JP2000093970A - Water cleaning apparatus - Google Patents

Water cleaning apparatus

Info

Publication number
JP2000093970A
JP2000093970A JP10266209A JP26620998A JP2000093970A JP 2000093970 A JP2000093970 A JP 2000093970A JP 10266209 A JP10266209 A JP 10266209A JP 26620998 A JP26620998 A JP 26620998A JP 2000093970 A JP2000093970 A JP 2000093970A
Authority
JP
Japan
Prior art keywords
water
chlorine
chlorine compound
supply means
ions
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
Application number
JP10266209A
Other languages
Japanese (ja)
Other versions
JP3887969B2 (en
Inventor
Yuko Fujii
優子 藤井
Tomohide Matsumoto
朋秀 松本
Takemi Oketa
岳見 桶田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP26620998A priority Critical patent/JP3887969B2/en
Publication of JP2000093970A publication Critical patent/JP2000093970A/en
Application granted granted Critical
Publication of JP3887969B2 publication Critical patent/JP3887969B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To clean water by physical cleaning system and to efficiently and stably generate a chlorine compd. by feeding chlorine ion and to perform sterilization of water in relation to cleaning of water. SOLUTION: In a circulation flow path 9, a circulation means 12 for circulating water, an agglomerating means 13 for agglomerating suspended substances in water, a filtration means 14 for filtering the suspended substances in water, a chlorine ion feeding means 16 for feeding chlorine ion to a chlorine compd. feeding means 15 are provided and the chlorine compd. feeding means 15 electrolyzes the fed chlorine ion under retained condition and after chlorine compd. such as hypochlorous acid are formed, they are mixed into the circulation flow path. It is possible thereby to obtain stable sterilization effect and to decrease amt. of chlorine ion to be fed.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は浴槽内の入浴水のよ
うに水槽水を浄化殺菌することで再使用を可能とする水
浄化装置に関し、特に水を循環して浄化し再利用する水
浄化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water purifier which purifies and sterilizes aquarium water, such as bath water in a bathtub, so that it can be reused. Related to the device.

【0002】[0002]

【従来技術】従来のこの種の水浄化装置は特開平8−2
81280号公報に記載されているようなものが一般的
であった。この水浄化装置は図8に示すように、循環路
1にポンプ2とヒーター3と内部に微生物を繁殖させた
浄化手段4を備えていた。さらに、浄化手段4の上流と
下流を結ぶバイパス路5を備え、このバイパス路5に次
亜塩素酸などの塩素化合物を生成させる殺菌手段6を備
えていた。また、ポンプ2の働きにより、浴槽8内の水
7を循環流路1からヒーター3を通って浄化手段4及び
バイパス路5の殺菌手段6に水を送り込み、浄化手段4
内に繁殖した微生物の働きにより水中の懸濁態及び有機
物質の除去を行うように構成されている。
2. Description of the Related Art A conventional water purifying apparatus of this kind is disclosed in
The one described in JP-A-81280 was common. As shown in FIG. 8, this water purification apparatus was provided with a pump 2 and a heater 3 in a circulation path 1 and a purification means 4 in which microorganisms were propagated inside. Furthermore, a bypass 5 connecting the upstream and downstream of the purification means 4 was provided, and a sterilization means 6 for producing a chlorine compound such as hypochlorous acid was provided in the bypass 5. Further, by the operation of the pump 2, the water 7 in the bathtub 8 is sent from the circulation channel 1 through the heater 3 to the purifying means 4 and the sterilizing means 6 of the bypass path 5.
It is configured to remove suspended substances in water and organic substances by the action of microorganisms propagated therein.

【0003】さらに、浄化手段4内に繁殖した微生物を
死滅させないためにバイパス路5をもうけ、バイパス路
5上に殺菌手段6を設けて残留塩素を発生させている。
この生成した残留塩素は、浄化手段4の下流側で循環流
路1の水に混合することで、浄化手段4内に存在する微
生物を死滅することなく水の浄化及び殺菌を行ってい
た。そして、殺菌手段6で生成する残留塩素の水中の濃
度を浄化手段4に影響のない0.5〜1.0ppmにする
ようにしていた。
Further, in order to prevent the microorganisms propagated in the purifying means 4 from being killed, a bypass 5 is provided, and a sterilizing means 6 is provided on the bypass 5 to generate residual chlorine.
The generated residual chlorine is mixed with the water in the circulation channel 1 downstream of the purifying means 4 to purify and sterilize the water without killing the microorganisms present in the purifying means 4. Then, the concentration of residual chlorine generated in the sterilizing means 6 in the water is adjusted to 0.5 to 1.0 ppm which does not affect the purifying means 4.

【0004】また、ここで使用する殺菌手段6としては
特開昭56−31489号公報に開示されているような
電気分解器が用いられており、さらに、殺菌用電気分解
器としては特開昭61−283391号公報に開示され
ている様な無隔膜タイプのものがある。これは電気分解
器内部に1対の電極を設け、この電極間に電流を印加す
ることで水中の塩素イオンを酸化させ、次亜塩素酸など
の塩素化合物を生成するものである。これは電気分解器
に1対の電極を設け、電極間に電流あるいは電圧を印加
することにより水中の塩素イオンを酸化させて次亜塩素
酸などの塩素化合物を生成するものである。
As the sterilizing means 6 used here, an electrolyzer disclosed in Japanese Patent Application Laid-Open No. 56-31489 is used. There is a non-diaphragm type as disclosed in JP-A-61-283391. In this method, a pair of electrodes is provided inside an electrolyzer, and a current is applied between the electrodes to oxidize chlorine ions in water to generate a chlorine compound such as hypochlorous acid. In this method, a pair of electrodes is provided in an electrolyzer, and a current or a voltage is applied between the electrodes to oxidize chlorine ions in water to generate a chlorine compound such as hypochlorous acid.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、図8に
示した従来の水浄化装置では、浄化手段内で微生物を繁
殖し、微生物によって浴槽水に溶存している有機物質な
どを浄化させているため、殺菌手段によって発生させる
塩素化合物濃度を浄化手段内の微生物に影響のない0.
5ppm〜1.0ppm以下の濃度にする必要があった。この
ように塩素化合物濃度を高くできないため、水中の細菌
の殺菌能力に限りがあるという問題があった。
However, in the conventional water purification apparatus shown in FIG. 8, microorganisms are propagated in the purification means, and the microorganisms purify organic substances and the like dissolved in bath water. The concentration of chlorine compounds generated by the sterilizing means is not affected by microorganisms in the purifying means.
It was necessary to make the concentration 5 ppm to 1.0 ppm or less. Since the chlorine compound concentration cannot be increased as described above, there is a problem that the bactericidal ability of bacteria in water is limited.

【0006】さらに、電解手段としての電気分解器は水
中の塩素イオンを電気分解することで次亜塩素酸等の塩
素化合物を生成するが、浴槽水中の塩素イオン濃度のば
らつきによる電解効率のばらつきや浴槽水中に塩素化合
物を消費するアンモニアや有機物等が含まれるため、電
解効率が低下してしまう等の問題があった。つまり、実
際には塩素化合物濃度を0.1〜0.2ppmにする能
力しかなく、安定した電解効率を得るために食塩などの
塩素イオンを含む物質を浴槽に供給する必要があった。
しかしこの場合には手作業によるメンテナンスが必要と
なった。
Further, an electrolyzer as an electrolysis means generates a chlorine compound such as hypochlorous acid by electrolyzing chloride ions in water. Since bath water contains ammonia and organic substances that consume chlorine compounds, there has been a problem that the electrolysis efficiency is reduced. In other words, in practice, it has only the ability to make the chlorine compound concentration 0.1 to 0.2 ppm, and it is necessary to supply a substance containing chlorine ions such as salt to the bathtub in order to obtain stable electrolysis efficiency.
However, in this case, manual maintenance was required.

