ナトリウムが、塩
水槽路13から塩水供給槽4に供給された浴槽水31に
溶解して塩水が生成し、この塩水は塩供給路17、電解
槽路30を経由し、第一電極室路14から有隔膜電解槽
2の第一電極室2aに供給されると共に第二電極室路1
5から有隔膜電解槽2の第二電極室2bに供給され、第
一電極室2a及び第二電極室2b中の余剰の塩水は第一
電極室導出路22、イオン水路26、流出路16を経由
して浴槽1に返送される。When the water quality of the bathtub water 31 is changed to alkaline, first, as shown in FIG.
Is opened, the third valve 34, the fourth valve 35, and the sixth valve 37 are closed, and the circulating pump 5 operates in this state. At this time, the bathtub water 31 is supplied by the operation of the circulation pump 5,
Electrolysis introduction path 12, salt water tank path 13, salt supply path 17, electrolytic tank path 30, first electrode chamber path 14, second electrode chamber path 15, first electrode chamber outlet path, first electrode chamber outlet path 22, ion A circulation flow path composed of a water bypass path 24, an ion water path 26, and an outflow path 16, an inflow path 11, a filtration flow path 27, a filtration water path 25,
It circulates through two circulation passages of the circulation passage constituted by the outflow passage 16. Inflow channel 11, filtration channel 27, filtration channel 2
5, in the circulation channel constituted by the outflow channel 16, FIG.
As in the case of (1), the bathtub water 31 is purified in the filtration tank 7. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13 to generate salt water, and this salt water passes through the salt supply path 17 and the electrolytic tank path 30. Then, while being supplied from the first electrode chamber path 14 to the first electrode chamber 2a of the diaphragm electrolyzer 2, the second electrode chamber path 1
5 is supplied to the second electrode chamber 2b of the diaphragm electrolyzer 2, and the excess salt water in the first electrode chamber 2a and the second electrode chamber 2b passes through the first electrode chamber outlet passage 22, the ion water passage 26, and the outflow passage 16. Returned to bathtub 1 via
【0040】次に図8に示すように、第5弁36が開状
態、第1弁32、第3弁34、第4弁35、第6弁37
が閉状態となり、この状態で引き続き循環ポンプ5が作
動する。このとき流入路11、濾過流路27、濾過水路
25、流出路16で構成される循環流路は維持されて、
濾過槽7において浴槽水31の浄化が引き続き行われ
る。この状態で白金−イリジウム混合電極3aが陰極、
白金電極3bが陽極となるように、この電極間に電圧が
印可され、有隔膜電解槽2において電気分解により第一
電極室2aにアルカリ性イオン水が、第二電極室2bに
酸性イオン水が生成する。ここで第二電極室2bに設け
られた白金電極3bは酸素発生効率が高いため、この酸
性イオン水中では塩素の発生が抑制されている。このよ
うに生成されたイオン水は有隔膜電解槽2内に保持され
る。Next, as shown in FIG. 8, the fifth valve 36 is open, the first valve 32, the third valve 34, the fourth valve 35, and the sixth valve 37.
Is closed, and the circulation pump 5 continues to operate in this state. At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained,
Purification of the bathtub water 31 is continued in the filtration tank 7. In this state, the platinum-iridium mixed electrode 3a is a cathode,
A voltage is applied between the electrodes so that the platinum electrode 3b becomes an anode, and alkaline ionized water is generated in the first electrode chamber 2a and acidic ionized water is generated in the second electrode chamber 2b by electrolysis in the diaphragm electrolyzer 2. I do. Here, since the platinum electrode 3b provided in the second electrode chamber 2b has a high oxygen generation efficiency, generation of chlorine in the acidic ionic water is suppressed. The ion water thus generated is held in the diaphragm electrolyzer 2.
【0041】次に電気分解の終了後に、図9に示すよう
に、第3弁34、第4弁35、第6弁37が開状態、第
1弁32、第5弁36が閉状態となり、この状態で引き
続き循環ポンプ5が作動する。この状態でモータ8を作
動させてノズル9を回転させる。このとき流入路11、
電解導入路12、電解槽路30を経由して、第一電極室
路14から第一電極室2a内に、第二電極室路15から
第二電極室2b内に浴槽水31が導入される水流が発生
する。第一電極室2a内のアルカリ性イオン水は、浴槽
水31に押し出されて第一電極室導出路22、イオン水
路26、流出路16を経由して流出口44から浴槽1内
に供給されて、浴槽1内の浴槽水31をアルカリ性に水
質改変する。また第二電極室2b内の酸性イオン水は、
第二電極室導出路21、排水導入路19、排水路18を
経由して浴槽1外に排出される。一方、濾過流路27を
経由して濾過槽7に導入される浴槽水31は、回転する
ノズル9の吐水口10から濾過膜46に向けて吹き付け
られ、この水流により濾過膜46の表面に付着した汚物
がはぎ取られて濾過膜46が洗浄され、この汚物を含む
洗浄後の浴槽水31は、水圧抵抗の高い濾過膜46を透
過せずに洗浄水排出口7bを水圧抵抗の低い洗浄水排出
路23を通過し、排水路18にて酸性イオン水と混合さ
れて、浴槽1外に排出される酸性イオン水を希釈する。
このとき酸性イオン水中の塩素が濾過槽洗浄後の浴槽水
中に含まれる垢、埃、細菌等の有機物や無機物と反応し
て分解され、排水からの有害、有臭の塩素ガスの気化を
抑制される。Next, after the completion of the electrolysis, as shown in FIG. 9, the third valve 34, the fourth valve 35, and the sixth valve 37 are opened, the first valve 32, and the fifth valve 36 are closed, In this state, the circulation pump 5 operates continuously. In this state, the motor 8 is operated to rotate the nozzle 9. At this time, the inflow channel 11,
Bath water 31 is introduced from the first electrode chamber path 14 into the first electrode chamber 2a and from the second electrode chamber path 15 into the second electrode chamber 2b via the electrolysis introduction path 12 and the electrolytic cell path 30. Water flow occurs. The alkaline ionized water in the first electrode chamber 2a is pushed out into the bathtub water 31 and is supplied into the bathtub 1 from the outlet 44 through the first electrode chamber lead-out passage 22, the ion water passage 26, and the outflow passage 16, The water quality of the bathtub water 31 in the bathtub 1 is changed to alkaline. The acidic ion water in the second electrode chamber 2b is
The water is discharged out of the bathtub 1 via the second electrode chamber lead-out passage 21, the drain introduction passage 19, and the drain passage 18. On the other hand, the bath water 31 introduced into the filtration tank 7 through the filtration channel 27 is sprayed from the water discharge port 10 of the rotating nozzle 9 toward the filtration membrane 46, and adheres to the surface of the filtration membrane 46 by this water flow. The filtered dirt is stripped off and the filter membrane 46 is washed, and the washed bathtub water 31 containing the dirt does not pass through the filter membrane 46 having a high hydraulic resistance and the washing water outlet 7b is washed with the cleaning water having a low hydraulic resistance. The water passes through the discharge passage 23, is mixed with the acidic ion water in the drain passage 18, and dilutes the acidic ion water discharged to the outside of the bathtub 1.
At this time, chlorine in the acidic ionized water reacts with organic and inorganic substances such as dirt, dust, and bacteria contained in the bath water after the washing of the filtration tank and is decomposed, thereby suppressing the vaporization of harmful and odorous chlorine gas from the wastewater. You.
【0042】この場合、浴槽水31をアルカリ性に水質
改変する動作と浴槽水31を浄化する動作が同時に行わ
れるものである。また酸性イオン水は一旦第二電極室2
b内に保持された後、必要な分だけ中和、希釈されて排
出されるものであり、酸性イオン水を排出する際の浴槽
水31の排出量が低減されているものであり、また酸性
イオン水の希釈に、本来そのまま排出される濾過膜46
を洗浄後の浴槽水31を用いているので、浴槽水31の
排出量が更に低減されている。In this case, the operation of changing the water quality of the bathtub water 31 to alkaline and the operation of purifying the bathtub water 31 are performed simultaneously. Further, the acidic ionized water is temporarily stored in the second electrode chamber 2.
b, after being neutralized and diluted by a necessary amount and discharged, the discharge amount of the bath water 31 when discharging the acidic ionized water is reduced. Filtration membrane 46 originally discharged as it is for dilution of ion water
Since the bath water 31 after washing is used, the discharge amount of the bath water 31 is further reduced.
【0043】また浴槽水31を殺菌する場合は、まず図
7に示すように、第1弁32、第5弁36が開状態、第
3弁34、第4弁35、第6弁37が閉状態となり、こ
の状態で循環ポンプ5が作動する。このとき循環ポンプ
5の働きにより浴槽水31は流入路11、電解導入路1
2、塩水槽路13、塩供給路17、電解槽路30、第一
電極室路14、第二電極室路15、第一電極室導出路、
第一電極室導出路22、イオン水バイパス路24、イオ
ン水路26、流出路16にて構成される循環流路と、流
入路11、濾過流路27、濾過水路25、流出路16で
構成される循環流路の、二系統の循環流路を循環する。
流入路11、濾過流路27、濾過水路25、流出路16
で構成される循環流路においては、図6の場合と同様
に、濾過槽7において浴槽水31の浄化が行われる。ま
た塩水供給槽4内の塩化ナトリウムが、塩水槽路13か
ら塩水供給槽4に供給された浴槽水31に溶解して塩水
が生成し、この塩水は塩供給路17、電解槽路30を経
由し、第一電極室路14から有隔膜電解槽2の第一電極
室2aに供給されると共に第二電極室路15から有隔膜
電解槽2の第二電極室2bに供給され、第一電極室2a
及び第二電極室2b中の余剰の塩水は第一電極室導出路
22、イオン水路26、流出路16を経由して浴槽1に
返送される。When the bathtub water 31 is to be sterilized, first, as shown in FIG. 7, the first valve 32 and the fifth valve 36 are opened, and the third valve 34, the fourth valve 35 and the sixth valve 37 are closed. State, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied to the inflow channel 11 and the electrolysis introduction channel 1 by the operation of the circulation pump 5.
2, salt water tank path 13, salt supply path 17, electrolytic tank path 30, first electrode chamber path 14, second electrode chamber path 15, first electrode chamber lead-out path,
It is composed of a circulation flow path composed of the first electrode chamber lead-out path 22, an ion water bypass path 24, an ion water path 26, and an outflow path 16, and an inflow path 11, a filtration flow path 27, a filtration water path 25, and an outflow path 16. Circulates through two circulation channels.
Inflow channel 11, filtration channel 27, filtration water channel 25, outflow channel 16
In the circulating flow path constituted by, the bath water 31 is purified in the filtration tank 7 as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13 to generate salt water, and this salt water passes through the salt supply path 17 and the electrolytic tank path 30. Then, the first electrode chamber 2 is supplied to the first electrode chamber 2 a of the diaphragm electrolyzer 2 from the first electrode chamber path 14, and the second electrode chamber 15 is supplied to the second electrode chamber 2 b of the diaphragm electrolyzer 2. Room 2a
The surplus salt water in the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber outlet passage 22, the ion water passage 26, and the outflow passage 16.
【0044】次に図8に示すように、第5弁36が開状
態、第1弁32、第3弁34、第4弁35、第6弁37
が閉状態となり、この状態で引き続き循環ポンプ5が作
動する。このとき流入路11、濾過流路27、濾過水路
25、流出路16で構成される循環流路は維持されて、
濾過槽7において浴槽水31の浄化が引き続き行われ
る。この状態で白金−イリジウム混合電極3aが陽極、
白金電極3bが陰極となるように、この電極間に電圧が
印可され、有隔膜電解槽2において電気分解により第一
電極室2aに酸性イオン水が、第二電極室2bにアルカ
リ性イオン水が生成する。ここで第一電極室2aに設け
られた白金−イリジウム混合電極3aは塩素発生効率が
高いため、この酸性イオン水中では塩素が効率良く発生
される。このように生成されたイオン水は有隔膜電解槽
2内に保持される。Next, as shown in FIG. 8, the fifth valve 36 is open, the first valve 32, the third valve 34, the fourth valve 35, and the sixth valve 37.
Is closed, and the circulation pump 5 continues to operate in this state. At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained,
Purification of the bathtub water 31 is continued in the filtration tank 7. In this state, the platinum-iridium mixed electrode 3a is an anode,
A voltage is applied between the electrodes so that the platinum electrode 3b becomes a cathode, and acidic ionized water is generated in the first electrode chamber 2a and alkaline ionized water is generated in the second electrode chamber 2b by electrolysis in the diaphragm electrolyzer 2. I do. Here, since the platinum-iridium mixed electrode 3a provided in the first electrode chamber 2a has a high chlorine generation efficiency, chlorine is generated efficiently in the acidic ionized water. The ion water thus generated is held in the diaphragm electrolyzer 2.
【0045】次に電気分解の終了後に、図10に示すよ
うに、第4弁35、第5弁36が開状態、第1弁32、
第3弁34、第6弁37が閉状態となり、この状態で引
き続き循環ポンプ5が作動する。このとき流入路11、
濾過流路27、濾過水路25、流出路16で構成される
循環流路は維持されて、濾過槽7において浴槽水31の
浄化が引き続き行われる。またこのとき流入路11、電
解導入路12、電解槽路30を経由して、第一電極室路
14から第一電極室2a内に、第二電極室路15から第
二電極室2b内に浴槽水31が導入される水流が発生す
る。第一電極室2a内の酸性イオン水は浴槽水31に押
し出されて第一電極室導出路22を経由してイオン水路
26に至り、また第二電極室2b内のアルカリ性イオン
水は、第二電極室導出路21、イオン水バイパス路24
を経由してやはりイオン水路26に至るものであり、イ
オン水路26においてアルカリ性イオン水と酸性イオン
水とが混合される。この混合水は中性又は弱アルカリ性
のイオン水であり、また酸性イオン水が高濃度で塩素を
含んでいたため、高い塩素濃度を有している。この混合
水は、流出路16において、濾過槽7において浄化され
た後の浴槽水31と混合し、流出路16を通って流出口
44から浴槽1内に供給され、混合水中の塩素にて浴槽
1内の浴槽水31が殺菌される。この場合、浴槽水31
の浄化と浴槽水31の殺菌とが同時に行われる。Next, after the end of the electrolysis, as shown in FIG. 10, the fourth valve 35 and the fifth valve 36 are open, and the first valve 32
The third valve 34 and the sixth valve 37 are closed, and in this state, the circulation pump 5 is continuously operated. At this time, the inflow channel 11,
The circulation flow path composed of the filtration flow path 27, the filtration water path 25, and the outflow path 16 is maintained, and the purification of the bath water 31 is continuously performed in the filtration tank 7. At this time, via the inflow path 11, the electrolysis introduction path 12, and the electrolytic cell path 30, the first electrode chamber path 14 enters the first electrode chamber 2a and the second electrode chamber path 15 enters the second electrode chamber 2b. A water flow into which the bath water 31 is introduced is generated. The acidic ionic water in the first electrode chamber 2a is pushed out by the bathtub water 31 and reaches the ion water channel 26 via the first electrode chamber lead-out passage 22, and the alkaline ionic water in the second electrode chamber 2b is Electrode chamber lead-out path 21, ion water bypass path 24
The ionized water channel 26 also reaches the ionized water channel 26, where the alkaline ionized water and the acidic ionized water are mixed. This mixed water is neutral or weakly alkaline ionized water, and has a high chlorine concentration because the acidic ionized water contains chlorine at a high concentration. This mixed water is mixed with the bath water 31 after being purified in the filtration tank 7 in the outflow passage 16, supplied into the bath tub 1 through the outflow passage 16 through the outflow passage 16, and mixed with chlorine in the mixed water. Bath water 31 in 1 is sterilized. In this case, bath water 31
Purification and sterilization of bathtub water 31 are performed simultaneously.
【0046】上記の浴槽水31をアルカリ性に水質改変
しながら濾過膜46を洗浄する動作と、浴槽水31を殺
菌する動作は、一回ずつ交互に、あるいはどちらか一方
の動作が複数回繰り返して行われると共に他方の動作が
一回行われるものであり、この場合、浴槽水31をアル
カリ性に保ちながら、殺菌された衛生的な状態に保つこ
とができ、しかも濾過膜46が洗浄されて濾過膜46の
膜流量が保たれ、高い効率で濾過槽7による浴槽水31
の浄化が行われるものである。The operation of washing the filter membrane 46 while altering the bathtub water 31 to alkaline water quality and the operation of sterilizing the bathtub water 31 are alternately performed one time at a time, or one of the operations is repeated a plurality of times. The operation is performed once and the other operation is performed once. In this case, the bathtub water 31 can be maintained in an alkaline state, and can be maintained in a sterilized and sanitary state. In addition, the filtration membrane 46 is washed and filtered. The bath flow rate 31 is maintained by the filtration tank 7 at a high efficiency while the membrane flow rate of 46 is maintained.
Purification is performed.
【0047】また浴槽水31を酸性に水質改変する場
合、まず図7に示すように、第1弁32、第5弁36が
開状態、第3弁34、第4弁35、第6弁37が閉状態
となり、この状態で循環ポンプ5が作動する。このとき
循環ポンプ5の働きにより浴槽水31は流入路11、電
解導入路12、電解槽路30、第一電極室路14、第一
電極室導出路、第一電極室導出路22、イオン水バイパ
ス路24、イオン水路26、流出路16にて構成される
循環流路と、流入路11、濾過流路27、濾過水路2
5、流出路16で構成される循環流路の、二系統の循環
流路を循環する。流入路11、濾過流路27、濾過水路
25、流出路16で構成される循環流路においては、図
6の場合と同様に、濾過槽7において浴槽水31の浄化
が行われる。また塩水供給槽4内の塩化ナトリウムが、
塩水槽路13から塩水供給槽4に供給された浴槽水31
に溶解して塩水が生成し、この塩水は塩供給路17、電
解槽路30を経由し、第一電極室路14から有隔膜電解
槽2の第一電極室2aに供給されると共に第二電極室路
15から有隔膜電解槽2の第二電極室2bに供給され、
第一電極室2a及び第二電極室2b中の余剰の塩水は第
一電極室導出路22、イオン水路26、流出路16を経
由して浴槽1に返送される。When the bath tub water 31 is modified to have an acidic water quality, the first valve 32 and the fifth valve 36 are opened, the third valve 34, the fourth valve 35, and the sixth valve 37 are first opened as shown in FIG. Is closed, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied by the circulation pump 5 so that the bath water 31 flows into the inflow passage 11, the electrolytic introduction passage 12, the electrolytic bath passage 30, the first electrode chamber passage 14, the first electrode chamber outlet passage, the first electrode chamber outlet passage 22, and the ionic water. A circulation channel composed of a bypass channel 24, an ion channel 26, and an outflow channel 16, the inflow channel 11, the filtration channel 27, and the filtration channel 2;
5. Circulate through two circulation passages of the circulation passage constituted by the outflow passage 16. In the circulation flow path constituted by the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Also, the sodium chloride in the salt water supply tank 4
Bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13
To form salt water, which is supplied from the first electrode chamber line 14 to the first electrode chamber 2a of the diaphragm electrolyzer 2 via the salt supply channel 17 and the electrolytic cell channel 30 and the second electrode chamber 2a. It is supplied from the electrode chamber path 15 to the second electrode chamber 2 b of the diaphragm electrolyzer 2,
Excess salt water in the first electrode chamber 2a and the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber lead-out passage 22, the ion water passage 26, and the outflow passage 16.
【0048】次に図8に示すように、第5弁36が開状
態、第1弁32、第3弁34、第4弁35、第6弁37
が閉状態となり、この状態で引き続き循環ポンプ5が作
動する。このとき流入路11、濾過流路27、濾過水路
25、流出路16で構成される循環流路は維持されて、
濾過槽7において浴槽水31の浄化が引き続き行われ
る。この状態で白金−イリジウム混合電極3aが陽極、
白金電極3bが陰極となるように、この電極間に電圧が
印可され、有隔膜電解槽2において電気分解により第一
電極室2aに酸性イオン水が、第二電極室2bにアルカ
リ性イオン水が生成する。ここで第一電極室2aに設け
られた白金−イリジウム混合電極3aは塩素発生効率が
高いため、この酸性イオン水中では塩素が効率良く発生
される。このように生成されたイオン水は有隔膜電解槽
2内に保持される。Next, as shown in FIG. 8, the fifth valve 36 is open, the first valve 32, the third valve 34, the fourth valve 35, and the sixth valve 37.
Is closed, and the circulation pump 5 continues to operate in this state. At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained,
Purification of the bathtub water 31 is continued in the filtration tank 7. In this state, the platinum-iridium mixed electrode 3a is an anode,
A voltage is applied between the electrodes so that the platinum electrode 3b becomes a cathode, and acidic ionized water is generated in the first electrode chamber 2a and alkaline ionized water is generated in the second electrode chamber 2b by electrolysis in the diaphragm electrolyzer 2. I do. Here, since the platinum-iridium mixed electrode 3a provided in the first electrode chamber 2a has a high chlorine generation efficiency, chlorine is generated efficiently in the acidic ionized water. The ion water thus generated is held in the diaphragm electrolyzer 2.
【0049】次に電気分解の終了後、図11に示すよう
に、第1弁32、第5弁36が開状態、第3弁34、第
4弁35、第6弁37が閉状態となり、この状態で引き
続き循環ポンプ5が作動する。このとき流入路11、濾
過流路27、濾過水路25、流出路16で構成される循
環流路は維持されて、濾過槽7において浴槽水31の浄
化が引き続き行われる。またこのとき流入路11、電解
導入路12、電解槽路30を経由して、第一電極室路1
4から第一電極室2a内に、第二電極室路15から第二
電極室2b内に浴槽水31が導入される水流が発生す
る。第一電極室2a内の酸性イオン水は、浴槽水31に
押し出されて第一電極室導出路22、イオン水路26、
流出路16を経由して流出口44から浴槽1内に供給さ
れて、浴槽1内の浴槽水31を酸性に水質改変する。ま
た第二電極室2b内のアルカリ性イオン水は、第二電極
室導出路21、排水導入路19、排水路18を経由して
浴槽1外に排出される。Next, after the end of the electrolysis, as shown in FIG. 11, the first valve 32 and the fifth valve 36 are opened, the third valve 34, the fourth valve 35, and the sixth valve 37 are closed. In this state, the circulation pump 5 operates continuously. At this time, the circulation flow path composed of the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16 is maintained, and the purification of the bath water 31 in the filtration tank 7 is continued. Also, at this time, the first electrode chamber passage 1 passes through the inflow passage 11, the electrolysis introduction passage 12, and the electrolysis tank passage 30.
4, a water flow is generated in which the bath water 31 is introduced into the second electrode chamber 2 b from the second electrode chamber path 15 into the first electrode chamber 2 a. The acidic ionic water in the first electrode chamber 2a is pushed out by the bathtub water 31, and the first electrode chamber outlet passage 22, the ion water passage 26,
The water is supplied into the bathtub 1 from the outlet 44 via the outflow passage 16, and the water quality of the bathtub water 31 in the bathtub 1 is acidified. The alkaline ionized water in the second electrode chamber 2b is discharged to the outside of the bathtub 1 via the second electrode chamber outlet passage 21, the drain introduction passage 19, and the drain passage 18.
【0050】またこのとき図9に示すように、第6弁3
7を開状態とすると共に、この状態でモータ8を作動さ
せてノズル9を回転させてもよい。この場合、濾過流路
27を経由して濾過槽7に導入される浴槽水31は、回
転するノズル9の吐水口10から濾過膜46に向けて吹
き付けられ、この水流により濾過膜46の表面に付着し
た汚物がはぎ取られ、この汚物を含む洗浄後の浴槽水3
1は、水圧抵抗の高い濾過膜46を透過せずに洗浄水排
出口7bを水圧抵抗の低い洗浄水排出路23を通過し、
排水路18にてアルカリ性イオン水と混合されて、浴槽
1外に排出されるアルカリ性イオン水を希釈する。At this time, as shown in FIG.
7 may be opened, and the motor 8 may be operated to rotate the nozzle 9 in this state. In this case, the bath water 31 introduced into the filtration tank 7 via the filtration channel 27 is sprayed from the water discharge port 10 of the rotating nozzle 9 toward the filtration membrane 46, and the water flow causes the water to flow onto the surface of the filtration membrane 46. The attached dirt is stripped off, and the washed bathtub water 3 containing the dirt is removed.
1 passes the washing water outlet 7b through the washing water discharge passage 23 having a low hydraulic resistance without passing through the filtration membrane 46 having a high hydraulic resistance,
The water is mixed with the alkaline ionized water in the drain 18 to dilute the alkaline ionized water discharged out of the bathtub 1.
【0051】上記の浴槽水の水質改変装置では、電気分
解中においては、有隔膜電解槽2に浴槽水31が供給さ
れないため、有隔膜電解槽2に供給される浴槽水31の
量を低減して浴槽水31中に含まれる不純物やカルシウ
ムによる電極表面や隔膜45の汚染を抑制することがで
きる。In the apparatus for modifying the quality of bath water, the bath water 31 is not supplied to the electrolytic cell 2 during electrolysis, so that the amount of bath water 31 supplied to the electrolytic cell 2 is reduced. Thus, contamination of the electrode surface and the diaphragm 45 by impurities and calcium contained in the bathtub water 31 can be suppressed.
【0052】図12に本発明に係る浴槽水の水質改変装
置の更に他例を示す。この浴槽水の水質改変装置には、
図5と同様の循環ポンプ5、有隔膜電解槽2、塩水供給
槽濾過膜46及び濾過槽7が配設されている。FIG. 12 shows still another example of the bathtub water quality modifying apparatus according to the present invention. In this bathtub water quality modification device,
A circulation pump 5, a diaphragm electrolytic cell 2, a salt water supply tank filtration membrane 46 and a filtration tank 7 similar to those in FIG. 5 are provided.
【0053】また更に浴槽水の水流が通る流路、及びこ
れらの流路の流通を開閉する、電磁弁等からなる開閉弁
が配設されている。ここでいう浴槽水31には、浴槽水
31に塩化ナトリウムを溶解して得られる塩水、並びに
この塩水や浴槽水31を電気分解して得られる酸性イオ
ン水やアルカリ性イオン水が含まれる。Further, a flow path through which the bathtub water flows, and an on-off valve such as an electromagnetic valve for opening and closing the flow of these flow paths are provided. The bath water 31 referred to here includes salt water obtained by dissolving sodium chloride in the bath water 31, and acidic ion water and alkaline ion water obtained by electrolyzing the salt water and the bath water 31.
【0054】浴槽水31が通る流路のうち、流入路11
は下流側が浴槽1中の浴槽水31に配設されて、その下
流側の端部が流入口43として開口しており、上流側が
循環ポンプ5に接続されている。電解導入路12は上流
側が循環ポンプ5に接続され、下流側において塩水槽路
13と電解槽路30に分岐している。塩水槽路13の下
流側は塩水供給槽4の流入口4dに接続されている。電
解槽路30の下流側は第一電極室路14と第二電極室路
15に分岐され、第一電極室路14の下流側は有隔膜電
解槽2の第一電極室2aに、第二電極室路15の下流側
は有隔膜電解槽2の第二電極室2bにそれぞれ接続され
ている。第一電極室導出路22の上流側は有隔膜電解槽
2の第一電極室2aに接続され、下流側はイオン水路2
6の上流側に接続され、イオン水路26の下流側は流出
路16の上流側に接続されている。流出路16の下流側
は浴槽1内の浴槽水31に接続され、下流側の端部は流
出口44として開口されている。この流出路16にはヒ
ータ6が配設されており、ヒータ6が作動している場合
は流出路16を通る水流はヒータ6にて加熱される。ま
た塩供給路17は上流側が塩水供給槽4の流出口4eに
接続され、下流側は第二電極室路15の流路の途中に、
第二電極室路15と合流するように接続されている。第
二電極室導出路21の上流側は有隔膜電解槽2の第二電
極室2bに接続され、下流側は洗浄イオン路28の上流
側に接続されている。洗浄イオン路28の下流側は濾過
流路27の配管の途中に濾過流路27と合流するように
接続されている。洗浄水排出路23の上流側は濾過槽7
の洗浄水排出口7bに接続され、下流側は排水路18の
上流側に接続されている。浴槽水バイパス路29の上流
側は流入路11の配管の途中に、流入路11から分岐す
るように接続されており、下流側は排水路18の上流側
に、洗浄水排出路23と共に接続されている。排水路1
8の下流側は浴槽1外に導出されている。Of the flow path through which bath water 31 passes, inflow path 11
The downstream side is disposed in the bathtub water 31 in the bathtub 1, the downstream end thereof is opened as an inflow port 43, and the upstream side is connected to the circulation pump 5. The upstream side of the electrolysis introduction path 12 is connected to the circulation pump 5, and the downstream side is branched into a salt water tank path 13 and an electrolysis tank path 30. The downstream side of the salt water tank path 13 is connected to the inlet 4 d of the salt water supply tank 4. The downstream side of the electrolytic cell path 30 is branched into a first electrode chamber path 14 and a second electrode chamber path 15, and the downstream side of the first electrode chamber path 14 is connected to the first electrode chamber 2 a of the diaphragm electrolyzer 2. The downstream side of the electrode chamber path 15 is connected to the second electrode chamber 2 b of the diaphragm electrolyzer 2. The upstream side of the first electrode chamber lead-out passage 22 is connected to the first electrode chamber 2 a of the diaphragm electrolyzer 2, and the downstream side is the ion water passage 2.
6 and the downstream side of the ion water channel 26 is connected to the upstream side of the outflow channel 16. The downstream side of the outflow channel 16 is connected to bath water 31 in the bathtub 1, and the downstream end is opened as an outlet 44. The heater 6 is disposed in the outflow passage 16, and when the heater 6 is operating, the water flow passing through the outflow passage 16 is heated by the heater 6. Further, the upstream side of the salt supply path 17 is connected to the outlet 4 e of the salt water supply tank 4, and the downstream side is located in the middle of the flow path of the second electrode chamber path 15.
It is connected so as to merge with the second electrode chamber path 15. The upstream side of the second electrode chamber lead-out path 21 is connected to the second electrode chamber 2 b of the diaphragm electrolyzer 2, and the downstream side is connected to the upstream side of the cleaning ion path 28. The downstream side of the cleaning ion path 28 is connected to the filtration flow path 27 in the middle of the piping of the filtration flow path 27 so as to merge therewith. The filtration tank 7 is located upstream of the washing water discharge path 23.
The downstream side is connected to the upstream side of the drainage channel 18. The upstream side of the bathtub water bypass passage 29 is connected in the middle of the pipe of the inflow passage 11 so as to branch off from the inflow passage 11, and the downstream side is connected to the upstream side of the drainage passage 18 together with the washing water discharge passage 23. ing. Drainage 1
The downstream side of 8 is led out of the bathtub 1.