【0007】[0007]

【課題を解決するための手段】本発明の水浄化装置は、
循環流路に水を循環する循環手段と、水中の懸濁物質を
凝集する凝集手段と、水の懸濁物質をろ過するろ過手段
と、塩素化合物供給手段に塩素イオンを供給する塩素イ
オン供給手段を設け、前記塩素化合物供給手段は供給さ
れた塩素イオンを滞留状態で電気分解し、次亜塩素酸など
の塩素化合物を生成した後、前記循環流路に混入するも
のである。
The water purifying apparatus of the present invention comprises:
Circulating means for circulating water in the circulation channel, aggregating means for aggregating suspended substances in water, filtering means for filtering suspended substances in water, and chlorine ion supplying means for supplying chlorine ions to chlorine compound supplying means The chlorine compound supply means electrolyzes the supplied chlorine ions in a stagnant state, generates a chlorine compound such as hypochlorous acid, and then mixes the chlorine ions into the circulation channel.

【0008】上記発明によれば、水中の懸濁物質等の汚
れを凝集手段で生成した金属水和物で凝集し、粒子径を
増大させ、この凝集塊を濾過手段でろ過することで、水
の浄化を行う。このため、死菌等の非常に小さな汚れや
有機物を除去することが可能となる。さらに、凝集手段
を用いた物理浄化方式を採用しているので、微生物浄化
方式に比べ供給する塩素化合物供給量を低く抑える必要
がなく、十分な殺菌効果を得ることができる。また、塩
素化合物供給手段は、塩素イオン供給手段によって供給
された高濃度の塩素イオンを含む水を滞留状態で電気分
解することで効率良く、高濃度の塩素化合物が生成可能
になる。ここで、塩素イオン供給手段は塩素化合物供給
手段のみに塩素イオンを供給すれば良いので、浴槽に供
給する場合に比べ塩素イオン添加量が少なくてすむ。こ
のため、塩素イオン(例えば食塩等)溶液の貯蔵量を低
減することが可能となり、塩素イオン溶液を長期にわた
って補給することなく効果的な殺菌が可能となる。
According to the above invention, dirt such as suspended substances in water is aggregated by the metal hydrate generated by the aggregation means, the particle diameter is increased, and the aggregate is filtered by the filtration means, whereby water is removed. Perform purification. For this reason, it becomes possible to remove very small dirt and organic matter such as dead bacteria. Furthermore, since the physical purification method using the aggregating means is employed, it is not necessary to suppress the supply amount of the chlorine compound supplied as compared with the microorganism purification method, and a sufficient sterilizing effect can be obtained. In addition, the chlorine compound supply means can efficiently generate a high concentration chlorine compound by electrolyzing water containing high concentration chloride ions supplied by the chlorine ion supply means in a stagnant state. Here, since the chlorine ion supply means only needs to supply chlorine ions to the chlorine compound supply means, the amount of chlorine ion addition is small as compared with the case where the chlorine ions are supplied to the bathtub. For this reason, it is possible to reduce the storage amount of the chloride ion (for example, salt) solution, and it is possible to perform effective sterilization without replenishing the chloride ion solution for a long time.

【0009】[0009]

【発明の実施の形態】本発明の水浄化装置は、循環流路
に水を循環する循環手段と、水中の懸濁物質を凝集する
凝集手段と、水の懸濁物質をろ過するろ過手段と、塩素
化合物供給手段に塩素イオンを供給する塩素イオン供給
手段を設け、前記塩素化合物供給手段は供給された塩素
イオンを滞留状態で電気分解し、次亜塩素酸などの塩素化
合物を生成した後、前記循環流路に混入するものであ
る。
BEST MODE FOR CARRYING OUT THE INVENTION A water purifying apparatus according to the present invention comprises a circulating means for circulating water in a circulation flow path, a flocculating means for flocculating suspended substances in water, and a filtering means for filtering suspended substances in water. A chlorine ion supply means for supplying chlorine ions to the chlorine compound supply means is provided, and the chlorine compound supply means electrolyzes the supplied chlorine ions in a stagnant state to generate a chlorine compound such as hypochlorous acid. It is mixed with the circulation flow path.

【0010】そして、水中の懸濁物質等の汚れを凝集手
段で生成した金属水和物で凝集し、粒子径を増大させ、
この凝集塊を濾過手段でろ過除去することで、死菌等の
非常に小さな汚れや有機物等を除去することが可能とな
る。さらに、水を電気分解することで塩素化合物を生成
する塩素化合物供給手段と塩素化合物供給手段に塩素イ
オンを供給する塩素イオン供給手段を設け、塩素化合物
供給手段にのみ塩素イオンを供給しその塩素イオンが混
合された水を滞留状態で電気分解するため、高濃度の塩
素イオン溶液を電気分解することになり電解効率が上が
る。また、塩素イオン供給手段は塩素化合物供給手段の
みに供給することで、塩素イオン添加量が少なくてみ、
塩素イオン(例えば食塩等)溶液の貯蔵量を低減するこ
とが可能となり、塩素イオン溶液を長期にわたって補給
することなく効果的な殺菌が可能となる。
[0010] Then, dirt such as suspended substances in water is aggregated by the metal hydrate generated by the aggregation means, and the particle diameter is increased.
By filtering and removing the aggregate by a filtration means, it becomes possible to remove very small dirt such as dead bacteria and organic substances. Further, a chlorine compound supply means for generating a chlorine compound by electrolyzing water and a chlorine ion supply means for supplying chlorine ions to the chlorine compound supply means are provided, and chlorine ions are supplied only to the chlorine compound supply means and the chlorine ion is supplied. Is electrolyzed in a stagnant state, so that a high-concentration chlorine ion solution is electrolyzed, thereby increasing the electrolysis efficiency. Also, by supplying the chlorine ion supply means only to the chlorine compound supply means, the amount of chlorine ion addition can be reduced,
The storage amount of the chloride ion (eg, salt) solution can be reduced, and effective sterilization can be performed without replenishing the chlorine ion solution for a long time.

【0011】また、塩素化合物供給手段は、水供給手段
から供給された水と塩素イオン供給手段から供給された
塩素イオンとの混合液を滞留状態で電解する構成とした
ものである。
The chlorine compound supply means is configured to electrolyze a mixed solution of water supplied from the water supply means and chlorine ions supplied from the chlorine ion supply means in a stagnant state.

【0012】そして、塩素化合物供給手段によって残留
塩素を生成するが、入浴水のように有機物や塩素を消費
する還元性物質を含んだ水ではなく、水供給手段(例え
ば水道や給湯器)からの水を電気分解することによって
短時間で高濃度の塩素化合物を生成できる。このため、
生成効率が向上し、塩素イオンの供給量を低減すること
ができる。
[0012] Then, residual chlorine is generated by the chlorine compound supply means, but not from water containing organic substances or reducing substances consuming chlorine, such as bath water, but from water supply means (for example, tap water or a water heater). By electrolyzing water, a high concentration of chlorine compounds can be generated in a short time. For this reason,
The production efficiency is improved, and the supply amount of chlorine ions can be reduced.

【0013】また、塩素化合物供給手段を5〜45℃の
温度範囲で動作させるものである。そして、塩素化合物
供給手段として電気分解を行う場合は、水温が45℃を
越えると熱分解等により急激に塩素化合物の残存量が減
少し、5℃未満では電子の活性が低下し、塩素ガスの発
生効率が低下する。このため、発生量が安定する5〜4
5℃で行うことで塩素の発生効率を良くし、殺菌性能を
向上することができる。
Further, the chlorine compound supply means is operated in a temperature range of 5 to 45 ° C. When electrolysis is performed as the chlorine compound supply means, when the water temperature exceeds 45 ° C., the residual amount of the chlorine compound decreases sharply due to thermal decomposition and the like. Generation efficiency decreases. For this reason, the amount of generation is stable.
By performing at 5 ° C., the generation efficiency of chlorine can be improved, and the sterilization performance can be improved.

【0014】本発明の請求項4にかかる水浄化装置は塩
素化合物供給手段によって生成された塩素化合物を凝集
手段の動作終了後に循環流路に混入し循環流路に混入す
るものである。
According to a fourth aspect of the present invention, in the water purifying apparatus, the chlorine compound generated by the chlorine compound supply means is mixed into the circulation flow path after the operation of the aggregating means and mixed into the circulation flow path.