【0055】また開閉弁のうち、第1弁32は塩水槽路
13に、第2弁33は第二電極室路15の塩供給路17
との接続位置よりも上流側に、第5弁36はイオン水バ
イパス路24に、第7弁38は第一電極室路14に、第
8弁39は洗浄イオン路28に、第9弁40は濾過流路
27の洗浄イオン路28との接続位置よりも上流側に、
第10弁41は浴槽水バイパス路29に、第11弁42
は排水路18にそれぞれ設けられ、各流路の流通を、こ
の開閉弁の配設位置において開閉する。Among the on-off valves, the first valve 32 is connected to the salt water tank passage 13, and the second valve 33 is connected to the salt supply passage 17 of the second electrode chamber passage 15.
The fifth valve 36 is connected to the ion water bypass passage 24, the seventh valve 38 is connected to the first electrode chamber passage 14, the eighth valve 39 is connected to the cleaning ion passage 28, and the ninth valve 40 On the upstream side of the connection position of the filtration channel 27 with the washing ion channel 28,
The tenth valve 41 is connected to the bathtub water bypass passage 29 and the eleventh valve 42
Are respectively provided in the drainage passages 18 and open and close the flow of each flow passage at the position where the on-off valve is disposed.
【0056】ここでイオン水路26の下流側は、浴槽1
内に直接接続してもよい。Here, the downstream side of the ion channel 26 is the bathtub 1
You may connect directly inside.
【0057】この浴槽水の水質改変装置の動作を図13
〜21を示して説明する。ここでこれらの図面中で白抜
きで示されている開閉弁は開状態の弁を、黒く塗りつぶ
して示されている開閉弁は閉状態の弁をそれぞれ示し、
また流路中の矢印は各流路における浴槽水31の流れの
向きを示す。FIG. 13 shows the operation of the bath water quality modifying device.
21 will be described. Here, in these drawings, the open / closed valves shown in white represent open valves, and the open / closed valves shown in black represent closed valves, respectively.
Arrows in the flow paths indicate the direction of the flow of bathtub water 31 in each flow path.
【0058】浴槽水31を濾過槽7にて浄化する場合
は、図13に示すように、第9弁40が開状態、第1弁
32、第2弁33、第5弁36、第7弁38、第8弁3
9、第10弁41、第11弁42が閉状態となり、この
状態で循環ポンプ5が作動する。このとき循環ポンプ5
の働きにより浴槽水31は流入路11、濾過流路27、
濾過水路25、流出路16で構成される循環流路を循環
する。このとき濾過流路27から濾過槽7に供給される
浴槽水31は、ノズル9の吐水口10から濾過槽7の上
流側に供給され、更に濾過膜46を通過して濾過槽7の
下流側に導入されるものであり、濾過槽7にて入浴等に
より浴槽水31に混入した垢、埃、細菌等を濾過し、浴
槽水31が浄化されて清潔に保つことができるものであ
る。またこのとき流出路16を通過する浴槽水31の温
度が所定の設定温度よりも低い場合は、ヒータ6が作動
して浴槽水31が加熱される。When purifying the bathtub water 31 in the filtration tank 7, the ninth valve 40 is open, the first valve 32, the second valve 33, the fifth valve 36, the seventh valve as shown in FIG. 38, 8th valve 3
The ninth, tenth and eleventh valves 41 and 42 are closed, and the circulation pump 5 operates in this state. At this time, the circulation pump 5
By the action of the bathtub water 31, the inflow channel 11, the filtration channel 27,
It circulates through a circulation channel composed of the filtration water channel 25 and the outflow channel 16. At this time, the bath water 31 supplied from the filtration channel 27 to the filtration tank 7 is supplied from the water discharge port 10 of the nozzle 9 to the upstream side of the filtration tank 7, further passes through the filtration membrane 46, and is downstream of the filtration tank 7. The dirt, dust, bacteria, and the like mixed in the bathtub water 31 by bathing or the like in the filter tank 7 are filtered, and the bathtub water 31 is purified and can be kept clean. Further, at this time, when the temperature of the bathtub water 31 passing through the outflow passage 16 is lower than a predetermined set temperature, the heater 6 is operated to heat the bathtub water 31.
【0059】浴槽水31をアルカリ性に水質改変する場
合は、まず図14に示すように、第1弁32、第5弁3
6、第9弁40が開状態、第2弁33、第7弁38、第
8弁39、第10弁41、第11弁42が閉状態とな
り、この状態で循環ポンプ5が作動する。このとき循環
ポンプ5の働きにより浴槽水31は流入路11、電解導
入路12、塩水槽路13、塩供給路17、第二電極室路
15、第二電極室導出路21、イオン水バイパス路2
4、イオン水路26、流出路16にて構成される循環流
路と、流入路11、濾過流路27、濾過水路25、流出
路16で構成される循環流路の、二系統の循環流路を循
環する。流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路においては、図13の場
合と同様に、濾過槽7において浴槽水31の浄化が行わ
れる。また塩水供給槽4内の塩化ナトリウムが、塩水槽
路13から塩水供給槽4に供給された浴槽水31に溶解
して塩水が生成し、この塩水は塩供給路17、電解槽路
30を経由し、第一電極室路14から有隔膜電解槽2の
第一電極室2aに供給されると共に第二電極室路15か
ら有隔膜電解槽2の第二電極室2bに供給され、第一電
極室2a及び第二電極室2b中の余剰の塩水は第一電極
室導出路22、イオン水路26、流出路16を経由して
浴槽1に返送される。When the water quality of the bathtub water 31 is changed to alkaline, first, as shown in FIG.
6, the ninth valve 40 is open, the second valve 33, the seventh valve 38, the eighth valve 39, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied by the operation of the circulation pump 5 so that the bath water 31 flows into the inflow path 11, the electrolytic introduction path 12, the salt water tank path 13, the salt supply path 17, the second electrode chamber path 15, the second electrode chamber outlet path 21, the ionic water bypass path. 2
4. Two circulation flow paths: a circulation flow path composed of the ion water path 26 and the outflow path 16 and a circulation flow path composed of the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16. Circulate. In the circulation flow path including the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13 to generate salt water, and this salt water passes through the salt supply path 17 and the electrolytic tank path 30. Then, the first electrode chamber 2 is supplied to the first electrode chamber 2 a of the diaphragm electrolyzer 2 from the first electrode chamber path 14, and the second electrode chamber 15 is supplied to the second electrode chamber 2 b of the diaphragm electrolyzer 2. Excess salt water in the chamber 2a and the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber lead-out passage 22, the ion water passage 26, and the outflow passage 16.
【0060】次に図15に示すように、第1弁32、第
5弁36、第9弁40が開状態、第2弁33、第7弁3
8、第8弁39、第10弁41、第11弁42が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路は維持されて、濾過槽7
において浴槽水31の浄化が引き続き行われる。この状
態で白金−イリジウム混合電極3aが陰極、白金電極3
bが陽極となるように、この電極間に電圧が印可され、
有隔膜電解槽2において電気分解により第一電極室2a
にアルカリ性イオン水が、第二電極室2bに酸性イオン
水が生成する。このように生成されたイオン水は有隔膜
電解槽2内に保持される。Next, as shown in FIG. 15, the first valve 32, the fifth valve 36, and the ninth valve 40 are open, and the second valve 33, the seventh valve 3
The eighth, eighth, and thirty-ninth valve 41, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 continues to operate in this state.
At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained, and the filtration tank 7 is maintained.
The purifying of the bathtub water 31 is continuously performed. In this state, the platinum-iridium mixed electrode 3a serves as a cathode and the platinum electrode 3
A voltage is applied between the electrodes so that b becomes an anode,
The first electrode chamber 2a is formed by electrolysis in the diaphragm electrolytic cell 2.
And alkaline ionized water is generated in the second electrode chamber 2b. The ion water thus generated is held in the diaphragm electrolyzer 2.
【0061】次に電気分解の終了後、図16に示すよう
に、第7弁38、第9弁40、第11弁42が開状態、
第1弁32、第2弁33、第5弁36、第8弁39、第
10弁41が閉状態となり、この状態で引き続き循環ポ
ンプ5が作動する。このとき流入路11、電解導入路1
2、電解槽路30を経由して、第一電極室路14から第
一電極室2a内に浴槽水31が導入される水流が発生す
る。第一電極室2a内のアルカリ性イオン水は、浴槽水
31に押し出されて第一電極室導出路22、イオン水路
26、流出路16を経由して流出口44から浴槽1内に
供給されて、浴槽1内の浴槽水31をアルカリ性に水質
改変する。一方、濾過流路27を経由して濾過槽7に導
入される浴槽水31は、水圧抵抗の高い濾過膜46を透
過せずに洗浄水排出口7bを通じて水圧抵抗の低い洗浄
水排出路23を通過し、排水路18を通って浴槽1外に
排出される。Next, after the electrolysis is completed, the seventh valve 38, the ninth valve 40, and the eleventh valve 42 are opened as shown in FIG.
The first valve 32, the second valve 33, the fifth valve 36, the eighth valve 39, and the tenth valve 41 are closed, and the circulation pump 5 continues to operate in this state. At this time, the inflow path 11 and the electrolysis introduction path 1
2. A water flow in which the bath water 31 is introduced into the first electrode chamber 2a from the first electrode chamber path 14 via the electrolytic cell path 30 is generated. The alkaline ionized water in the first electrode chamber 2a is pushed out into the bathtub water 31 and is supplied into the bathtub 1 from the outlet 44 through the first electrode chamber lead-out passage 22, the ion water passage 26, and the outflow passage 16, The water quality of the bathtub water 31 in the bathtub 1 is changed to alkaline. On the other hand, the bath water 31 introduced into the filtration tank 7 via the filtration channel 27 does not pass through the filtration membrane 46 having a high hydraulic resistance and flows through the cleaning water discharge path 23 having a low hydraulic resistance through the cleaning water discharge port 7b. The water passes through the drainage channel 18 and is discharged out of the bathtub 1.
【0062】次に図17に示すように、第7弁38、第
8弁39、第11弁42が開状態、第1弁32、第2弁
33、第5弁36、第9弁40、第10弁41が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、電解導入路12、電解槽路30を
経由して、第一電極室路14から第一電極室2a内に、
第二電極室路15から第二電極室2b内に浴槽水31が
導入される水流が発生する。第一電極室2a内のアルカ
リ性イオン水は、図16の場合と同様に、引き続き浴槽
水31に押し出されて第一電極室導出路22、イオン水
路26、流出路16を経由して流出口44から浴槽1内
に供給されて、浴槽1内の浴槽水31をアルカリ性に水
質改変する。また第二電極室2b内の酸性イオン水は、
第二電極室導出路21、洗浄イオン路28、濾過流路2
7を経由して濾過槽7に導入される。酸性イオン水は濾
過槽7に貯められ、濾過槽7内の余剰の酸性イオン水
は、水圧抵抗の低い洗浄水排出路23を通過し、排水路
18を通って浴槽1外に排出される。ここで、図16に
示す動作を行わずに、図15に示す動作から直接図17
に示す動作に移行することにより、有隔膜電解槽2から
のアルカリ性イオン水と酸性イオン水の排出を同時に開
始しても良い。Next, as shown in FIG. 17, the seventh valve 38, the eighth valve 39, and the eleventh valve 42 are open, and the first valve 32, the second valve 33, the fifth valve 36, the ninth valve 40, The tenth valve 41 is closed, and the circulation pump 5 continues to operate in this state.
At this time, via the inflow path 11, the electrolysis introduction path 12, and the electrolytic cell path 30, the first electrode chamber path 14 into the first electrode chamber 2a,
A water flow for introducing the bath water 31 from the second electrode chamber passage 15 into the second electrode chamber 2b is generated. The alkaline ionized water in the first electrode chamber 2a is continuously pushed out by the bath water 31 similarly to the case of FIG. 16, and is discharged through the first electrode chamber outlet passage 22, the ion water passage 26, the outflow passage 16 and the outlet 44. Is supplied into the bathtub 1 to change the water quality of the bathtub water 31 in the bathtub 1 to alkaline. The acidic ion water in the second electrode chamber 2b is
Second electrode chamber lead-out passage 21, cleaning ion passage 28, filtration passage 2
It is introduced into the filtration tank 7 via. The acidic ionized water is stored in the filtration tank 7, and excess acid ionized water in the filtration tank 7 passes through the washing water discharge passage 23 having a low hydraulic resistance, and is discharged to the outside of the bathtub 1 through the drainage passage 18. Here, instead of performing the operation shown in FIG. 16, the operation shown in FIG.
The discharge to alkaline ionized water and acidic ionized water from the diaphragm electrolyzer 2 may be started at the same time by shifting to the operation shown in FIG.
【0063】次に図18に示すように、第9弁40、第
10弁41が開状態、第1弁32、第2弁33、第5弁
36、第7弁38、第8弁39、第11弁42が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
この状態でモータ8を作動させてノズル9を回転させ
る。このとき浴槽水バイパス路29、濾過流路27、洗
浄水排出路23からなる閉じた循環流路が形成され、濾
過槽7に貯められていた酸性イオン水がこの閉じた循環
流路を循環する。この閉じた循環流路を循環する酸性イ
オン水は、濾過流路27を経由して濾過槽7に導入さ
れ、回転するノズル9の吐水口10から濾過膜46に向
けて吹き付けられ、この水流により濾過膜46の表面に
付着した汚物がはぎ取られる。この汚物を含む洗浄後の
浴槽水31は、水圧抵抗の高い濾過膜46を透過せずに
洗浄水排出口7bを水圧抵抗の低い洗浄水排出路23を
通過し、浴槽水バイパス路29を経由して再び濾過流路
27から濾過槽7に導入される。またこのとき酸性イオ
ン水中の塩素にて濾過膜46に付着した有機物を分解除
去すると共に、濾過膜46を酸性下におくことで濾過膜
46に付着している金属塩が溶解する。Next, as shown in FIG. 18, the ninth valve 40 and the tenth valve 41 are open, the first valve 32, the second valve 33, the fifth valve 36, the seventh valve 38, the eighth valve 39, The eleventh valve 42 is closed, and the circulation pump 5 is continuously operated in this state.
In this state, the motor 8 is operated to rotate the nozzle 9. At this time, a closed circulation flow path composed of the bathtub water bypass path 29, the filtration flow path 27, and the washing water discharge path 23 is formed, and the acidic ion water stored in the filtration tank 7 circulates through the closed circulation flow path. . The acidic ionized water circulating through the closed circulation flow path is introduced into the filtration tank 7 via the filtration flow path 27, and is sprayed from the water discharge port 10 of the rotating nozzle 9 toward the filtration membrane 46. Dirt adhering to the surface of the filtration membrane 46 is removed. The washed bathtub water 31 containing the dirt passes through the washing water outlet 7b through the washing water discharge passage 23 having a low hydraulic resistance without passing through the filtration membrane 46 having a high hydraulic resistance, and passes through the bathtub water bypass passage 29. Then, it is again introduced into the filtration tank 7 from the filtration channel 27. At this time, the organic substances attached to the filtration membrane 46 are decomposed and removed by chlorine in the acidic ionic water, and the metal salts attached to the filtration membrane 46 are dissolved by keeping the filtration membrane 46 under acidity.
【0064】次に図19に示すように、第9弁40、第
11弁42が開状態、第1弁32、第2弁33、第5弁
36、第7弁38、第8弁39、第10弁41が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき、流入路11、濾過流路27、洗浄水排出路2
3、排水路18からなる流路が形成され、流出口44か
ら導入される浴槽水31が、閉じた循環流路を循環して
いた、汚物を含む酸性イオン水を押し出して、排水路1
8を経由して浴槽1外に排出し、更にこの流路をすすい
で洗浄する。その後、図13に示す通常の循環状態に復
帰する。Next, as shown in FIG. 19, the ninth valve 40 and the eleventh valve 42 are open, the first valve 32, the second valve 33, the fifth valve 36, the seventh valve 38, the eighth valve 39, The tenth valve 41 is closed, and the circulation pump 5 continues to operate in this state.
At this time, the inflow channel 11, the filtration channel 27, the washing water discharge channel 2
3. A flow path composed of the drainage channel 18 is formed, and the bath water 31 introduced from the outlet 44 pushes out acidic ionized water containing dirt that has been circulating in the closed circulation channel, and the drainage channel 1
The water is discharged out of the bathtub 1 via 8, and the flow path is further rinsed for cleaning. Then, it returns to the normal circulation state shown in FIG.
【0065】また浴槽水31を殺菌する場合は、まず図
14に示すように、第1弁32、第5弁36、第9弁4
0が開状態、第2弁33、第7弁38、第8弁39、第
10弁41、第11弁42が閉状態となり、この状態で
循環ポンプ5が作動する。このとき循環ポンプ5の働き
により浴槽水31は流入路11、電解導入路12、塩水
槽路13、塩供給路17、第二電極室路15、第二電極
室導出路21、イオン水バイパス路24、イオン水路2
6、流出路16にて構成される循環流路と、流入路1
1、濾過流路27、濾過水路25、流出路16で構成さ
れる循環流路の、二系統の循環流路を循環する。流入路
11、濾過流路27、濾過水路25、流出路16で構成
される循環流路においては、図13の場合と同様に、濾
過槽7において浴槽水31の浄化が行われる。また塩水
供給槽4内の塩化ナトリウムが、塩水槽路13から塩水
供給槽4に供給された浴槽水31に溶解して塩水が生成
し、この塩水は塩供給路17、電解槽路30を経由し、
第一電極室路14から有隔膜電解槽2の第一電極室2a
に供給されると共に第二電極室路15から有隔膜電解槽
2の第二電極室2bに供給され、第一電極室2a及び第
二電極室2b中の余剰の塩水は第一電極室導出路22、
イオン水路26、流出路16を経由して浴槽1に返送さ
れる。When the bathtub water 31 is to be sterilized, first, as shown in FIG. 14, the first valve 32, the fifth valve 36, the ninth valve 4
0 is in an open state, the second valve 33, the seventh valve 38, the eighth valve 39, the tenth valve 41, and the eleventh valve 42 are in a closed state, and the circulating pump 5 operates in this state. At this time, the bath water 31 is supplied by the operation of the circulation pump 5 so that the bath water 31 flows into the inflow path 11, the electrolytic introduction path 12, the salt water tank path 13, the salt supply path 17, the second electrode chamber path 15, the second electrode chamber outlet path 21, and the ionic water bypass path. 24, Ion waterway 2
6. Circulation flow path composed of outflow path 16 and inflow path 1
1. Circulation is performed in two circulation passages of a circulation passage composed of a filtration passage 27, a filtration water passage 25, and an outflow passage 16. In the circulation flow path including the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13 to generate salt water, and this salt water passes through the salt supply path 17 and the electrolytic tank path 30. And
From the first electrode chamber path 14 to the first electrode chamber 2a of the diaphragm electrolyzer 2
And the excess salt water in the first electrode chamber 2a and the second electrode chamber 2b is supplied from the second electrode chamber path 15 to the second electrode chamber 2b of the diaphragm electrolyzer 2. 22,
The water is returned to the bathtub 1 via the ion water channel 26 and the outflow channel 16.
【0066】次に図15に示すように、第1弁32、第
5弁36、第9弁40が開状態、第2弁33、第7弁3
8、第8弁39、第10弁41、第11弁42が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路は維持されて、濾過槽7
において浴槽水31の浄化が引き続き行われる。この状
態で白金−イリジウム混合電極3aが陽極、白金電極3
bが陰極となるように、この電極間に電圧が印可され、
有隔膜電解槽2において電気分解により第一電極室2a
に酸性イオン水が、第二電極室2bにアルカリ性イオン
水が生成する。ここで第一電極室2aに設けられた白金
−イリジウム混合電極3aは塩素の発生効率が高いた
め、この酸性イオン水中では塩素が効率よく発生され
る。このように生成されたイオン水は有隔膜電解槽2内
に保持される。Next, as shown in FIG. 15, the first valve 32, the fifth valve 36, the ninth valve 40 are open, the second valve 33, the seventh valve 3
The eighth, eighth, and thirty-ninth valve 41, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 continues to operate in this state.
At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained, and the filtration tank 7 is maintained.
The purifying of the bathtub water 31 is continuously performed. In this state, the platinum-iridium mixed electrode 3a serves as the anode and the platinum electrode 3
A voltage is applied between the electrodes so that b becomes a cathode,
The first electrode chamber 2a is formed by electrolysis in the diaphragm electrolytic cell 2.
Acidic ion water is generated, and alkaline ion water is generated in the second electrode chamber 2b. Here, since the platinum-iridium mixed electrode 3a provided in the first electrode chamber 2a has a high chlorine generation efficiency, chlorine is generated efficiently in the acidic ionized water. The ion water thus generated is held in the diaphragm electrolyzer 2.
【0067】次に電気分解の終了後、図20に示すよう
に、第2弁33、第7弁38、第1弁32、第5弁3
6、第9弁40が開状態、第8弁39、第10弁41、
第11弁42が閉状態となり、この状態で引き続き循環
ポンプ5が作動する。このとき流入路11、濾過流路2
7、濾過水路25、流出路16で構成される循環流路は
維持されて、濾過槽7において浴槽水31の浄化が引き
続き行われる。またこのとき流入路11、電解導入路1
2、電解槽路30を経由して、第一電極室路14から第
一電極室2a内に、第二電極室路15から第二電極室2
b内に浴槽水31が導入される水流が発生する。第一電
極室2a内の酸性イオン水は浴槽水31に押し出されて
第一電極室導出路22を経由してイオン水路26に至
り、また第二電極室2b内のアルカリ性イオン水は、第
二電極室導出路21、イオン水バイパス路24を経由し
てやはりイオン水路26に至るものであり、イオン水路
26においてアルカリ性イオン水と酸性イオン水とが混
合される。この混合水は中性又は弱アルカリ性のイオン
水であり、また酸性イオン水が高濃度で塩素を含んでい
たため、高い塩素濃度を有している。この混合水は、流
出路16において、濾過槽7において浄化された後の浴
槽水31と混合し、流出路16を通って流出口44から
浴槽1内に供給され、混合水中の塩素にて浴槽1内の浴
槽水31が殺菌される。この場合、浴槽水31の浄化と
浴槽水31の殺菌とが同時に行われる。Next, after the completion of the electrolysis, as shown in FIG. 20, the second valve 33, the seventh valve 38, the first valve 32, the fifth valve 3
6, the ninth valve 40 is open, the eighth valve 39, the tenth valve 41,
The eleventh valve 42 is closed, and the circulation pump 5 is continuously operated in this state. At this time, the inflow channel 11 and the filtration channel 2
The circulation flow path composed of the filtration water channel 25 and the outflow channel 16 is maintained, and the purification of the bath water 31 is continued in the filtration tank 7. At this time, the inflow path 11 and the electrolysis introduction path 1
2. Via the electrolytic cell channel 30, the first electrode channel 14 enters the first electrode chamber 2a, and the second electrode chamber channel 15 enters the second electrode chamber 2a.
A water flow into which the bathtub water 31 is introduced is generated in b. The acidic ionic water in the first electrode chamber 2a is pushed out by the bathtub water 31 and reaches the ion water channel 26 via the first electrode chamber lead-out passage 22, and the alkaline ionic water in the second electrode chamber 2b is It again reaches the ion water channel 26 via the electrode chamber lead-out channel 21 and the ion water bypass channel 24, and the alkaline ion water and the acidic ion water are mixed in the ion water channel 26. This mixed water is neutral or weakly alkaline ionized water, and has a high chlorine concentration because the acidic ionized water contains chlorine at a high concentration. This mixed water is mixed with the bath water 31 after being purified in the filtration tank 7 in the outflow passage 16, supplied into the bath tub 1 through the outflow passage 16 through the outflow passage 16, and mixed with chlorine in the mixed water. Bath water 31 in 1 is sterilized. In this case, purification of bath water 31 and sterilization of bath water 31 are performed simultaneously.
【0068】上記の浴槽水31をアルカリ性に水質改変
しながら濾過膜46を洗浄する動作と、浴槽水31を殺
菌する動作は、一回ずつ交互に、あるいはどちらか一方
の動作が複数回繰り返して行われると共に他方の動作が
一回行われるものであり、この場合、浴槽水31をアル
カリ性に保ちながら、殺菌された衛生的な状態に保つこ
とができ、しかも濾過膜46が洗浄されて濾過膜46の
膜流量が保たれ、高い効率で濾過槽7による浴槽水31
の浄化が行われるものである。The operation of washing the filter membrane 46 while altering the water quality of the bathtub water 31 to alkaline and the operation of sterilizing the bathtub water 31 are alternately performed one time at a time, or one of the operations is repeated a plurality of times. The operation is performed once while the other operation is performed once. In this case, the bathtub water 31 can be maintained in an alkaline state, and can be maintained in a sterilized and sanitary state. The bath flow rate 31 is maintained at a high efficiency with the membrane flow rate of 46 maintained.
Purification is performed.
【0069】また浴槽水31を酸性に水質改変する場
合、まず図14に示すように、第1弁32、第5弁3
6、第9弁40が開状態、第2弁33、第7弁38、第
8弁39、第10弁41、第11弁42が閉状態とな
り、この状態で循環ポンプ5が作動する。このとき循環
ポンプ5の働きにより浴槽水31は流入路11、電解導
入路12、塩水槽路13、塩供給路17、第二電極室路
15、第二電極室導出路21、イオン水バイパス路2
4、イオン水路26、流出路16にて構成される循環流
路と、流入路11、濾過流路27、濾過水路25、流出
路16で構成される循環流路の、二系統の循環流路を循
環する。流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路においては、図13の場
合と同様に、濾過槽7において浴槽水31の浄化が行わ
れる。また塩水供給槽4内の塩化ナトリウムが、塩水槽
路13から塩水供給槽4に供給された浴槽水31に溶解
して塩水が生成し、この塩水は塩供給路17、電解槽路
30を経由し、第一電極室路14から有隔膜電解槽2の
第一電極室2aに供給されると共に第二電極室路15か
ら有隔膜電解槽2の第二電極室2bに供給され、第一電
極室2a及び第二電極室2b中の余剰の塩水は第一電極
室導出路22、イオン水路26、流出路16を経由して
浴槽1に返送される。When the bath tub water 31 is modified to have an acidic water quality, first, as shown in FIG.
6, the ninth valve 40 is open, the second valve 33, the seventh valve 38, the eighth valve 39, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied by the operation of the circulation pump 5 so that the bath water 31 flows into the inflow path 11, the electrolytic introduction path 12, the salt water tank path 13, the salt supply path 17, the second electrode chamber path 15, the second electrode chamber outlet path 21, the ionic water bypass path. 2
4. Two circulation flow paths: a circulation flow path composed of the ion water path 26 and the outflow path 16 and a circulation flow path composed of the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16. Circulate. In the circulation flow path including the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13 to generate salt water, and this salt water passes through the salt supply path 17 and the electrolytic tank path 30. Then, the first electrode chamber 2 is supplied to the first electrode chamber 2 a of the diaphragm electrolyzer 2 from the first electrode chamber path 14, and the second electrode chamber 15 is supplied to the second electrode chamber 2 b of the diaphragm electrolyzer 2. Excess salt water in the chamber 2a and the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber lead-out passage 22, the ion water passage 26, and the outflow passage 16.
【0070】次に図15に示すように、第1弁32、第
5弁36、第9弁40が開状態、第2弁33、第7弁3
8、第8弁39、第10弁41、第11弁42が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路は維持されて、濾過槽7
において浴槽水31の浄化が引き続き行われる。この状
態で白金−イリジウム混合電極3aが陽極、白金電極3
bが陰極となるように、この電極間に電圧が印可され、
有隔膜電解槽2において電気分解により第一電極室2a
にアルカリ性イオン水が、第二電極室2bに酸性イオン
水が生成する。ここで第一電極室2aに設けられた白金
−イリジウム混合電極3aは塩素の発生効率が高いた
め、この酸性イオン水中では塩素が効率よく発生され
る。このように生成されたイオン水は有隔膜電解槽2内
に保持される。Next, as shown in FIG. 15, the first valve 32, the fifth valve 36, and the ninth valve 40 are open, the second valve 33, the seventh valve 3
The eighth, eighth, and thirty-ninth valve 41, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 continues to operate in this state.
At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained, and the filtration tank 7 is maintained.
The purifying of the bathtub water 31 is continuously performed. In this state, the platinum-iridium mixed electrode 3a serves as the anode and the platinum electrode 3
A voltage is applied between the electrodes so that b becomes a cathode,
The first electrode chamber 2a is formed by electrolysis in the diaphragm electrolytic cell 2.
And alkaline ionized water is generated in the second electrode chamber 2b. Here, since the platinum-iridium mixed electrode 3a provided in the first electrode chamber 2a has a high chlorine generation efficiency, chlorine is generated efficiently in the acidic ionized water. The ion water thus generated is held in the diaphragm electrolyzer 2.
【0071】次に電気分解の終了後、図16に示すよう
に、第7弁38、第9弁40、第11弁42が開状態、
第1弁32、第2弁33、第5弁36、第8弁39、第
10弁41が閉状態となり、この状態で引き続き循環ポ
ンプ5が作動する。このとき流入路11、電解導入路1
2、電解槽路30を経由して、第一電極室路14から第
一電極室2a内に浴槽水31が導入される水流が発生す
る。第一電極室2a内の酸性イオン水は、浴槽水31に
押し出されて第一電極室導出路22、イオン水路26、
流出路16を経由して流出口44から浴槽1内に供給さ
れて、浴槽1内の浴槽水31を酸性に水質改変する。一
方、濾過流路27を経由して濾過槽7に導入される浴槽
水31は、水圧抵抗の高い濾過膜46を透過せずに洗浄
水排出口7bを水圧抵抗の低い洗浄水排出路23を通過
し、排水路18を通って浴槽1外に排出される。Next, after the electrolysis is completed, the seventh valve 38, the ninth valve 40, and the eleventh valve 42 are opened as shown in FIG.
The first valve 32, the second valve 33, the fifth valve 36, the eighth valve 39, and the tenth valve 41 are closed, and the circulation pump 5 continues to operate in this state. At this time, the inflow path 11 and the electrolysis introduction path 1
2. A water flow in which the bath water 31 is introduced into the first electrode chamber 2a from the first electrode chamber path 14 via the electrolytic cell path 30 is generated. The acidic ionic water in the first electrode chamber 2a is pushed out by the bathtub water 31, and the first electrode chamber outlet passage 22, the ion water passage 26,
The water is supplied into the bathtub 1 from the outlet 44 via the outflow passage 16, and the water quality of the bathtub water 31 in the bathtub 1 is acidified. On the other hand, the bath water 31 introduced into the filtration tank 7 via the filtration flow path 27 does not pass through the filtration membrane 46 having high hydraulic resistance, and flows through the cleaning water discharge port 7b through the cleaning water discharge path 23 having low hydraulic resistance. The water passes through the drainage channel 18 and is discharged out of the bathtub 1.