【0015】そして、凝集によって浴槽水中の有機物や
細菌などを除去した浴槽水に、塩素化合物を供給するこ
とによって、塩素の消費を抑制し効率良い殺菌効果が得
られる。
By supplying a chlorine compound to the bath water from which organic substances and bacteria in the bath water have been removed by coagulation, the consumption of chlorine is suppressed and an efficient sterilizing effect is obtained.

【0016】また、循環流路に第1のバルブを設け、水
槽と塩素化合物供給手段の閉ループ循環回路を形成し、
塩素化合物供給手段によって生成された塩素化合物が所
定時間凝集手段とろ過手段を通過しない構成にしたもの
である。
Further, a first valve is provided in the circulation flow path to form a closed loop circulation circuit of the water tank and the chlorine compound supply means,
The chlorine compound generated by the chlorine compound supply means does not pass through the aggregation means and the filtration means for a predetermined time.

【0017】そして、浴槽と塩素化合物供給手段を閉ル
ープにし、塩素化合物が供給された浴槽水は凝集手段と
ろ過手段を一定時間通過しないため、ろ過手段などに堆
積された有機物や細菌などによる残留塩素の消費を防ぐ
ことができる。このため、効率良い殺菌が可能となる。
Since the bath and the chlorine compound supply means are closed loop, and the bath water supplied with the chlorine compound does not pass through the flocculation means and the filtration means for a certain period of time, residual chlorine due to organic substances and bacteria accumulated in the filtration means and the like. Consumption can be prevented. For this reason, efficient sterilization becomes possible.

【0018】また、循環流路に第2のバルブと第3のバ
ルブを設けてろ過手段に堆積した凝集塊を逆流洗浄によ
って除去した後、塩素化合物供給手段によって生成され
た塩素化合物を循環流路に混入するものである。
Further, a second valve and a third valve are provided in the circulation channel to remove aggregates deposited on the filtration means by backwashing, and then the chlorine compound generated by the chlorine compound supply means is supplied to the circulation channel. Is mixed in.

【0019】そして、塩素化合物を消費するろ過手段に
堆積した凝集塊を逆流洗浄で除去した後、塩素化合物を
循環流路を介して水槽に供給するため、残留塩素の消費
を抑制し効率良い殺菌が可能となる。
[0019] Then, after removing the agglomerates deposited on the filtration means consuming the chlorine compound by backwashing, the chlorine compound is supplied to the water tank through the circulation channel, so that the consumption of the residual chlorine is suppressed and the sterilization is performed efficiently. Becomes possible.

【0020】また、水槽水の残留塩素濃度を検知する塩
素化合物検知手段を設け、前記塩素化合物検知手段の出
力信号に応じて塩素化合物供給手段を制御するものであ
る。
Further, a chlorine compound detecting means for detecting the residual chlorine concentration of the aquarium water is provided, and the chlorine compound supplying means is controlled in accordance with an output signal of the chlorine compound detecting means.

【0021】そして、浴槽内の塩素化合物濃度に応じて
供給する塩素化合物量を制御できるので、過剰な供給を
抑え、人体や肌への影響がない。さらに塩素が消費され
て濃度が低い場合には既定値まで供給することによっ
て、十分な殺菌が可能となる。
Since the amount of the chlorine compound supplied can be controlled in accordance with the concentration of the chlorine compound in the bathtub, excessive supply is suppressed and there is no effect on the human body and skin. Further, when chlorine is consumed and the concentration is low, sufficient sterilization becomes possible by supplying the chlorine to a predetermined value.

【0022】また、浴槽水の汚れを検知する汚れ検知手
段を設け、前記汚れ検知手段の出力信号に応じて凝集手
段及び塩素化合物供給手段を動作させ、生成された塩素
化合物を循環流路に供給するものである。
Further, a dirt detecting means for detecting dirt of bathtub water is provided, and the aggregating means and the chlorine compound supplying means are operated in accordance with an output signal of the dirt detecting means to supply the generated chlorine compound to the circulation channel. Is what you do.

【0023】そして、汚れ検知手段として浴槽水の濁度
を光の透過度で検出する濁度計で検出し、汚れ具合に応
じて凝集手段を制御させることによって、浄化が完全に
行われた後、塩素化合物供給手段によって生成された塩
素化合物を循環流路に混入することによって、塩素の消
費を抑制し、効率良く十分な殺菌が可能となる。
The turbidity of the bathtub water is detected by a turbidity meter which detects the turbidity of the bath water as a dirt detecting means, and the aggregating means is controlled in accordance with the degree of dirt. By mixing the chlorine compound generated by the chlorine compound supply means into the circulation channel, the consumption of chlorine is suppressed, and efficient and sufficient sterilization becomes possible.

【0024】[0024]

【実施例】以下、本発明の一実施例について図面を用い
て説明する。なお、実施例としては水槽として浴槽を用
いた場合につき説明する。
An embodiment of the present invention will be described below with reference to the drawings. As an embodiment, a case where a bathtub is used as a water tank will be described.

【0025】(実施例1)図1において、8は浴槽であ
る。循環流路9は浴槽8から浴槽水を吸い込む吸い込み
口10から浴槽水を浴槽8に吐き出す吐き出し口11ま
での浴槽水を循環する流路である。また、循環手段12
は浴槽水を循環流路9内で循環させるポンプである。ま
た凝集手段13は、金属水和物を水に溶出可能なアルミ
ニウム製の電極及びステンレス製の本体で構成され(図
示せず)、この凝集手段13によって粒子径が増大した
懸濁物質をろ過手段14で浴槽水を浄化する。さらに塩
素イオン供給手段16は塩素化合物供給手段15に塩素
イオンを供給し、塩素化合物供給手段15は供給された
塩素イオンを電気分解することによって次亜塩素酸等の
塩素化合物を生成する。この時、塩素化合物供給手段1
5は塩素イオンが供給された水を滞留状態で電気分解し
塩素化合物を生成する。その後、生成された塩素化合物
を循環環路9に混入し浴槽8に供給する。また、浴槽水
の温度を一定に保つため循環流路9にはヒータ17を設
けて保温している。
(Embodiment 1) In FIG. 1, reference numeral 8 denotes a bathtub. The circulation flow path 9 is a flow path that circulates bathtub water from a suction port 10 that sucks bathtub water from the bathtub 8 to a discharge port 11 that discharges bathtub water into the bathtub 8. Further, the circulation means 12
Is a pump for circulating bath water in the circulation channel 9. The aggregating means 13 is composed of an aluminum electrode capable of eluting a metal hydrate into water and a stainless steel main body (not shown). At 14 purify the bath water. Further, the chlorine ion supply means 16 supplies chlorine ions to the chlorine compound supply means 15, and the chlorine compound supply means 15 generates a chlorine compound such as hypochlorous acid by electrolyzing the supplied chlorine ions. At this time, the chlorine compound supply means 1
5 electrolyzes water supplied with chlorine ions in a stagnant state to generate chlorine compounds. Thereafter, the generated chlorine compound is mixed into the circulation circuit 9 and supplied to the bath 8. Further, a heater 17 is provided in the circulation channel 9 to keep the temperature of the bath water constant.

【0026】次に動作、作用について説明すると、浴槽
水は循環流路9に流入し凝集手段13へ導かれる。凝集
手段13は、金属水和物を水に溶出可能なアルミニウム
製の電極及びステンレス製の本体(図示せず)で構成さ
れ、電極を陽極、本体を陰極として電気分解により水中
にアルミニウムイオンを溶出する。そして溶出したアル
ミニウムイオンは水中で直ちに金属水和物の水酸化アル
ミニウムとなり、この水酸化アルミニウムと水中の懸濁
物質とが化学反応し、凝集塊を生成するため、懸濁物質
の粒子径を増大することができる。この粒子径が増大し
た懸濁物質をろ過手段14(図示せず)により除去する
ことで浴槽水を浄化する。
Next, the operation and the operation will be described. The bathtub water flows into the circulation channel 9 and is guided to the aggregating means 13. The aggregating means 13 is composed of an aluminum electrode and a stainless steel main body (not shown) capable of eluting a metal hydrate into water, and eluting aluminum ions into water by electrolysis using the electrode as an anode and the main body as a cathode. I do. The eluted aluminum ions are immediately converted into aluminum hydroxide, a metal hydrate, in water, and the aluminum hydroxide reacts with the suspended substance in the water to form aggregates, thereby increasing the particle size of the suspended substance. can do. The bath water is purified by removing the suspended substance having the increased particle diameter by the filtering means 14 (not shown).