【0072】次に図17に示すように、第7弁38、第
8弁39、第11弁42が開状態、第1弁32、第2弁
33、第5弁36、第9弁40、第10弁41が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、電解導入路12、電解槽路30を
経由して、第一電極室路14から第一電極室2a内に、
第二電極室路15から第二電極室2b内に浴槽水31が
導入される水流が発生する。第一電極室2a内の酸性イ
オン水は、図16の場合と同様に、引き続き浴槽水31
に押し出されて第一電極室導出路22、イオン水路2
6、流出路16を経由して流出口44から浴槽1内に供
給されて、浴槽1内の浴槽水31を酸性に水質改変す
る。また第二電極室2b内のアルカリ性イオン水は、第
二電極室導出路21、洗浄イオン路28、濾過流路27
を経由して濾過槽7に導入される。濾過槽7内のアルカ
リ性イオン水は水圧抵抗の低い洗浄水排出路23を通過
し、排水路18を通って浴槽1外に排出される。ここ
で、図16に示す動作を行わずに、図15に示す動作か
ら直接図17に示す動作に移行することにより、有隔膜
電解槽2からのアルカリ性イオン水と酸性イオン水の排
出を同時に開始しても良い。Next, as shown in FIG. 17, the seventh valve 38, the eighth valve 39, and the eleventh valve 42 are open, and the first valve 32, the second valve 33, the fifth valve 36, the ninth valve 40, The tenth valve 41 is closed, and the circulation pump 5 continues to operate in this state.
At this time, via the inflow path 11, the electrolysis introduction path 12, and the electrolytic cell path 30, the first electrode chamber path 14 into the first electrode chamber 2a,
A water flow for introducing the bath water 31 from the second electrode chamber passage 15 into the second electrode chamber 2b is generated. The acidic ionic water in the first electrode chamber 2a continues to be supplied to the bath water 31 as in the case of FIG.
To the first electrode chamber outlet passage 22 and the ion water passage 2
6. The water is supplied into the bathtub 1 from the outlet 44 via the outflow passage 16, and the water quality of the bathtub water 31 in the bathtub 1 is changed to acidic. Further, the alkaline ionized water in the second electrode chamber 2b is supplied to the second electrode chamber outlet path 21, the cleaning ion path 28, the filtration path 27.
Through the filter tank 7. The alkaline ionized water in the filtration tank 7 passes through the washing water discharge passage 23 having a low hydraulic resistance, and is discharged out of the bathtub 1 through the drainage passage 18. Here, the operation shown in FIG. 15 is directly shifted to the operation shown in FIG. 17 without performing the operation shown in FIG. 16, so that the discharge of the alkaline ionized water and the acidic ionized water from the diaphragm electrolyzer 2 is started simultaneously. You may.
【0073】上記の浴槽水の水質改変装置では、電気分
解中においては、有隔膜電解槽2に浴槽水31が供給さ
れないため、有隔膜電解槽2に供給される浴槽水31の
量を低減して浴槽水31中に含まれる不純物やカルシウ
ムによる電極表面や隔膜45の汚染を抑制することがで
きる。In the apparatus for modifying water quality of bath water, the bath water 31 is not supplied to the electrolytic cell 2 during electrolysis. Thus, contamination of the electrode surface and the diaphragm 45 by impurities and calcium contained in the bathtub water 31 can be suppressed.
【0074】[0074]
【発明の効果】本発明の請求項1に係る浴槽水の水質改
変装置は、有隔膜電解槽と、有隔膜電解槽内の隔膜にて
隔てられた一方の電解室内に塩化ナトリウムを供給する
塩水供給槽と、電気分解に供される浴槽水を浴槽から有
隔膜電解槽に供給し、有隔膜電解槽にて電気分解により
生成するアルカリ性イオン水と酸性イオン水のうち一方
のイオン水を浴槽に供給すると共に他方のイオン水を浴
槽外に排出する浴槽水の流路と、この浴槽水の流路に水
流を発生させる循環ポンプとを具備するものであり、有
隔膜電解槽内の浴槽水に塩化ナトリウムを添加して導電
性を向上し、電気分解に必要な電力を低減することがで
き、また有隔膜電解槽内の浴槽水中の塩化物イオン及び
ナトリウムイオンの濃度が向上されて、電気分解により
陰極側で水酸化ナトリウム濃度の高いアルカリ性イオン
水を生成すると共に、陽極側で塩酸濃度の高い酸性イオ
ン水を生成することができ、このようなイオン水を浴槽
水のpHの改変に利用することができるものである。According to a first aspect of the present invention, there is provided an apparatus for modifying water quality of bath tub water, wherein the salt water supplies sodium chloride into a diaphragm electrolytic cell and one of the electrolytic chambers separated by a diaphragm in the diaphragm electrolytic cell. A supply tank and a bathtub water to be supplied to the electrolysis are supplied from the bathtub to the diaphragm electrolyzer, and one of the alkaline ionic water and the acidic ionic water generated by the electrolysis in the diaphragm electrolyzer is supplied to the bathtub. A bathtub water flow path for supplying and discharging the other ion water out of the bathtub, and a circulation pump for generating a water flow in the bathtub water flow path are provided. The conductivity can be improved by adding sodium chloride, the power required for electrolysis can be reduced, and the concentration of chloride ions and sodium ions in the bath water in the diaphragm electrolyzer is improved, resulting in electrolysis. The hydroxide on the cathode side In addition to generating alkaline ionized water having a high concentration of lithium, acidic ionized water having a high concentration of hydrochloric acid can be generated on the anode side, and such ionized water can be used for modifying the pH of bath water. .
【0075】また本発明の請求項2に係る浴槽水の水質
改変装置は、請求項1の構成に加えて、有隔膜電解槽に
おける電気分解の進行中に、有隔膜電解槽にて電気分解
により生成するアルカリ性イオン水と酸性イオン水のう
ち一方のイオン水を連続的に浴槽に供給し、有隔膜電解
槽における電気分解の終了後に他方のイオン水を浴槽外
に排出する浴槽水の流路を具備するものであり、イオン
水を浴槽外に排出する際の排水量を低減して、浴槽内の
浴槽水の急激な減少を抑制することができるものであ
る。The bath water quality modifying apparatus according to claim 2 of the present invention, in addition to the constitution of claim 1, further comprises an electrolysis in the diaphragm electrolyzer during electrolysis in the diaphragm electrolyzer. One of the generated alkaline ionized water and acidic ionized water is continuously supplied to the bath, and after the completion of the electrolysis in the diaphragm electrolyzer, the other is discharged out of the bath. The present invention can reduce the amount of drainage when discharging ionized water out of the bathtub, thereby suppressing a rapid decrease in bathtub water in the bathtub.
【0076】また本発明の請求項3に係る浴槽水の水質
改変装置は、有隔膜電解槽と、有隔膜電解槽内の隔膜に
て隔てられた両方の電解室内に塩化ナトリウムを供給す
る塩水供給槽と、電気分解に供される浴槽水を浴槽から
有隔膜電解槽に供給し、有隔膜電解槽における電気分解
終了後に、有隔膜電解槽にて電気分解により生成するア
ルカリ性イオン水と酸性イオン水のうちの一方のイオン
水を浴槽に供給すると共に他方のイオン水を浴槽外に排
出する浴槽水の流路と、この浴槽水の流路に水流を発生
させる循環ポンプとを具備するものであり、有隔膜電解
槽内の浴槽水に塩化ナトリウムを添加して導電性を向上
し、電気分解に必要な電力を低減することができ、また
有隔膜電解槽内の浴槽水中の塩化物イオン及びナトリウ
ムイオンの濃度が向上されて、電気分解により陰極側で
水酸化ナトリウム濃度の高いアルカリ性イオン水を生成
すると共に、陽極側で塩酸濃度の高い酸性イオン水を生
成することができ、このようなイオン水を浴槽水のpH
の改変に利用することができるものであり、またイオン
水を浴槽外に排出する際の排水量を低減して、浴槽内の
浴槽水の急激な減少を抑制することができるものであ
り、また有隔膜電解槽に供給される浴槽水の量を低減し
て浴槽水中に含まれる不純物やカルシウムによる電極表
面や隔膜の汚染を抑制することができるものである。The bath water quality modifying apparatus according to claim 3 of the present invention is a salt water supply apparatus for supplying sodium chloride to a diaphragm electrolyzer and both electrolysis chambers separated by a diaphragm in the diaphragm electrolyzer. A tank and a bath water to be subjected to electrolysis are supplied from the bath to the diaphragm electrolyzer, and after the electrolysis in the diaphragm electrolyzer is completed, alkaline ionized water and acidic ionic water generated by electrolysis in the diaphragm electrolyzer are supplied. A tub water flow path for supplying one of the ion water to the bath tub and discharging the other ion water out of the bath tub, and a circulation pump for generating a water flow in the bath tub water flow path. Sodium chloride can be added to the bath water in a diaphragm electrolyzer to improve conductivity, reduce the power required for electrolysis, and reduce chloride ions and sodium in the bath water in the diaphragm electrolyzer. Ion concentration It is possible to generate alkaline ionized water having a high concentration of sodium hydroxide on the cathode side by electrolysis and to generate acidic ionized water having a high concentration of hydrochloric acid on the anode side by electrolysis. pH
It can also be used for modification of water, and can reduce the amount of effluent when discharging ionized water out of the bathtub, thereby suppressing the rapid decrease of bathtub water in the bathtub. The present invention can reduce the amount of bath water supplied to the diaphragm electrolyzer to suppress contamination of the electrode surface and the diaphragm due to impurities and calcium contained in the bath water.
【0077】また本発明の請求項4に係る浴槽水の水質
改変装置は、請求項1乃至3のいずれかの構成に加え
て、有隔膜電解槽にて電気分解により生成するアルカリ
性イオン水と酸性イオン水のうちのアルカリ性イオン水
を浴槽に供給すると共に酸性イオン水を浴槽外に排出す
る動作と、電気分解により生成するアルカリ性イオン水
と酸性イオン水の両方を浴槽に供給する動作とを一回ず
つ交互に行うか、あるいは一方の動作を複数回行うのに
対して他方の動作を一回行うものであり、浴槽にアルカ
リ性イオン水を供給することにより浴槽中の浴槽水をア
ルカリ性に水質改変すると共に、アルカリ性イオン水と
酸性イオン水が混合された中性又は弱アルカリ性で塩素
濃度の高い混合水を浴槽に供給することにより浴槽中の
浴槽水をアルカリ性に保ったまま塩素にて浴槽水を殺菌
することができるものである。The water quality modifying apparatus for bathtub water according to claim 4 of the present invention, in addition to the constitution according to any one of claims 1 to 3, further comprises an alkaline ionized water generated by electrolysis in a diaphragm electrolyzer and an acidic water. The operation of supplying the alkaline ionized water of the ionized water to the bathtub and discharging the acidic ionized water out of the bathtub, and the operation of supplying both the alkaline ionized water and the acidic ionized water generated by electrolysis to the bathtub once. Alternately, or one operation is performed a plurality of times, while the other operation is performed once, and the water quality of the bathtub in the bathtub is changed to alkaline by supplying alkaline ionized water to the bathtub. In addition, the bath water in the bath tub is made alkaline by supplying neutral or weakly alkaline mixed water having a high chlorine concentration, in which alkaline ion water and acidic ion water are mixed, to the bath tub. One in which it is possible to sterilize the bath water by keeping the as chlorine.
【0078】また本発明の請求項5に係る浴槽水の水質
改変装置、請求項1乃至4のいずれかの構成に加えて、
表面が白金−イリジウム混合物にて形成された白金−イ
リジウム混合物電極を有する第一電解室及び表面が白金
にて形成された白金電極を有する第二電解室が設けられ
た有隔膜電解槽と、白金−イリジウム混合物電極を陰
極、白金電極を陽極として電気分解を行ったときに有隔
膜電解槽にて生成されるアルカリ性イオン水を浴槽に供
給すると共に酸性イオン水を浴槽外に排出し、白金電極
を陰極、白金−イリジウム混合物電極を陽極として電気
分解を行ったときに有隔膜電解槽にて生成されるアルカ
リ性イオン水と酸性イオン水の両方を浴槽に供給する浴
槽水の流路を具備するものであり、アルカリ性イオン水
を浴槽に供給する場合は酸性イオン水を酸素発生効率の
高い白金電極が配設された電極室で生成し、排出される
酸性イオン水中の塩素濃度を低減して排水から有害で有
臭の塩素ガスが気化し、雰囲気中に放出されることを防
止することができるものであり、またアルカリ性イオン
水と酸性イオン水が混合された中性又は弱アルカリ性の
混合水を浴槽に供給する場合は、酸性イオン水を塩素の
発生効率が高い白金−イリジウム混合物電極が配設され
た電極室にて生成し、混合水中の塩素濃度を向上して殺
菌性能を向上することができるものであり、浴槽中の浴
槽水をアルカリ性に保ったまま高濃度の塩素にて浴槽水
を殺菌することができるものである。Further, in addition to the apparatus for modifying the quality of bathtub water according to claim 5 of the present invention,
A first electrolytic chamber having a platinum-iridium mixture electrode whose surface is formed of a platinum-iridium mixture, and a diaphragm electrolytic cell provided with a second electrolytic chamber having a platinum electrode whose surface is formed of platinum; -The alkaline ionic water generated in the diaphragm electrolyzer when the electrolysis is performed using the iridium mixture electrode as the cathode and the platinum electrode as the anode is supplied to the bath, and the acidic ion water is discharged out of the bath, and the platinum electrode is discharged. Cathode, comprising a bath water channel for supplying both alkaline ionized water and acidic ionized water generated in the diaphragm electrolyzer when electrolysis is performed using the platinum-iridium mixture electrode as the anode. Yes, when supplying alkaline ionized water to the bathtub, acidic ionized water is generated in the electrode chamber where a platinum electrode with high oxygen generation efficiency is installed, and the salt in the acidic ionized water discharged is discharged. It can prevent harmful and odorous chlorine gas from evaporating from wastewater by reducing the concentration and releasing it into the atmosphere.Also, neutral or mixed alkaline ionized water and acidic ionized water can be used. When supplying weakly alkaline mixed water to the bathtub, acidic ionized water is generated in the electrode chamber where the platinum-iridium mixture electrode with high chlorine generation efficiency is installed, and the chlorine concentration in the mixed water is improved to sterilize it. The performance can be improved, and the bath water can be sterilized with high-concentration chlorine while the bath water in the bath is kept alkaline.