【0027】さらに、塩素イオン供給手段16は塩素イ
オンを含む溶液を貯蔵し塩素化合物供給手段15に所定
量を供給する。本実施例では塩素イオンを含む溶液とし
て化学的に安定な食塩水(NaCl溶液)を使用した。
塩素化合物供給手段15は水溶液の電気分解を行う電解
槽で構成され、内部には少なくとも一対の電極が備えら
れている(図示せず)。ここで用いた電極は、基材がチ
タンまたはチタン合金であり、表面には白金またはイリ
ジウムなどの貴金属を被膜したものを用いている。
Further, the chlorine ion supply means 16 stores a solution containing chloride ions and supplies a predetermined amount to the chlorine compound supply means 15. In this embodiment, a chemically stable salt solution (NaCl solution) was used as the solution containing chloride ions.
The chlorine compound supply means 15 is constituted by an electrolytic cell for electrolyzing an aqueous solution, and has at least a pair of electrodes inside (not shown). The electrode used here has a base material made of titanium or a titanium alloy, and has a surface coated with a precious metal such as platinum or iridium.

【0028】塩素化合物供給手段15は塩素イオン供給
手段16から塩素イオンを供給されたあと、塩素イオン
を含む溶液を滞留状態で電気分解し、次亜塩素酸等の塩
素化合物を生成して殺菌水を生成する。この殺菌水は循
環流路9を介して浴槽8に供給され、浴槽水は殺菌・浄
化される。ここで塩素イオン供給手段16により塩素イ
オンを加えるのは効率良くかつ、塩素化合物を得るため
である。
The chlorine compound supply means 15 is supplied with chlorine ions from the chlorine ion supply means 16 and then electrolyzes a solution containing chloride ions in a stagnant state to produce a chlorine compound such as hypochlorous acid to produce sterilized water. Generate This sterilized water is supplied to the bathtub 8 via the circulation channel 9, and the bathtub water is sterilized and purified. Here, the reason why chlorine ions are added by the chlorine ion supply means 16 is to obtain a chlorine compound efficiently and.

【0029】これは、塩素化合物供給手段15として電
気分解を行なっているが、この電気分解の原理としては
電極間に電流を流すと、(1)式に示すように陽極で塩
素イオンが酸化されて塩素ガス(Cl2)が発生する。
The electrolysis is performed as the chlorine compound supply means 15. The principle of this electrolysis is that when a current is passed between the electrodes, chlorine ions are oxidized at the anode as shown in equation (1). As a result, chlorine gas (Cl 2 ) is generated.

【0030】2Cl-→Cl2+2e (1) この発生したガスは(化2)に示すように水中にとけて
殺菌作用をもたらす次亜塩素酸を(HClO)を生成す
る。
2Cl → Cl 2 + 2e (1) The generated gas dissolves in water to produce hypochlorous acid (HClO) which has a bactericidal action as shown in (Chemical Formula 2).

【0031】Cl2+H2O→HClO+HCl (2) よって(1)(2)式に示すように次亜塩素酸の生成に
は塩素イオンの存在が必須条件であり、塩素イオン濃度
が高ければ高いほど次亜塩素酸の生成量が多くなる。こ
のことから塩素イオンを供給することによって短時間で
高濃度の次亜塩素酸を生成できるため、電解効率が向上
するとともに、供給される塩素イオン量が多いため、水
道水に含まれる塩素イオン濃度のばらつきを吸収し電解
効率の安定化を図ることができる。さらに塩素イオンを
供給した場合には導電率が上昇し地域の市水の導電率の
ばらつきも吸収できるため、低電圧で電気分解が可能と
なる。
Cl 2 + H 2 O → HClO + HCl (2) Therefore, as shown in the formulas (1) and (2), the presence of chloride ions is an essential condition for the generation of hypochlorous acid, and the higher the concentration of chloride ions, the higher the concentration. The more hypochlorous acid is generated, the greater the amount. From this fact, supplying chlorine ions can generate a high concentration of hypochlorous acid in a short time, improving the electrolysis efficiency and increasing the amount of supplied chlorine ions, thus increasing the concentration of chlorine ions contained in tap water. And the electrolysis efficiency can be stabilized. Further, when chlorine ions are supplied, the conductivity increases and the variation in the conductivity of city water in the region can be absorbed, so that electrolysis can be performed at a low voltage.

【0032】しかし、塩素イオンを供給する塩素イオン
供給手段16や塩素化合物供給手段15を循環流路9に
直列に設けた場合では、浴槽8及び循環系全体に塩素イ
オンを供給する構成となるため、多量の塩素イオンが必
要となっていた。
However, when the chlorine ion supply means 16 and the chlorine compound supply means 15 for supplying chlorine ions are provided in series in the circulation channel 9, the structure is such that chlorine ions are supplied to the bathtub 8 and the entire circulation system. , A large amount of chloride ions was required.

【0033】塩素イオンを塩素化合物供給手段15に供
給する構成では、塩素イオンの供給量は少なくてすみ、
しかも使用のされ方によって多少異なるが約5年程度の
メンテナンスを省くことができる。
In the configuration in which chlorine ions are supplied to the chlorine compound supply means 15, the supply amount of chlorine ions can be small,
In addition, although it varies slightly depending on the way of use, maintenance for about 5 years can be omitted.

【0034】ここで、塩素イオン供給手段16及び塩素
化合物供給手段15を循環流路9に直列に設けた場合
と、本発明の塩素化合物供給手段15のみに塩素イオン
を供給し、滞留状態で電気分解することで塩素化合物を
生成した場合の比較例を表1に示した。ここで使用する
水は井戸水のように塩素イオンを含まないものを用い
た。
Here, the case where the chlorine ion supply means 16 and the chlorine compound supply means 15 are provided in series in the circulation channel 9 and the case where chlorine ions are supplied only to the chlorine compound supply means 15 of the present invention, Table 1 shows a comparative example in which a chlorine compound was generated by decomposition. The water used here did not contain chlorine ions like well water.

【0035】[0035]

【表1】 [Table 1]

【0036】比較項目は必要な塩素イオン供給物質とし
ての食塩量(5年間を想定)と電解時の浴槽及び電解槽
の塩素イオン濃度、生成された残留塩素濃度、細菌数及
び電解電圧である。またこの浴槽8の容積は200l、
塩素化合物供給手段15の容積は300mlとした。さ
らに塩素化合物供給手段15の動作条件としての電極、
電解条件は同じとし、印加電流は1Aとした。さらに細
菌数は塩素化合物を供給する前は各々230000CF
U/ml、210000CFU/mlであり両者供大き
な差がないので問題ないとし、表1には供給1時間後の
細菌数を示した。なお、CFUはコロニーフォーミイン
グユニット(菌形成単位)のことである。
The comparison items are the required amount of salt (supposed to be 5 years) as a chloride ion supply substance, the concentration of chloride ions in the bathtub and the electrolytic cell during electrolysis, the concentration of residual chlorine generated, the number of bacteria, and the electrolysis voltage. The volume of this bathtub 8 is 200 l,
The volume of the chlorine compound supply means 15 was 300 ml. Further, an electrode as an operating condition of the chlorine compound supply means 15,
The electrolysis conditions were the same, and the applied current was 1A. Furthermore, the number of bacteria is 230,000 CF each before supplying chlorine compounds.
U / ml and 210,000 CFU / ml, and there was no significant difference between the two, and there was no problem. Table 1 shows the number of bacteria 1 hour after the supply. In addition, CFU is a colony forming unit (microbial formation unit).