【0079】また本発明の請求項6に係る浴槽水の水質
改変装置は、請求項1乃至5のいずれかの構成に加え
て、表面が白金−イリジウム混合物にて形成された白金
−イリジウム混合物電極を有する第一電解室及び表面が
白金にて形成された白金電極を有する第二電解室が設け
られた有隔膜電解槽と、白金−イリジウム混合物電極を
陰極、白金電極を陽極として電気分解を行ったときに有
隔膜電解槽にて生成されるアルカリ性イオン水を浴槽に
供給すると共に酸性イオン水を浴槽外に排出し、白金電
極を陰極、白金−イリジウム混合物電極を陽極として電
気分解を行ったときに有隔膜電解槽にて生成されるアル
カリ性イオン水を浴槽外に排出すると共に酸性イオン水
を浴槽に供給する浴槽水の流路を具備するものであり、
アルカリ性イオン水を浴槽に供給する場合は酸性イオン
水を酸素発生効率の高い白金電極が配設された電極室で
生成し、排出される酸性イオン水中の塩素濃度を低減し
て排水から有害で有臭の塩素ガスが気化し、雰囲気中に
放出されることを防止することができるものであり、ま
た酸性イオン水を浴槽に供給する場合は、酸性イオン水
を塩素の発生効率が高い白金−イリジウム混合物電極が
配設された電極室にて生成し、酸性イオン水中の塩素濃
度を向上して殺菌性能を向上することができるものであ
り、酸性イオン水にて浴槽中の浴槽水を酸性にすると共
に高濃度の塩素にて浴槽水を殺菌することができるもの
である。According to a sixth aspect of the present invention, there is provided an apparatus for modifying water quality of bathtub water according to any one of the first to fifth aspects, further comprising a platinum-iridium mixture electrode whose surface is formed of a platinum-iridium mixture. A first electrolytic chamber having a first electrolytic chamber and a second electrolytic chamber having a platinum electrode whose surface is formed of platinum, and a diaphragm-equipped electrolytic cell provided with a platinum-iridium mixture electrode as a cathode and a platinum electrode as an anode for electrolysis. When the alkaline ionized water generated in the diaphragm electrolyzer is supplied to the bath and the acidic ionized water is discharged out of the bath, the electrolysis is performed using the platinum electrode as the cathode and the platinum-iridium mixture electrode as the anode. It is provided with a bath water channel for discharging the alkaline ionized water generated in the diaphragm electrolyzer to the outside of the bathtub and supplying the acidic ionized water to the bathtub,
When supplying alkaline ionized water to the bathtub, acidic ionized water is generated in an electrode chamber equipped with a platinum electrode with high oxygen generation efficiency, and the concentration of chlorine in the discharged acidic ionized water is reduced to be harmful from wastewater. It can prevent the odorous chlorine gas from evaporating and being released into the atmosphere. When supplying acidic ionized water to the bathtub, the acidic ionized water is converted into platinum-iridium having a high chlorine generation efficiency. It is generated in the electrode chamber where the mixture electrode is disposed, and can improve the sterilization performance by increasing the chlorine concentration in the acidic ionized water, and acidify the bath water in the bathtub with the acidic ionized water. In addition, bath water can be sterilized with high-concentration chlorine.
【0080】また本発明の請求項7に係る水質改変装置
は、請求項1乃至6のいずれかの構成に加えて、有隔膜
電解槽にて生成されるアルカリ性イオン水と酸性イオン
水のうち一方のイオン水を浴槽に供給すると共に他方の
イオン水を浴槽水にて希釈した後に浴槽外に排出する浴
槽水の流路を具備するものであり、排出されるイオン水
を浴槽水にて希釈して中性に近づけた後に排出すること
ができ、特に酸性イオン水を排出する場合は浴槽水にて
希釈して中性に近づけることにより排水からの有害、有
臭の塩素ガスの気化を抑制することができるものである また本発明の請求項8に係る浴槽水の水質改変装置は、
請求項1乃至7のいずれかの構成に加えて、浴槽水を浄
化する濾過槽と、濾過槽に濾過槽の洗浄用水として浴槽
水を供給し、有隔膜電解槽にて生成されるアルカリ性イ
オン水と酸性イオン水のうち一方のイオン水を浴槽に供
給すると共に他方のイオン水を濾過槽の洗浄後の浴槽水
にて希釈した後に浴槽外に排出する浴槽水の流路を具備
するものであり、濾過槽にて入浴等により浴槽水に混入
した垢、埃、細菌等を濾過して、浴槽水を清潔に保つこ
とができるものであり、またこの濾過槽を浴槽水にて洗
浄することができるものであり、また濾過槽の洗浄に使
用された浴槽水にて、排出するイオン水を希釈して中性
に近づけた後に排出することができ、イオン水と濾過槽
洗浄後の浴槽水を別々に排出する場合よりも排水量を低
減して浴槽中の浴槽水の急激な減少を抑制することがで
き、また特に酸性イオン水を排出する場合は、この酸性
イオン水中の塩素が濾過槽洗浄後の浴槽水中に含まれる
垢、埃、細菌等の有機物や無機物と反応して分解され、
排水からの有害、有臭の塩素ガスの気化を抑制すること
ができるものである。A water quality modifying device according to claim 7 of the present invention is characterized in that, in addition to any one of the constitutions of claims 1 to 6, one of alkaline ionic water and acidic ionic water generated in a diaphragm electrolyzer. Is provided with a bathtub water flow path for supplying the ionized water to the bathtub and diluting the other ionized water with the bathtub water and then discharging the ionized water out of the bathtub, and diluting the discharged ionized water with the bathtub water. Can be discharged after approaching neutrality, especially in the case of discharging acidic ionized water, by suppressing the vaporization of harmful and odorous chlorine gas from wastewater by diluting with bath water to approach neutrality The bathtub water quality modifying device according to claim 8 of the present invention is
In addition to the configuration according to any one of claims 1 to 7, a filtration tank for purifying bath water, and bath water supplied to the filtration tank as washing water for the filtration tank, and alkaline ionic water generated in the diaphragm electrolytic cell. And a bath water flow path for supplying one ion water of the acidic ion water to the bath and diluting the other ion water with the bath water after washing the filtration bath, and then discharging the water out of the bath. It can filter out dirt, dust, bacteria, etc. mixed in the bathtub water by bathing in a filter tank, etc., to keep the bathtub water clean, and it is also possible to wash the filter tank with the bathtub water. It is also possible to dilute the ionic water to be discharged with the bath water used for washing the filtration tank and bring it closer to neutrality, and to discharge the ion water and the bath water after washing the filtration tank. Reduce the amount of drainage compared to when discharging separately The rapid decrease of water can be suppressed, and especially in the case of discharging acidic ionized water, the chlorine in the acidic ionized water contains organic and inorganic substances such as dirt, dust, and bacteria contained in the bath water after washing the filtration tank. Is decomposed by reacting with
It can suppress the vaporization of harmful and odorous chlorine gas from wastewater.
【0081】また本発明の請求項9に係る浴槽水の水質
改変装置は、請求項1乃至8のいずれかの構成に加え
て、浴槽水を浄化する濾過槽を具備するものであり、濾
過槽にて入浴等により浴槽水に混入した垢、埃、細菌等
を濾過して、浴槽水を清潔に保つことができるものであ
る。According to a ninth aspect of the present invention, there is provided an apparatus for modifying water quality of bathtub water, further comprising: By filtering dirt, dust, bacteria and the like mixed in the bathtub water by bathing or the like, the bathtub water can be kept clean.
【0082】また本発明の請求項10に係る水質改変装
置は、請求項9の構成に加えて、濾過膜として中空糸膜
を備える濾過槽と、濾過槽に濾過槽の洗浄用水として有
隔膜電解槽にて生成された酸性イオン水を供給する浴槽
水の流路とを具備するものであり、酸性イオン水中の塩
素にて中空糸膜に付着した有機物を分解除去すると共
に、中空糸膜を酸性下におくことで中空糸膜に付着して
いる金属塩を溶解して排出することができ、濾過槽の洗
浄性を向上することができるものである。The water quality modifying apparatus according to claim 10 of the present invention is characterized in that, in addition to the constitution of claim 9, a filtration tank provided with a hollow fiber membrane as a filtration membrane, and a diaphragm having a filtration tank as washing water for the filtration tank. A bath tub water flow path for supplying the acidic ion water generated in the tank, the chlorine in the acidic ion water decomposes and removes organic substances attached to the hollow fiber membrane, and removes the hollow fiber membrane from the acidic fiber. By setting it below, the metal salt adhering to the hollow fiber membrane can be dissolved and discharged, and the washing property of the filtration tank can be improved.
【図1】本発明の実施の形態の一例を示す概略図であ
る。FIG. 1 is a schematic diagram showing an example of an embodiment of the present invention.
【図2】同上の動作を示す概略図である。FIG. 2 is a schematic diagram showing the operation of the above.
【図3】同上の他の動作を示す概略図である。FIG. 3 is a schematic view showing another operation of the above.
【図4】同上の更に他の動作を示す概略図である。FIG. 4 is a schematic view showing still another operation of the above.
【図5】本発明の実施の形態の他例を示す概略図であ
る。FIG. 5 is a schematic diagram showing another example of the embodiment of the present invention.
【図6】同上の動作を示す概略図である。FIG. 6 is a schematic diagram showing the operation of the above.
【図7】同上の他の動作を示す概略図である。FIG. 7 is a schematic diagram showing another operation of the above.
【図8】同上の更に他の動作を示す概略図である。FIG. 8 is a schematic diagram showing still another operation of the above.
【図9】同上の更に他の動作を示す概略図である。FIG. 9 is a schematic diagram showing still another operation of the above.
【図10】同上の更に他の動作を示す概略図である。FIG. 10 is a schematic diagram showing still another operation of the above.
【図11】同上の更に他の動作を示す概略図である。FIG. 11 is a schematic diagram showing still another operation of the above.
【図12】本発明の実施の形態の更に他例を示す概略図
である。FIG. 12 is a schematic diagram showing still another example of the embodiment of the present invention.
【図13】同上の動作を示す概略図である。FIG. 13 is a schematic diagram showing the operation of the above.
【図14】同上の他の動作を示す概略図である。FIG. 14 is a schematic diagram showing another operation of the above.
【図15】同上の更に他の動作を示す概略図である。FIG. 15 is a schematic view showing still another operation of the above.
【図16】同上の更に他の動作を示す概略図である。FIG. 16 is a schematic diagram showing still another operation of the above.
【図17】同上の更に他の動作を示す概略図である。FIG. 17 is a schematic view showing still another operation of the above.
【図18】同上の更に他の動作を示す概略図である。FIG. 18 is a schematic view showing still another operation of the above.
【図19】同上の更に他の動作を示す概略図である。FIG. 19 is a schematic view showing still another operation of the above.
【図20】同上の更に他の動作を示す概略図である。FIG. 20 is a schematic view showing still another operation of the above.
【図21】同上の更に他の動作を示す概略図である。FIG. 21 is a schematic view showing still another operation of the above.
1 浴槽 2 有隔膜電解槽 3a 白金−イリジウム混合物電極 3b 白金電極 4 塩水供給槽 5 循環ポンプ 7 濾過槽 31 浴槽水 45 隔膜 46 濾過膜 REFERENCE SIGNS LIST 1 bath tub 2 diaphragm electrolysis tank 3 a platinum-iridium mixed electrode 3 b platinum electrode 4 salt water supply tank 5 circulation pump 7 filtration tank 31 bath water 45 diaphragm 46 filtration membrane
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【手続補正書】[Procedure amendment]
【提出日】平成11年10月25日(1999.10.
25)[Submission Date] October 25, 1999 (1999.10.
25)
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0039[Correction target item name] 0039
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0039】浴槽水31をアルカリ性に水質改変する場
合は、まず図7に示すように、第1弁32、第5弁36
が開状態、第3弁34、第4弁35、第6弁37が閉状
態となり、この状態で循環ポンプ5が作動する。このと
き循環ポンプ5の働きにより浴槽水31は流入路11、
電解導入路12、塩水槽路13、塩供給路17、電解槽
路30、第一電極室路14、第二電極室路15、第一電
極室導出路22、第二電極室導出路21、イオン水バイ
パス路24、イオン水路26、流出路16にて構成され
る循環流路と、流入路11、濾過流路27、濾過水路2
5、流出路16で構成される循環流路の、二系統の循環
流路を循環する。流入路11、濾過流路27、濾過水路
25、流出路16で構成される循環流路においては、図
6の場合と同様に、濾過槽7において浴槽水31の浄化
が行われる。また塩水供給槽4内の塩化ナトリウムが、
塩水槽路13から塩水供給槽4に供給された浴槽水31
に溶解して塩水が生成し、この塩水は塩供給路17、電
解槽路30を経由し、第一電極室路14から有隔膜電解
槽2の第一電極室2aに供給されると共に第二電極室路
15から有隔膜電解槽2の第二電極室2bに供給され、
第一電極室2a及び第二電極室2b中の余剰の塩水は第
一電極室導出路22、第二電極室導出路21、イオン水
路26、流出路16を経由して浴槽1に返送される。When the water quality of the bathtub water 31 is changed to alkaline, first, as shown in FIG.
Is opened, the third valve 34, the fourth valve 35, and the sixth valve 37 are closed, and the circulating pump 5 operates in this state. At this time, the bathtub water 31 is supplied by the operation of the circulation pump 5,
An electrolysis introduction path 12, a salt water tank path 13, a salt supply path 17, an electrolysis tank path 30, a first electrode chamber path 14, a second electrode chamber path 15, a first electrode chamber outlet path 22, a second electrode chamber outlet path 21 , A circulation flow path including an ion water bypass path 24, an ion water path 26, and an outflow path 16, the inflow path 11, the filtration flow path 27, and the filtration water path 2;
5. Circulate through two circulation passages of the circulation passage constituted by the outflow passage 16. In the circulation flow path constituted by the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Also, the sodium chloride in the salt water supply tank 4
Bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13
To form salt water, which is supplied from the first electrode chamber line 14 to the first electrode chamber 2a of the diaphragm electrolyzer 2 via the salt supply channel 17 and the electrolytic cell channel 30 and the second electrode chamber 2a. It is supplied from the electrode chamber path 15 to the second electrode chamber 2 b of the diaphragm electrolyzer 2,
Excess salt water in the first electrode chamber 2a and the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber outlet path 22 , the second electrode chamber outlet path 21 , the ion water path 26, and the outflow path 16. .
【手続補正2】[Procedure amendment 2]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0043[Correction target item name] 0043
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0043】また浴槽水31を殺菌する場合は、まず図
7に示すように、第1弁32、第5弁36が開状態、第
3弁34、第4弁35、第6弁37が閉状態となり、こ
の状態で循環ポンプ5が作動する。このとき循環ポンプ
5の働きにより浴槽水31は流入路11、電解導入路1
2、塩水槽路13、塩供給路17、電解槽路30、第一
電極室路14、第二電極室路15、第一電極室導出路2
2、第二電極室導出路21、イオン水バイパス路24、
イオン水路26、流出路16にて構成される循環流路
と、流入路11、濾過流路27、濾過水路25、流出路
16で構成される循環流路の、二系統の循環流路を循環
する。流入路11、濾過流路27、濾過水路25、流出
路16で構成される循環流路においては、図6の場合と
同様に、濾過槽7において浴槽水31の浄化が行われ
る。また塩水供給槽4内の塩化ナトリウムが、塩水槽路
13から塩水供給槽4に供給された浴槽水31に溶解し
て塩水が生成し、この塩水は塩供給路17、電解槽路3
0を経由し、第一電極室路14から有隔膜電解槽2の第
一電極室2aに供給されると共に第二電極室路15から
有隔膜電解槽2の第二電極室2bに供給され、第一電極
室2a及び第二電極室2b中の余剰の塩水は第一電極室
導出路22、第二電極室導出路21、イオン水路26、
流出路16を経由して浴槽1に返送される。When the bathtub water 31 is to be sterilized, first, as shown in FIG. 7, the first valve 32 and the fifth valve 36 are opened, and the third valve 34, the fourth valve 35 and the sixth valve 37 are closed. State, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied to the inflow channel 11 and the electrolysis introduction channel 1 by the operation of the circulation pump 5.
2, salt water tank path 13, salt supply path 17, electrolytic tank path 30, first electrode chamber path 14, second electrode chamber path 15, first electrode chamber lead-out path 2
2, the second electrode chamber lead-out path 21 , an ion water bypass path 24,
It circulates through two circulation flow paths: a circulation flow path composed of the ion water path 26 and the outflow path 16 and a circulation flow path composed of the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16. I do. In the circulation flow path constituted by the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied from the salt water tank path 13 to the salt water supply tank 4 to generate salt water.