【0037】この結果からも本発明の水浄化装置が、電
解効率、食塩メンテナンス、制御面、殺菌面で有効があ
ることが解った。
The results also show that the water purification apparatus of the present invention is effective in terms of electrolysis efficiency, salt maintenance, control, and sterilization.

【0038】さらに、図2に塩素化合物供給手段として
本実施例で用いた電気分解手段15の電解温度と塩素化
合物濃度について示した。この時、定電流を2A、2時
間印加し、図2にはその時の水の塩素化合物濃度を示し
た。
FIG. 2 shows the electrolysis temperature and the chlorine compound concentration of the electrolysis means 15 used in this embodiment as the chlorine compound supply means. At this time, a constant current was applied at 2 A for 2 hours, and FIG. 2 shows the chlorine compound concentration at that time.

【0039】図2に示すように、水温が5〜45℃では
生成される塩素化合物濃度はほぼ安定しており、45℃
を越えると急激に減少してくることが解る。つまり、塩
素化合物供給手段15として電気分解を実施した場合は
生成される塩素化合物は電解温度に強く依存することが
判明し、5〜45℃が最も最適な電解温度であることが
解る。このため、本発明の水浄化装置において電気分解
する入浴水は循環流路9内で循環することで温度を5〜
45℃の範囲内に低下させた後に、電気分解させて塩素
を生成させ、その後ヒータ17によって再度加熱保温
し、浴槽8内に送り込む構成にした。この結果、効率良
く残留塩素を生成でき電力消費を最低限に抑えることが
可能となった。
As shown in FIG. 2, when the water temperature is 5 to 45 ° C., the concentration of the generated chlorine compound is almost stable.
It turns out that it decreases sharply when it exceeds. That is, when electrolysis is performed as the chlorine compound supply means 15, it is found that the generated chlorine compound strongly depends on the electrolysis temperature, and it is understood that 5 to 45 ° C. is the most optimal electrolysis temperature. Therefore, the bath water electrolyzed in the water purification apparatus of the present invention is circulated in the circulation flow path 9 so that the temperature of the bath water becomes 5 to 5.
After the temperature was lowered to the range of 45 ° C., chlorine was generated by electrolysis, and then the temperature was again heated and maintained by the heater 17 and sent into the bath 8. As a result, it was possible to efficiently generate residual chlorine and to minimize power consumption.

【0040】(実施例2)図3は本発明の実施例2の水
浄化装置を示す構成図である。
(Embodiment 2) FIG. 3 is a block diagram showing a water purification apparatus according to Embodiment 2 of the present invention.

【0041】本実施例2において、実施例1と異なる点
は塩素化合物供給手段15に水を供給する水供給手段1
8(例えば水道・給湯器)を設け、塩素化合物供給手段
15は水供給手段18と、塩素イオン供給手段16から
供給された水を電気分解し、供給された塩素イオンから
塩素化合物である塩素化合物を生成する構成とした。
The second embodiment differs from the first embodiment in that the water supply means 1 for supplying water to the chlorine compound supply means 15
8 (for example, a tap water / water heater), the chlorine compound supply means 15 electrolyzes water supplied from the water supply means 18 and the chlorine ion supply means 16, and converts the supplied chlorine ions into chlorine compounds which are chlorine compounds. Is generated.

【0042】この塩素化合物つまり残留塩素によって浴
槽水の殺菌・浄化を行うが、通常浴槽水では塩素を消費
する有機物や還元性物質(Fe、Mn、Zn等)や細菌
が含まれており、塩素化合物を生成しても循環流路9及
び浴槽8に混入する前に消費されてしまい、塩素化合物
の生成効率が低くなる。しかし、本発明の水浄化装置に
おいて、塩素化合物供給手段16は水供給手段18によ
って上記物質が混入されていな水中に塩素化合物を生成
するため、循環流路9や浴槽8に混入する前の塩素化合
物の消費を抑制し、生成効率が高い。さらに、水道水等
には殺菌のため通常約1ppm程度の塩素化合物が含ま
れており、この塩素化合物も殺菌・浄化に用いることが
できるため、殺菌能力も高くなる。
Bath water is sterilized and purified by this chlorine compound, that is, residual chlorine. Usually, bath water contains chlorine-consuming organic substances, reducing substances (Fe, Mn, Zn, etc.) and bacteria. Even if a compound is generated, it is consumed before being mixed into the circulation channel 9 and the bath 8, resulting in low chlorine compound generation efficiency. However, in the water purification apparatus of the present invention, since the chlorine compound supply means 16 generates the chlorine compound in the water in which the substance is not mixed by the water supply means 18, the chlorine compound before mixing into the circulation channel 9 and the bathtub 8 is used. The compound consumption is suppressed and the production efficiency is high. Furthermore, tap water or the like usually contains about 1 ppm of a chlorine compound for sterilization, and this chlorine compound can also be used for sterilization and purification, so that the sterilization ability is also increased.

【0043】実施例1では浴槽水を電気分解したため、
塩素化合物供給手段15内の塩素化合物濃度は約260
ppmで浴槽では0.35ppmであったが、本実施例
では水供給手段18からの水を電気分解しているので塩
素化合物供給手段15内の塩素化合物濃度は330pp
mであり、浴槽の塩素化合物濃度も0.4ppmであっ
た。
In Example 1, the bath water was electrolyzed.
The chlorine compound concentration in the chlorine compound supply means 15 is about 260
In the present embodiment, the water from the water supply means 18 is electrolyzed, so that the concentration of the chlorine compound in the chlorine compound supply means 15 is 330 pp.
m, and the chlorine compound concentration in the bathtub was also 0.4 ppm.

【0044】さらに一般細菌数については生成した塩素
化合物を供給する前には250000CFU/mlあっ
たものが1100CFU/mlに抑えられた。
Further, the number of general bacteria was 250,000 CFU / ml before supplying the produced chlorine compound, but was reduced to 1100 CFU / ml.

【0045】つまり、生成した塩素化合物濃度が高いた
めに、殺菌効果も高くなった。このことから、水供給手
段18によって塩素化合物供給手段15に塩素化合物を
消費する物質を含まない水を供給することによって電解
効率を高め、殺菌効果も向上した。
That is, since the concentration of the produced chlorine compound was high, the bactericidal effect was also high. From this, by supplying water containing no substance consuming the chlorine compound to the chlorine compound supply means 15 by the water supply means 18, the electrolysis efficiency was increased and the sterilization effect was also improved.

【0046】さらに、凝集手段13によって凝集後の浄
化された入浴水に塩素化合物供給手段15によって生成
された塩素化合物を混入することで殺菌性能が高くな
る。つまり、凝集手段13及びろ過手段14により水中
の懸濁物質を除去し、その浄化した水に塩素化合物供給
手段15によって生成した塩素化合物を混入することに
よって、殺菌以外に使用されるの塩素化合物の消費を抑
制することができる。表1及び上記に述べた値は凝集後
に塩素化合物供給手段15によって生成した塩素化合物
を浴槽8に供給したが、同条件で凝集前に生成した残留
塩素を供給した場合、塩素化合物供給手段15で生成さ
れた約330ppmの塩素化合物が循環流路9に返送し
た時点で浴槽水に含まれる有機物や垢、細菌等によって
消費されてしまい、浴槽8の塩素化合物濃度は0.20
ppmにまで減少した。
Further, by mixing the chlorine compound generated by the chlorine compound supply means 15 into the bath water purified after the aggregation by the flocculation means 13, the sterilization performance is improved. That is, the suspended substance in the water is removed by the aggregating means 13 and the filtering means 14, and the chlorine compound generated by the chlorine compound supplying means 15 is mixed with the purified water, whereby the chlorine compound used for purposes other than sterilization is removed. Consumption can be suppressed. Table 1 and the values described above indicate that the chlorine compound generated by the chlorine compound supply means 15 after aggregation was supplied to the bath 8. However, when residual chlorine generated before aggregation under the same conditions was supplied, the chlorine compound supply means 15 When about 330 ppm of the generated chlorine compound is returned to the circulation channel 9, it is consumed by organic matter, dirt, bacteria, and the like contained in the bathtub water.
ppm.

【0047】よって、凝集手段13とろ過手段14によ
って浴槽水中の有機物等の塩素化合物を消費する物質を
除去し、その後塩素化合物供給手段15によって生成し
た塩素化合物を浴槽8に供給することで効率良い殺菌が
可能となる。
Therefore, a substance that consumes a chlorine compound such as an organic substance in bath water is removed by the aggregating means 13 and the filtering means 14, and then the chlorine compound generated by the chlorine compound supplying means 15 is supplied to the bath 8 by the chlorine compound supplying means. Sterilization becomes possible.

【0048】(実施例3)図4は本発明の実施例3の水
浄化装置を示す構成図である。
(Embodiment 3) FIG. 4 is a block diagram showing a water purification apparatus according to Embodiment 3 of the present invention.

【0049】なお、実施例1と同一符号のものは同一構
成を有し、説明は省略する。本実施例3において、実施
例1及び2と異なる点は浴槽8と塩素化合物供給手段1
5の閉ループ循環回路を形成するように循環流路9に第
1のバルブ19を設け、塩素化合物が混入された水が所
定時間凝集手段13とろ過手段14を通過しない構成に
したものである。
The components having the same reference numerals as in the first embodiment have the same configuration, and the description will be omitted. The third embodiment is different from the first and second embodiments in that the bath 8 and the chlorine compound supply means 1 are different.
A first valve 19 is provided in the circulation flow path 9 so as to form a closed loop circulation circuit of No. 5 so that water containing a chlorine compound does not pass through the aggregation means 13 and the filtration means 14 for a predetermined time.

【0050】次に動作、作用を説明すると、循環流路9
に第1のバルブ19を設けることにより、凝集手段13
及びろ過手段14の動作時には浴槽水は図4に示す19
−aの方向に流れ、吐き出し口11を通り浴槽8に入り
循環する。
Next, the operation and operation will be described.
By providing the first valve 19 to the aggregating means 13
When the filtering means 14 is in operation, the bath water is supplied to the tub 19 shown in FIG.
It flows in the direction of -a, passes through the outlet 11 and enters the bathtub 8 to circulate.

【0051】次に凝集手段13及びろ過手段14が所定
時間動作した後、第1のバルブ19によって浴槽8と塩
素化合物供給手段15の閉ループ循環回路を形成し浴槽
水は図4に示す19−b方向に循環し、所定時間凝集手
段13とろ過手段14を通過しない構成にする。そして
塩素化合物供給手段15によって滞留状態で電気分解す
ることで生成された塩素化合物は形成した閉ループ循環
回路内の水中に供給することで、浴槽水を殺菌・浄化す
る。
Next, after the aggregating means 13 and the filtering means 14 operate for a predetermined time, the first valve 19 forms a closed loop circulation circuit of the bathtub 8 and the chlorine compound supply means 15, and the bathtub water is 19-b shown in FIG. In such a direction as not to pass through the aggregating means 13 and the filtering means 14 for a predetermined time. The chlorine compound generated by the electrolysis in the stagnant state by the chlorine compound supply means 15 is supplied into the water in the formed closed loop circulation circuit to sterilize and purify the bath water.

【0052】開ループ(19−a)と閉ループ(19−
b)での浴槽に存在する塩素化合物濃度について測定し
た。その結果、開ループでは0.4ppmであったが本
実施例の閉ループの場合では約0.5ppm存在した。
The open loop (19-a) and the closed loop (19-a)
The chlorine compound concentration present in the bath in b) was measured. As a result, it was 0.4 ppm in the open loop, but was about 0.5 ppm in the case of the closed loop of this embodiment.

【0053】これは、凝集手段13及びろ過手段14に
は除去した浴槽水の混濁物質等が存在しており、塩素化
合物供給手段15によって生成された塩素化合物も凝集
手段13及びろ過手段を循環することによって消費され
てしまう。しかし、本実施例のように第1のバルブ19
を設けて閉ループを形成することにより、残留塩素の消
費を抑制すると、浴槽中の残留塩素濃度が約1.3倍ほ
ど高くなり、殺菌効果も向上した。
This is because the turbid substance and the like removed from the bathtub water are present in the flocculating means 13 and the filtering means 14, and the chlorine compound generated by the chlorine compound supplying means 15 also circulates through the flocculating means 13 and the filtering means. It is consumed by things. However, as in this embodiment, the first valve 19
When a closed loop was formed to provide a closed loop to suppress the consumption of residual chlorine, the concentration of residual chlorine in the bathtub was increased about 1.3 times, and the sterilizing effect was also improved.

【0054】(実施例4)図5は本発明の実施例4の水
浄化装置を示す構成図である。
(Embodiment 4) FIG. 5 is a block diagram showing a water purification apparatus according to Embodiment 4 of the present invention.

【0055】なお、実施例1と同一符号のものは同一構
成を有し、説明は省略する。本実施例3において、実施
例1、2及び3と異なる点は第2のバルブ20を設け、
第一のバルブ19と第2のバルブ20、第3のバルブ2
1の動作制御によりろ過手段14に堆積した凝集塊を逆
流洗浄することで除去した後、塩素化合物供給手段15
によって生成された塩素化合物を浴槽8に供給する構成
にした点である。
The components having the same reference numerals as in the first embodiment have the same configuration, and the description is omitted. The third embodiment is different from the first, second and third embodiments in that a second valve 20 is provided.
First valve 19, second valve 20, third valve 2
After removing the agglomerates deposited on the filtration means 14 by backflow washing under the operation control of 1, the chlorine compound supply means 15
Is that the chlorine compound generated by the above is supplied to the bathtub 8.

【0056】次に動作、作用を説明すると、凝集手段1
3及びろ過手段14の動作時では浴槽水は図5に示す1
9−aの方向に流れ、吐き出し口11を通り浴槽8に入
り循環される。次に凝集手段13及びろ過手段14が所
定時間動作した後、第1のバルブ19及び第2のバルブ
20によって水は20−b方向に流れる。この時、第3
のバルブ21は開き循環回路によってろ過手段14は逆
流洗浄され、堆積された混濁物質を排出することができ
る。その後、第1のバルブ19、第2のバルブ20、第
3のバルブ21を元に戻し、浴槽水を20−a方向に循
環し、塩素化合物供給手段15によって生成された塩素
化合物を循環流路9に混入し殺菌・浄化を行う。
Next, the operation and operation will be described.
3 and the operation of the filtration means 14, the bathtub water is 1 shown in FIG.
It flows in the direction of 9-a and enters the bathtub 8 through the outlet 11 and is circulated. Next, after the aggregation means 13 and the filtration means 14 operate for a predetermined time, the water flows in the 20-b direction by the first valve 19 and the second valve 20. At this time, the third
The valve 21 is opened, and the filtration means 14 is backwashed by the circulation circuit, and the accumulated turbid substance can be discharged. Thereafter, the first valve 19, the second valve 20, and the third valve 21 are returned to their original positions, the bath water is circulated in the 20-a direction, and the chlorine compound generated by the chlorine compound supply means 15 is circulated in the circulation flow path. 9 to sterilize and purify.

【0057】この場合も塩素化合物の消費が抑えられ、
実施例3と同様に効率良い殺菌効果が得られた。
Also in this case, the consumption of chlorine compounds is suppressed,
As in Example 3, an efficient bactericidal effect was obtained.

【0058】(実施例5)図6は本発明の実施例5の水
浄化装置を示す構成図である。なお、実施例1と同一符
号のものは同一構成を有し、説明は省略する。
(Embodiment 5) FIG. 6 is a block diagram showing a water purification apparatus according to Embodiment 5 of the present invention. The components having the same reference numerals as those in the first embodiment have the same configuration, and the description will be omitted.

【0059】本実施例5において、実施例1〜4と異な
る点は、浴槽水の塩素化合物濃度を検知する塩素化合物
検知手段22を設け、前記塩素化合物検知手段22の出
力信号に応じて塩素化合物供給手段15の動作時間を制
御する構成にしたものである。
The fifth embodiment is different from the first to fourth embodiments in that a chlorine compound detecting means 22 for detecting the concentration of a chlorine compound in bathtub water is provided, and a chlorine compound detecting means 22 is provided in accordance with an output signal of the chlorine compound detecting means 22. In this configuration, the operation time of the supply unit 15 is controlled.