0, is supplied from the first electrode chamber path 14 to the first electrode chamber 2a of the diaphragm electrolyzer 2 and from the second electrode chamber path 15 is supplied to the second electrode chamber 2b of the diaphragm electrolyzer 2; Excess salt water in the first electrode chamber 2a and the second electrode chamber 2b is discharged from the first electrode chamber outlet passage 22 , the second electrode chamber outlet passage 21 , the ion water passage 26,
It is returned to the bathtub 1 via the outflow channel 16.
【手続補正3】[Procedure amendment 3]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0047[Correction target item name] 0047
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0047】また浴槽水31を酸性に水質改変する場
合、まず図7に示すように、第1弁32、第5弁36が
開状態、第3弁34、第4弁35、第6弁37が閉状態
となり、この状態で循環ポンプ5が作動する。このとき
循環ポンプ5の働きにより浴槽水31は流入路11、電
解導入路12、電解槽路30、第一電極室路14、第二
電極室路15、第一電極室導出路22、第二電極室導出
路21、イオン水バイパス路24、イオン水路26、流
出路16にて構成される循環流路と、流入路11、濾過
流路27、濾過水路25、流出路16で構成される循環
流路の、二系統の循環流路を循環する。流入路11、濾
過流路27、濾過水路25、流出路16で構成される循
環流路においては、図6の場合と同様に、濾過槽7にお
いて浴槽水31の浄化が行われる。また塩水供給槽4内
の塩化ナトリウムが、塩水槽路13から塩水供給槽4に
供給された浴槽水31に溶解して塩水が生成し、この塩
水は塩供給路17、電解槽路30を経由し、第一電極室
路14から有隔膜電解槽2の第一電極室2aに供給され
ると共に第二電極室路15から有隔膜電解槽2の第二電
極室2bに供給され、第一電極室2a及び第二電極室2
b中の余剰の塩水は第一電極室導出路22、第二電極室
導出路21、イオン水路26、流出路16を経由して浴
槽1に返送される。When the bath tub water 31 is modified to have an acidic water quality, the first valve 32 and the fifth valve 36 are opened, the third valve 34, the fourth valve 35, and the sixth valve 37 are first opened as shown in FIG. Is closed, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied by the operation of the circulation pump 5 to the inflow path 11, the electrolysis introduction path 12, the electrolysis tank path 30, the first electrode chamber path 14, and the second
Electrode chamber path 15, first electrode chamber lead-out path 22, second electrode chamber lead-out
The path 21 , the circulating flow path composed of the ion water bypass path 24, the ionic water path 26, and the outflow path 16, and the circulation flow path composed of the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16. Circulate through two circulation channels. In the circulation flow path constituted by the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank path 13 to generate salt water, and this salt water passes through the salt supply path 17 and the electrolytic tank path 30. Then, the first electrode chamber 2 is supplied to the first electrode chamber 2 a of the diaphragm electrolyzer 2 from the first electrode chamber path 14, and the second electrode chamber 15 is supplied to the second electrode chamber 2 b of the diaphragm electrolyzer 2. Chamber 2a and second electrode chamber 2
The excess salt water in b is discharged from the first electrode chamber outlet passage 22 and the second electrode chamber.
The water is returned to the bathtub 1 via the outlet channel 21 , the ion water channel 26, and the outflow channel 16.
【手続補正4】[Procedure amendment 4]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0059[Correction target item name] 0059
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0059】浴槽水31をアルカリ性に水質改変する場
合は、まず図14に示すように、第1弁32、第5弁3
6、第9弁40が開状態、第2弁33、第7弁38、第
8弁39、第10弁41、第11弁42が閉状態とな
り、この状態で循環ポンプ5が作動する。このとき循環
ポンプ5の働きにより浴槽水31は流入路11、電解導
入路12、塩水槽路13、塩供給路17、第二電極室路
15、第二電極室導出路21、イオン水バイパス路2
4、イオン水路26、流出路16にて構成される循環流
路と、流入路11、濾過流路27、濾過水路25、流出
路16で構成される循環流路の、二系統の循環流路を循
環する。流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路においては、図13の場
合と同様に、濾過槽7において浴槽水31の浄化が行わ
れる。また塩水供給槽4内の塩化ナトリウムが、塩水槽
路13から塩水供給槽4に供給された浴槽水31に溶解
して塩水が生成し、この塩水は塩供給路17、第二電極
室路15から有隔膜電解槽2の第二電極室2bに供給さ
れ、第二電極室2b中の余剰の塩水は第一電極室導出路
22、イオン水路26、流出路16を経由して浴槽1に
返送される。When the water quality of the bathtub water 31 is changed to alkaline, first, as shown in FIG.
6, the ninth valve 40 is open, the second valve 33, the seventh valve 38, the eighth valve 39, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied by the operation of the circulation pump 5 so that the bath water 31 flows into the inflow path 11, the electrolytic introduction path 12, the salt water tank path 13, the salt supply path 17, the second electrode chamber path 15, the second electrode chamber outlet path 21, the ionic water bypass path. 2
4. Two circulation flow paths: a circulation flow path composed of the ion water path 26 and the outflow path 16 and a circulation flow path composed of the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16. Circulate. In the circulation flow path including the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank passage 13 to generate salt water, and the salt water is formed in the salt supply passage 17 and the second electrode chamber passage 15. Is supplied to the second electrode chamber 2b of the diaphragm electrolyzer 2, and the excess salt water in the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber outlet passage 22, the ion water passage 26, and the outflow passage 16. Is done.
【手続補正5】[Procedure amendment 5]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0060[Correction target item name] 0060
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0060】次に図15に示すように、第5弁36、第
9弁40が開状態、第1弁32、第2弁33、第7弁3
8、第8弁39、第10弁41、第11弁42が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路は維持されて、濾過槽7
において浴槽水31の浄化が引き続き行われる。この状
態で白金−イリジウム混合電極3aが陰極、白金電極3
bが陽極となるように、この電極間に電圧が印可され、
有隔膜電解槽2において電気分解により第一電極室2a
にアルカリ性イオン水が、第二電極室2bに酸性イオン
水が生成する。このように生成されたイオン水は有隔膜
電解槽2内に保持される。Next, as shown in FIG. 15 , the fifth valve 36 and the ninth valve 40 are open, the first valve 32, the second valve 33, and the seventh valve 3
The eighth, eighth, and thirty-ninth valve 41, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 continues to operate in this state.
At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained, and the filtration tank 7 is maintained.
The purifying of the bathtub water 31 is continuously performed. In this state, the platinum-iridium mixed electrode 3a serves as a cathode and the platinum electrode 3
A voltage is applied between the electrodes so that b becomes an anode,
The first electrode chamber 2a is formed by electrolysis in the diaphragm electrolytic cell 2.
And alkaline ionized water is generated in the second electrode chamber 2b. The ion water thus generated is held in the diaphragm electrolyzer 2.
【手続補正6】[Procedure amendment 6]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0065[Correction target item name] 0065
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0065】また浴槽水31を殺菌する場合は、まず図
14に示すように、第1弁32、第5弁36、第9弁4
0が開状態、第2弁33、第7弁38、第8弁39、第
10弁41、第11弁42が閉状態となり、この状態で
循環ポンプ5が作動する。このとき循環ポンプ5の働き
により浴槽水31は流入路11、電解導入路12、塩水
槽路13、塩供給路17、第二電極室路15、第二電極
室導出路21、イオン水バイパス路24、イオン水路2
6、流出路16にて構成される循環流路と、流入路1
1、濾過流路27、濾過水路25、流出路16で構成さ
れる循環流路の、二系統の循環流路を循環する。流入路
11、濾過流路27、濾過水路25、流出路16で構成
される循環流路においては、図13の場合と同様に、濾
過槽7において浴槽水31の浄化が行われる。また塩水
供給槽4内の塩化ナトリウムが、塩水槽路13から塩水
供給槽4に供給された浴槽水31に溶解して塩水が生成
し、この塩水は塩供給路17、第二電極室路15から有
隔膜電解槽2の第二電極室2bに供給され、第二電極室
2b中の余剰の塩水は第一電極室導出路22、イオン水
路26、流出路16を経由して浴槽1に返送される。When the bathtub water 31 is to be sterilized, first, as shown in FIG. 14, the first valve 32, the fifth valve 36, the ninth valve 4
0 is in an open state, the second valve 33, the seventh valve 38, the eighth valve 39, the tenth valve 41, and the eleventh valve 42 are in a closed state, and the circulating pump 5 operates in this state. At this time, the bath water 31 is supplied by the operation of the circulation pump 5 so that the bath water 31 flows into the inflow path 11, the electrolytic introduction path 12, the salt water tank path 13, the salt supply path 17, the second electrode chamber path 15, the second electrode chamber outlet path 21, and the ionic water bypass path. 24, Ion waterway 2
6. Circulation flow path composed of outflow path 16 and inflow path 1
1. Circulation is performed in two circulation passages of a circulation passage composed of a filtration passage 27, a filtration water passage 25, and an outflow passage 16. In the circulation flow path including the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank passage 13 to generate salt water, and the salt water is formed in the salt supply passage 17 and the second electrode chamber passage 15. Is supplied to the second electrode chamber 2b of the diaphragm electrolyzer 2, and the excess salt water in the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber outlet passage 22, the ion water passage 26, and the outflow passage 16. Is done.
【手続補正7】[Procedure amendment 7]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0067[Correction target item name] 0067
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0067】次に電気分解の終了後、図20に示すよう
に、第2弁33、第7弁38、第1弁32、第9弁40
が開状態、第5弁36、第8弁39、第10弁41、第
11弁42が閉状態となり、この状態で引き続き循環ポ
ンプ5が作動する。このとき流入路11、濾過流路2
7、濾過水路25、流出路16で構成される循環流路は
維持されて、濾過槽7において浴槽水31の浄化が引き
続き行われる。またこのとき流入路11、電解導入路1
2、電解槽路30を経由して、第一電極室路14から第
一電極室2a内に、第二電極室路15から第二電極室2
b内に浴槽水31が導入される水流が発生する。第一電
極室2a内の酸性イオン水は浴槽水31に押し出されて
第一電極室導出路22を経由してイオン水路26に至
り、また第二電極室2b内のアルカリ性イオン水は、第
二電極室導出路21、イオン水バイパス路24を経由し
てやはりイオン水路26に至るものであり、イオン水路
26においてアルカリ性イオン水と酸性イオン水とが混
合される。この混合水は中性又は弱アルカリ性のイオン
水であり、また酸性イオン水が高濃度で塩素を含んでい
たため、高い塩素濃度を有している。この混合水は、流
出路16において、濾過槽7において浄化された後の浴
槽水31と混合し、流出路16を通って流出口44から
浴槽1内に供給され、混合水中の塩素にて浴槽1内の浴
槽水31が殺菌される。この場合、浴槽水31の浄化と
浴槽水31の殺菌とが同時に行われる。Next, after the completion of the electrolysis, as shown in FIG. 20, the second valve 33, the seventh valve 38, the first valve 32 , and the ninth valve 40
Is in an open state, the fifth valve 36, the eighth valve 39, the tenth valve 41, and the eleventh valve 42 are in a closed state. In this state, the circulating pump 5 continues to operate. At this time, the inflow channel 11 and the filtration channel 2
The circulation flow path composed of the filtration water channel 25 and the outflow channel 16 is maintained, and the purification of the bath water 31 is continued in the filtration tank 7. At this time, the inflow path 11 and the electrolysis introduction path 1
2. Via the electrolytic cell channel 30, the first electrode channel 14 enters the first electrode chamber 2a, and the second electrode chamber channel 15 enters the second electrode chamber 2a.
A water flow into which the bathtub water 31 is introduced is generated in b. The acidic ionic water in the first electrode chamber 2a is pushed out by the bathtub water 31 and reaches the ion water channel 26 via the first electrode chamber lead-out passage 22, and the alkaline ionic water in the second electrode chamber 2b is It again reaches the ion water channel 26 via the electrode chamber lead-out channel 21 and the ion water bypass channel 24, and the alkaline ion water and the acidic ion water are mixed in the ion water channel 26. This mixed water is neutral or weakly alkaline ionized water, and has a high chlorine concentration because the acidic ionized water contains chlorine at a high concentration. This mixed water is mixed with the bath water 31 after being purified in the filtration tank 7 in the outflow passage 16, supplied into the bath tub 1 through the outflow passage 16 through the outflow passage 16, and mixed with chlorine in the mixed water. Bath water 31 in 1 is sterilized. In this case, purification of bath water 31 and sterilization of bath water 31 are performed simultaneously.
【手続補正8】[Procedure amendment 8]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0069[Correction target item name] 0069
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0069】また浴槽水31を酸性に水質改変する場
合、まず図14に示すように、第1弁32、第5弁3
6、第9弁40が開状態、第2弁33、第7弁38、第
8弁39、第10弁41、第11弁42が閉状態とな
り、この状態で循環ポンプ5が作動する。このとき循環
ポンプ5の働きにより浴槽水31は流入路11、電解導
入路12、塩水槽路13、塩供給路17、第二電極室路
15、第二電極室導出路21、イオン水バイパス路2
4、イオン水路26、流出路16にて構成される循環流
路と、流入路11、濾過流路27、濾過水路25、流出
路16で構成される循環流路の、二系統の循環流路を循
環する。流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路においては、図13の場
合と同様に、濾過槽7において浴槽水31の浄化が行わ
れる。また塩水供給槽4内の塩化ナトリウムが、塩水槽
路13から塩水供給槽4に供給された浴槽水31に溶解
して塩水が生成し、この塩水は塩供給路17、第二電極
室路15から有隔膜電解槽2の第二電極室2bに供給さ
れ、第二電極室2b中の余剰の塩水は第一電極室導出路
22、イオン水路26、流出路16を経由して浴槽1に
返送される。When the bath tub water 31 is modified to have an acidic water quality, first, as shown in FIG.
6, the ninth valve 40 is open, the second valve 33, the seventh valve 38, the eighth valve 39, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 operates in this state. At this time, the bath water 31 is supplied by the operation of the circulation pump 5 so that the bath water 31 flows into the inflow path 11, the electrolytic introduction path 12, the salt water tank path 13, the salt supply path 17, the second electrode chamber path 15, the second electrode chamber outlet path 21, the ionic water bypass path. 2
4. Two circulation flow paths: a circulation flow path composed of the ion water path 26 and the outflow path 16 and a circulation flow path composed of the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16. Circulate. In the circulation flow path including the inflow path 11, the filtration flow path 27, the filtration water path 25, and the outflow path 16, the bath water 31 is purified in the filtration tank 7, as in the case of FIG. Further, sodium chloride in the salt water supply tank 4 is dissolved in the bath water 31 supplied to the salt water supply tank 4 from the salt water tank passage 13 to generate salt water, and the salt water is formed in the salt supply passage 17 and the second electrode chamber passage 15. Is supplied to the second electrode chamber 2b of the diaphragm electrolyzer 2, and the excess salt water in the second electrode chamber 2b is returned to the bathtub 1 via the first electrode chamber outlet passage 22, the ion water passage 26, and the outflow passage 16. Is done.
【手続補正9】[Procedure amendment 9]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0070[Correction target item name] 0070
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0070】次に図15に示すように、第1弁32、第
5弁36、第9弁40が開状態、第2弁33、第7弁3
8、第8弁39、第10弁41、第11弁42が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、濾過流路27、濾過水路25、流
出路16で構成される循環流路は維持されて、濾過槽7
において浴槽水31の浄化が引き続き行われる。この状
態で白金−イリジウム混合電極3aが陽極、白金電極3
bが陰極となるように、この電極間に電圧が印可され、
有隔膜電解槽2において電気分解により第一電極室2a
に酸性イオン水が、第二電極室2bにアルカリ性イオン
水が生成する。ここで第一電極室2aに設けられた白金
−イリジウム混合電極3aは塩素の発生効率が高いた
め、この酸性イオン水中では塩素が効率よく発生され
る。このように生成されたイオン水は有隔膜電解槽2内
に保持される。Next, as shown in FIG. 15, the first valve 32, the fifth valve 36, and the ninth valve 40 are open, the second valve 33, the seventh valve 3
The eighth, eighth, and thirty-ninth valve 41, the tenth valve 41, and the eleventh valve 42 are closed, and the circulation pump 5 continues to operate in this state.