【0060】次に動作、作用を説明すると、塩素化合物
供給手段15によって生成された塩素化合物は循環流路
9に混入され、浴槽水の有機物の分解や殺菌を行う。殺
菌能力は実施例1でも述べたように、浴槽水に含まれる
塩素化合物濃度に依存し、高ければ高いほど殺菌効果は
高い。しかし、微生物浄化では塩素化合物濃度を0.5
〜1.0ppm以内に抑える必要があるため、殺菌能力
に限界があるが、本発明の物理浄化方式では上限がない
ため十分な殺菌効果が得られる。しかし、実際には浴槽
水には塩素化合物を消費してしまう物質が含まれている
ため、塩素化合物供給手段15で生成された塩素化合物
を供給してもすぐに消費されてしまい、供給時に1pp
mであっても即座に消費され浴槽水の塩素化合物濃度は
0.1〜0.2ppmにまで低下する。また、この消費
速度は浴槽水に含まれる有機物等の塩素化合物を消費す
る物質によって異なるため、浴槽水の状態によって異な
ってしまい、安定した殺菌ができない状態であった。こ
のため、最適な塩素化合物濃度に保持する必要があり、
図6に示す浴槽の塩素化合物濃度を塩素化合物検知手段
22によって検知し、浴槽水の塩素化合物濃度が所定値
になるよう塩素化合物供給手段15を制御した。本実施
例において、塩素化合物検知手段22はアンペロメトリ
方式(電流滴定方式)の測定器を用いた。本実施例で
は、塩素化合物供給手段15によって滞留状態で塩素イ
オンを電気分解し、生成した塩素化合物を浴槽8に供給
後の塩素化合物の消費速度を検知し、その速度が既定値
以上であれば、再度塩素化合物供給手段15によって塩
素化合物を生成し供給する構成にした。
Next, the operation and action will be described. The chlorine compound generated by the chlorine compound supply means 15 is mixed into the circulation channel 9 to decompose and sterilize organic matter in the bathtub water. As described in Example 1, the sterilizing ability depends on the concentration of the chlorine compound contained in the bath water, and the higher the higher, the higher the sterilizing effect. However, in microbial purification, the chlorine compound concentration is set to 0.5
Since it is necessary to suppress the concentration to within 1.0 ppm, there is a limit to the sterilization ability. However, the physical purification system of the present invention has no upper limit, so that a sufficient sterilization effect can be obtained. However, since the bathtub water actually contains a substance that consumes a chlorine compound, even if the chlorine compound generated by the chlorine compound supply means 15 is supplied, it is immediately consumed, and 1 pp at the time of supply is supplied.
m, it is immediately consumed and the concentration of chlorine compounds in the bath water drops to 0.1 to 0.2 ppm. In addition, the consumption rate varies depending on the substance that consumes a chlorine compound such as an organic substance contained in the bathtub water, and therefore varies depending on the state of the bathtub water, so that stable sterilization cannot be performed. For this reason, it is necessary to maintain the optimal chlorine compound concentration,
The chlorine compound concentration in the bathtub shown in FIG. 6 was detected by the chlorine compound detection unit 22, and the chlorine compound supply unit 15 was controlled such that the chlorine compound concentration in the bathtub water became a predetermined value. In the present embodiment, an amperometric (current titration) measuring device was used as the chlorine compound detecting means 22. In the present embodiment, chlorine ions are electrolyzed in a stagnant state by the chlorine compound supply means 15 and the consumption rate of the chlorine compound after supplying the generated chlorine compound to the bath 8 is detected. Then, the chlorine compound is again generated and supplied by the chlorine compound supply means 15.

【0061】この結果、殺菌・浄化性能を向上し、常に
一定の殺菌能力を持つことが可能となった。
As a result, it is possible to improve the sterilizing / purifying performance and to always have a constant sterilizing ability.

【0062】(実施例6)図7は本発明の実施例6の水
浄化装置を示す構成図である。
(Embodiment 6) FIG. 7 is a block diagram showing a water purification apparatus according to Embodiment 6 of the present invention.

【0063】本実施例3において、実施例1〜5と異な
る点は入浴水の汚れを検知する汚れ検知手段23を設け
ている点である。
The third embodiment differs from the first to fifth embodiments in that a dirt detecting means 23 for detecting dirt in bathing water is provided.

【0064】なお、実施例1と同一符号のものは同一構
成を有し、説明は省略する。次に動作、作用を説明する
と、汚れ検知手段23は浴槽水の汚れを検知し、その汚
れ検知手段23の値が規定値以下になるまで凝集手段1
3を動作させた後、塩素化合物供給手段15によって生
成された塩素化合物を浴槽8に供給する構成とした。こ
こで、汚れ検知手段23として浴槽水の濁度を光の透過
度で検知する濁度計を使用した。浴槽水の汚れは、細菌
(生菌、死菌)や、人体から分泌される有機物、アンモ
ニア、垢等が挙げられる。このため、これら全てを濁度
として検出する事によって入浴水の状態を検知し凝集手
段13を制御する。
The components having the same reference numerals as in the first embodiment have the same configuration, and the description will be omitted. Next, the operation and action will be described. The dirt detecting means 23 detects dirt in the bathtub water, and until the value of the dirt detecting means 23 becomes equal to or less than a specified value, the agglutination means 1
3 was operated, and the chlorine compound generated by the chlorine compound supply means 15 was supplied to the bath 8. Here, a turbidity meter that detects the turbidity of bath water by the light transmittance was used as the dirt detecting means 23. Bath water stains include bacteria (live and dead), organic matter secreted from the human body, ammonia, dirt, and the like. Therefore, the state of bathing water is detected by detecting all of these as turbidity, and the aggregating means 13 is controlled.

【0065】このため、入浴水の汚れ具合に応じて凝集
手段13の動作時間を制御することができるため、塩素
化合物供給手段15によって生成された塩素化合物を供
給する前の入浴水は常に一定の条件に保つことができ
る。この結果、塩素が汚れ等によって殺菌以外に消費さ
れるのを抑制することができるため、入浴水の状態に関
わらずより効率良く殺菌効果を得ることができる。
Since the operation time of the aggregating means 13 can be controlled in accordance with the degree of contamination of the bath water, the bath water before the supply of the chlorine compound generated by the chlorine compound supply means 15 is always constant. Condition can be kept. As a result, it is possible to suppress the consumption of chlorine other than sterilization due to dirt or the like, so that a sterilizing effect can be obtained more efficiently regardless of the state of bathing water.

【0066】なお、上記実施例では循環水として浴槽水
を循環して利用した場合について説明したが、これに限
定されるものではなく浴槽水を浄化後、洗濯水や下洗い
水として利用する場合であってもよい。これら洗濯水や
下洗い水等として利用する場合、水槽として浴槽を利用
して循環して浄化後用いてもよいし、実用的に問題にな
らない場合は上記循環流路で浄化した後、直ちに利用し
てもよい。この場合は上記実施例における吐き出し口が
そのまま洗濯機等の給水口となる。
In the above embodiment, the case where the bathtub water is circulated and used as the circulating water has been described. However, the present invention is not limited to this case. It may be. When used as washing water or underwashing water, etc., the water may be circulated and purified using a bath tub, or if it does not pose a practical problem, purified immediately in the circulation channel and immediately used. May be. In this case, the spout in the above embodiment becomes the water supply port of the washing machine or the like as it is.

【0067】上記以外でも業務上水を再利用する場合の
水浄化装置に用いることができるのは勿論である。
Other than the above, it is needless to say that the present invention can be used for a water purifying apparatus when water is reused for business purposes.

【0068】[0068]

【発明の効果】以上の説明から明らかなように、本発明
の水浄化装置によれば、次の効果が得られる。
As apparent from the above description, the water purifying apparatus of the present invention has the following effects.