At this time, the circulation channel constituted by the inflow channel 11, the filtration channel 27, the filtration water channel 25, and the outflow channel 16 is maintained, and the filtration tank 7 is maintained.
The purifying of the bathtub water 31 is continuously performed. In this state, the platinum-iridium mixed electrode 3a serves as the anode and the platinum electrode 3
A voltage is applied between the electrodes so that b becomes a cathode,
The first electrode chamber 2a is formed by electrolysis in the diaphragm electrolytic cell 2.
Acid ion water, alkaline ionized water to the second electrode chamber 2b is produced. Here, since the platinum-iridium mixed electrode 3a provided in the first electrode chamber 2a has a high chlorine generation efficiency, chlorine is generated efficiently in the acidic ionized water. The ion water thus generated is held in the diaphragm electrolyzer 2.
【手続補正10】[Procedure amendment 10]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0072[Correction target item name] 0072
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0072】次に図17に示すように、第2弁33、第
7弁38、第8弁39、第11弁42が開状態、第1弁
32、第5弁36、第9弁40、第10弁41が閉状態
となり、この状態で引き続き循環ポンプ5が作動する。
このとき流入路11、電解導入路12、電解槽路30を
経由して、第一電極室路14から第一電極室2a内に、
第二電極室路15から第二電極室2b内に浴槽水31が
導入される水流が発生する。第一電極室2a内の酸性イ
オン水は、図16の場合と同様に、引き続き浴槽水31
に押し出されて第一電極室導出路22、イオン水路2
6、流出路16を経由して流出口44から浴槽1内に供
給されて、浴槽1内の浴槽水31を酸性に水質改変す
る。また第二電極室2b内のアルカリ性イオン水は、第
二電極室導出路21、洗浄イオン路28、濾過流路27
を経由して濾過槽7に導入される。濾過槽7内のアルカ
リ性イオン水は水圧抵抗の低い洗浄水排出路23を通過
し、排水路18を通って浴槽1外に排出される。ここ
で、図16に示す動作を行わずに、図15に示す動作か
ら直接図17に示す動作に移行することにより、有隔膜
電解槽2からのアルカリ性イオン水と酸性イオン水の排
出を同時に開始しても良い。Next, as shown in FIG. 17, the second valve 33, the seventh valve 38, the eighth valve 39, and the eleventh valve 42 are open, and the first valve 32 , the fifth valve 36, the ninth valve 40, The tenth valve 41 is closed, and the circulation pump 5 is continuously operated in this state.
At this time, via the inflow path 11, the electrolysis introduction path 12, and the electrolytic cell path 30, the first electrode chamber path 14 into the first electrode chamber 2a,
A water flow for introducing the bath water 31 from the second electrode chamber passage 15 into the second electrode chamber 2b is generated. The acidic ionic water in the first electrode chamber 2a continues to be supplied to the bath water 31 as in the case of FIG.
To the first electrode chamber outlet passage 22 and the ion water passage 2
6. The water is supplied into the bathtub 1 from the outlet 44 via the outflow passage 16, and the water quality of the bathtub water 31 in the bathtub 1 is changed to acidic. Further, the alkaline ionized water in the second electrode chamber 2b is supplied to the second electrode chamber outlet path 21, the cleaning ion path 28, the filtration path 27.
Through the filter tank 7. The alkaline ionized water in the filtration tank 7 passes through the washing water discharge passage 23 having a low hydraulic resistance, and is discharged out of the bathtub 1 through the drainage passage 18. Here, the operation shown in FIG. 15 is directly shifted to the operation shown in FIG. 17 without performing the operation shown in FIG. 16, so that the discharge of the alkaline ionized water and the acidic ionized water from the diaphragm electrolyzer 2 is started simultaneously. You may.
【手続補正11】[Procedure amendment 11]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図12[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図12】 FIG.
【手続補正12】[Procedure amendment 12]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図13[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図13】 FIG. 13
【手続補正13】[Procedure amendment 13]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図14[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図14】 FIG. 14
【手続補正14】[Procedure amendment 14]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図15[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図15】 FIG.
【手続補正15】[Procedure amendment 15]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図16[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図16】 FIG. 16
【手続補正16】[Procedure amendment 16]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図17[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図17】 FIG.
【手続補正17】[Procedure amendment 17]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図18[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図18】 FIG.
【手続補正18】[Procedure amendment 18]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図19[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図19】 FIG.
【手続補正19】[Procedure amendment 19]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図20[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図20】 FIG.
【手続補正20】[Procedure amendment 20]
【補正対象書類名】図面[Document name to be amended] Drawing
【補正対象項目名】図21[Correction target item name] FIG.
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【図21】 FIG. 21
フロントページの続き (72)発明者 氏家 良彦 大阪府門真市大字門真1048番地松下電工株 式会社内 Fターム(参考) 4D061 DA07 DB07 DB08 EA02 EB01 EB05 EB12 EB30 ED13 FA09 FA13 Continued on the front page (72) Inventor Yoshihiko Ujiie 1048 Kazuma Kadoma, Kadoma City, Osaka Prefecture F-term in Matsushita Electric Works, Ltd. 4D061 DA07 DB07 DB08 EA02 EB01 EB05 EB12 EB30 ED13 FA09 FA13
Claims (10)
にて隔てられた一方の電解室内に塩化ナトリウムを供給
する塩水供給槽と、電気分解に供される浴槽水を浴槽か
ら有隔膜電解槽に供給し、有隔膜電解槽にて電気分解に
より生成するアルカリ性イオン水と酸性イオン水のうち
一方のイオン水を浴槽に供給すると共に他方のイオン水
を浴槽外に排出する浴槽水の流路と、この浴槽水の流路
に水流を発生させる循環ポンプとを具備して成ることを
特徴とする浴槽水の水質改変装置。1. A diaphragm electrolytic cell, a salt water supply tank for supplying sodium chloride into one of the electrolytic chambers separated by a diaphragm in the diaphragm electrolytic cell, and a bath water for electrolysis from the bath. Bath water for supplying to the electrolytic bath and supplying one of alkaline ionic water and acidic ionic water generated by electrolysis in the electrolytic bath to the tub and discharging the other ionic water out of the tub. An apparatus for modifying water quality of bathtub water, comprising: a flow path; and a circulation pump for generating a water flow in the flow path of the bathtub water.
に、有隔膜電解槽にて電気分解により生成するアルカリ
性イオン水と酸性イオン水のうち一方のイオン水を連続
的に浴槽に供給し、有隔膜電解槽における電気分解の終
了後に他方のイオン水を浴槽外に排出する浴槽水の流路
を具備して成ることを特徴とする請求項1に記載の浴槽
水の水質改変装置。2. During the progress of electrolysis in a diaphragm electrolyzer, one of alkaline ionized water and acidic ionic water generated by electrolysis in the diaphragm electrolyzer is continuously supplied to the bath, 2. The bathtub water quality modifying device according to claim 1, further comprising a bathtub water flow path for discharging the other ion water out of the bathtub after the electrolysis in the diaphragm electrolyzer is completed.
にて隔てられた両方の電解室内に塩化ナトリウムを供給
する塩水供給槽と、電気分解に供される浴槽水を浴槽か
ら有隔膜電解槽に供給し、有隔膜電解槽における電気分
解終了後に、有隔膜電解槽にて電気分解により生成する
アルカリ性イオン水と酸性イオン水のうちの一方のイオ
ン水を浴槽に供給すると共に他方のイオン水を浴槽外に
排出する浴槽水の流路と、この浴槽水の流路に水流を発
生させる循環ポンプとを具備して成ることを特徴とする
浴槽水の水質改変装置。3. A diaphragm electrolyzer, a salt water supply tank for supplying sodium chloride into both electrolysis chambers separated by a diaphragm in the diaphragm electrolyzer, and a bath for electrolysis from the bath. After the electrolysis in the diaphragm electrolyzer is completed, one of the alkaline ionic water and the acidic ionic water generated by electrolysis in the diaphragm electrolyzer is supplied to the bath and the other is supplied to the bath. A bathtub water quality modifying device comprising: a bathtub water flow path for discharging ionized water out of the bathtub; and a circulation pump for generating a water flow in the bathtub water flow path.
るアルカリ性イオン水と酸性イオン水のうちのアルカリ
性イオン水を浴槽に供給すると共に酸性イオン水を浴槽
外に排出する動作と、電気分解により生成するアルカリ
性イオン水と酸性イオン水の両方を浴槽に供給する動作
とを一回ずつ交互に行うか、あるいは一方の動作を複数
回行うのに対して他方の動作を一回行うことを特徴とす
る請求項1乃至3のいずれかに記載の浴槽水の水質改変
装置。4. An operation of supplying an alkaline ionized water of an alkaline ionized water and an acidic ionized water generated by electrolysis in a diaphragm electrolyzer to a bathtub and discharging the acidic ionized water out of the bathtub; The operation of supplying both the generated alkaline ionized water and the acidic ionized water to the bath is alternately performed once each, or one operation is performed a plurality of times and the other operation is performed once. The water quality modifying device for bathtub water according to any one of claims 1 to 3.
された白金−イリジウム混合物電極を有する第一電解室
及び表面が白金にて形成された白金電極を有する第二電
解室が設けられた有隔膜電解槽と、白金−イリジウム混
合物電極を陰極、白金電極を陽極として電気分解を行っ
たときに有隔膜電解槽にて生成されるアルカリ性イオン
水を浴槽に供給すると共に酸性イオン水を浴槽外に排出
し、白金電極を陰極、白金−イリジウム混合物電極を陽
極として電気分解を行ったときに有隔膜電解槽にて生成
されるアルカリ性イオン水と酸性イオン水の両方を浴槽
に供給する浴槽水の流路を具備して成ることを特徴とす
る請求項1乃至4のいずれかに記載の浴槽水の水質改変
装置。5. A diaphragm provided with a first electrolytic chamber having a platinum-iridium mixture electrode whose surface is formed of a platinum-iridium mixture and a second electrolytic chamber having a platinum electrode whose surface is formed of platinum. Electrolyte, Platinum-Iridium mixture electrode as cathode, Platinum electrode as anode, and when electrolysis is performed, supply alkaline ionic water generated in the diaphragm electrolyzer to the bath and discharge acidic ion water out of the bath A bath water channel for supplying both alkaline ionized water and acidic ionized water generated in a diaphragm electrolytic cell when electrolysis is performed using a platinum electrode as a cathode and a platinum-iridium mixture electrode as an anode. The water quality modifying device for bathtub water according to any one of claims 1 to 4, comprising:
された白金−イリジウム混合物電極を有する第一電解室
及び表面が白金にて形成された白金電極を有する第二電
解室が設けられた有隔膜電解槽と、白金−イリジウム混
合物電極を陰極、白金電極を陽極として電気分解を行っ
たときに有隔膜電解槽にて生成されるアルカリ性イオン
水を浴槽に供給すると共に酸性イオン水を浴槽外に排出
し、白金電極を陰極、白金−イリジウム混合物電極を陽
極として電気分解を行ったときに有隔膜電解槽にて生成
されるアルカリ性イオン水を浴槽外に排出すると共に酸
性イオン水を浴槽に供給する浴槽水の流路を具備して成
ることを特徴とする請求項1乃至5のいずれかに記載の
浴槽水の水質改変装置。6. A diaphragm provided with a first electrolytic chamber having a platinum-iridium mixture electrode whose surface is formed of a platinum-iridium mixture and a second electrolytic chamber having a platinum electrode whose surface is formed of platinum. Electrolyte, Platinum-Iridium mixture electrode as cathode, Platinum electrode as anode, and when electrolysis is performed, supply alkaline ionic water generated in the diaphragm electrolyzer to the bath and discharge acidic ion water out of the bath A tub that discharges alkaline ionized water generated in a diaphragm electrolyzer when electrolysis is performed using a platinum electrode as a cathode and a platinum-iridium mixture electrode as an anode, and supplies acidic ionized water to the bathtub. The bathtub water quality modifying apparatus according to any one of claims 1 to 5, further comprising a water flow path.
イオン水と酸性イオン水のうち一方のイオン水を浴槽に
供給すると共に他方のイオン水を浴槽水にて希釈した後
に浴槽外に排出する浴槽水の流路を具備して成ることを
特徴とする請求項1乃至6のいずれかに記載の浴槽水の
水質改変装置。7. An alkaline ionized water and an acidic ionized water generated in a diaphragm electrolyzer are supplied to a bathtub, and the other ionized water is diluted with the bathtub water and then discharged out of the bathtub. The water quality modifying device for bathtub water according to any one of claims 1 to 6, further comprising a bathtub water flow path.
過槽の洗浄用水として浴槽水を供給し、有隔膜電解槽に
て生成されるアルカリ性イオン水と酸性イオン水のうち
一方のイオン水を浴槽に供給すると共に他方のイオン水
を濾過槽の洗浄後の浴槽水にて希釈した後に浴槽外に排
出する浴槽水の流路を具備して成ることを特徴とする請
求項1乃至7のいずれかに記載の浴槽水の水質改変装
置。8. A filter tank for purifying bath water, and bath water is supplied to the filter tank as washing water for the filter tank, and one of alkaline ionized water and acidic ionized water generated in the diaphragm electrolyzer is supplied. 8. A bathtub flow path for supplying water to the bathtub, diluting the other ionized water with the bathtub water after washing the filtration bath, and discharging the diluted bathwater to the outside of the bathtub. The water quality modifying device for bathtub water according to any one of the above.
ことを特徴とする請求項1乃至8のいずれかに記載の浴
槽水の水質改変装置。9. The apparatus for modifying water quality of bathtub water according to claim 1, further comprising a filtration tank for purifying bathtub water.
と、濾過槽に濾過槽の洗浄用水として有隔膜電解槽にて
生成された酸性イオン水を供給する浴槽水の流路とを具
備して成ることを特徴とする請求項9に記載の浴槽水の
水質改変装置。10. A filtration tank provided with a hollow fiber membrane as a filtration membrane, and a bath water flow path for supplying acidic ionic water generated in a diaphragm electrolysis tank as washing water for the filtration tank to the filtration tank. The water quality modifying device for bathtub water according to claim 9, wherein the water quality modifying device comprises:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14732999A JP3714031B2 (en) | 1999-05-26 | 1999-05-26 | Bath water quality modifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14732999A JP3714031B2 (en) | 1999-05-26 | 1999-05-26 | Bath water quality modifier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2000334458A true JP2000334458A (en) | 2000-12-05 |
| JP3714031B2 JP3714031B2 (en) | 2005-11-09 |
Family
ID=15427730
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14732999A Expired - Fee Related JP3714031B2 (en) | 1999-05-26 | 1999-05-26 | Bath water quality modifier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3714031B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113845181A (en) * | 2020-06-26 | 2021-12-28 | 松下知识产权经营株式会社 | Electrolyzed water generator and cleaning method of electrolyzed water generator |
-
1999
- 1999-05-26 JP JP14732999A patent/JP3714031B2/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113845181A (en) * | 2020-06-26 | 2021-12-28 | 松下知识产权经营株式会社 | Electrolyzed water generator and cleaning method of electrolyzed water generator |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3714031B2 (en) | 2005-11-09 |
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