【0069】(1)塩素化合物供給手段のみに塩素イオ
ンを供給する塩素イオン供給手段を設けて滞留電解によ
って塩素化合物供給手段によって塩素化合物を生成した
後、浴槽に返送する構成にすることで塩素イオン添加量
を低減でき、塩素イオン溶液を長期にわたって補給する
必要が無い。さらに塩素イオンを含む溶液を電気分解す
ることで効率のよい殺菌が可能となる。
(1) A chlorine ion supply means for supplying chlorine ions only to the chlorine compound supply means is provided, and a chlorine compound is generated by the chlorine compound supply means by residence electrolysis, and then returned to the bathtub. The amount of addition can be reduced, and there is no need to replenish the chloride ion solution for a long time. Furthermore, efficient sterilization becomes possible by electrolyzing a solution containing chlorine ions.

【0070】(2)水供給手段(例えば水道や給湯器)
からの水を電気分解することによって殺菌以外の塩素の
消費を抑制できるため塩素化合物の生成効率が向上する
とともに、塩素イオン供給手段の塩素イオン添加量を低
減することが可能となる。
(2) Water supply means (for example, water supply and water heater)
By electrolyzing water from the wastewater, the consumption of chlorine other than sterilization can be suppressed, so that the efficiency of chlorine compound generation is improved and the amount of chlorine ions added to the chlorine ion supply means can be reduced.

【0071】(3)塩素化合物供給手段としての電気分
解の電解温度を5〜45℃の範囲内で動作することで塩
素の発生効率を向上できるため、余分な塩素イオンの供
給を抑制できるので、メンテナンスの回数を削減でき、
かつ効率良く殺菌性能を向上することができる。
(3) Since the efficiency of chlorine generation can be improved by operating the electrolysis temperature in the range of 5 to 45 ° C. as the chlorine compound supply means, the supply of excess chlorine ions can be suppressed. Maintenance frequency can be reduced,
And the sterilization performance can be improved efficiently.

【0072】(4)凝集手段が動作終了後の有機物や細
菌などを除去した水に塩素化合物給手段によって生成し
た塩素化合物を循環流路に混入することによって、塩素
の消費を抑制し効率良い殺菌効果が得られた。
(4) The chlorine compound generated by the chlorine compound supply means is mixed into the circulation channel in water from which organic substances and bacteria have been removed after the operation of the flocculation means, thereby suppressing the consumption of chlorine and efficiently sterilizing. The effect was obtained.

【0073】(5)水槽と塩素化合物供給手段の閉ルー
プ循環回路を形成可能に循環流路にバルブを設け、塩素
化合物が混入された水は所定時間凝集手段とろ過手段を
通過しない構成にすることでろ過手段などに堆積された
有機物や細菌などによる塩素の消費を防ぐことができ、
効率良い殺菌が可能となる。
(5) A valve is provided in the circulation passage so that a closed loop circulation circuit of the water tank and the chlorine compound supply means can be formed, so that water containing the chlorine compound does not pass through the aggregation means and the filtration means for a predetermined time. It can prevent the consumption of chlorine by organic substances and bacteria etc. deposited on the filtration means, etc.
Efficient sterilization becomes possible.

【0074】(6)循環流路に第三のバルブを設けてろ
過手段に堆積した凝集塊を逆流洗浄することで除去した
後、塩素化合物供給手段を動作させて塩素化合物を水槽
に供給することで塩素の消費が抑えられ、効率良い殺菌
が可能となる。
(6) A third valve is provided in the circulation flow path to remove aggregates deposited on the filtration means by backwashing, and then the chlorine compound supply means is operated to supply the chlorine compound to the water tank. Thus, the consumption of chlorine is suppressed, and efficient sterilization becomes possible.

【0075】(7)水槽水の塩素化合物濃度を検知する
塩素化合物検知手段の出力信号に応じて塩素化合物供給
手段を制御することで、水槽水の状態にかかわらず安定
した殺菌が可能となる。
(7) By controlling the chlorine compound supply means according to the output signal of the chlorine compound detection means for detecting the concentration of the chlorine compound in the aquarium water, stable sterilization can be performed regardless of the state of the aquarium water.

【0076】(8)汚れ検知手段を設けて、水槽水の汚
れを検知し、汚れ具合に応じて凝集手段を動作させる時
間を制御する。その後、塩素化合物供給手段によって生
成された塩素を供給することで、水槽水の状態に関わら
ず常に一定の浄化・殺菌効果を得ることが可能となると
同時に供給する塩素イオンの量も低減できた。
(8) A dirt detecting means is provided to detect dirt in the aquarium water and to control the time for operating the aggregating means according to the degree of dirt. Thereafter, by supplying the chlorine generated by the chlorine compound supply means, it was possible to always obtain a constant purifying / sterilizing effect irrespective of the state of the aquarium water, and at the same time, it was possible to reduce the amount of supplied chlorine ions.

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

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

【図2】同水浄化装置の電解温度と残留塩素濃度の関係
を示す特性図
FIG. 2 is a characteristic diagram showing a relationship between electrolysis temperature and residual chlorine concentration of the water purification device.

【図3】本発明の実施例2における水浄化装置の構成図FIG. 3 is a configuration diagram of a water purification device according to a second embodiment of the present invention.

【図4】本発明の実施例3における水浄化装置の構成FIG. 4 is a configuration of a water purification device according to a third embodiment of the present invention.

【図5】本発明の実施例4における水浄化装置の構成図FIG. 5 is a configuration diagram of a water purification device according to a fourth embodiment of the present invention.

【図6】本発明の実施例5における水浄化装置の構成図FIG. 6 is a configuration diagram of a water purification device according to a fifth embodiment of the present invention.

【図7】本発明の実施例6における水浄化装置の構成図FIG. 7 is a configuration diagram of a water purification device according to a sixth embodiment of the present invention.

【図8】従来の水浄化装置の構成図FIG. 8 is a configuration diagram of a conventional water purification device.

【符号の説明】[Explanation of symbols]

8 浴槽 9 循環流路 10 吸い込み口 11 吐き出し口 12 ポンプ 13 凝集手段 14 ろ過手段 15 塩素化合物供給手段 16 塩素イオン供給手段 17 ヒータ 18 水供給手段 19 第1のバルブ 20 第2のバルブ 21 第3のバルブ 22 残留塩素検知手段 23 汚れ検知手段 Reference Signs List 8 bathtub 9 circulation channel 10 suction port 11 discharge port 12 pump 13 coagulation means 14 filtration means 15 chlorine compound supply means 16 chlorine ion supply means 17 heater 18 water supply means 19 first valve 20 second valve 21 third Valve 22 Residual chlorine detecting means 23 Dirt detecting means

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/50 550 C02F 1/50 550D 550L 560 560F 560Z 1/52 1/52 Z 1/76 1/76 A (72)発明者 桶田 岳見 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 4D050 AA10 AB06 BB04 BB06 BD04 BD06 BD08 CA15 CA16 4D061 AA07 AB01 AB10 AB11 AB15 BA03 BB01 BB04 BB27 BB37 BB39 BD12 4D062 BA17 BA19 BA21 BA28 BB01 CA20 DA09 DC04 EA35 FA23 FA24 FA29 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/50 550 C02F 1/50 550D 550L 560 560F 560Z 1/52 1/52 Z 1/76 1/76 A (72) Inventor Takemi Okeda 1006 Kazuma Kadoma, Kadoma, Osaka Prefecture F-term (reference) 4D050 AA10 AB06 BB04 BB06 BD04 BD06 BD08 CA15 CA16 4D061 AA07 AB01 AB10 AB11 AB15 BA03 BB01 BB04 BB27 BB37 BB37 BD12 4D062 BA17 BA19 BA21 BA28 BB01 CA20 DA09 DC04 EA35 FA23 FA24 FA29

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】循環流路に水を循環する循環手段と、水中
の懸濁物質を凝集する凝集手段と、水の懸濁物質をろ過
するろ過手段と、塩素化合物供給手段に塩素イオンを供
給する塩素イオン供給手段を設け、前記塩素化合物供給
手段は供給された塩素イオンを滞留状態で電気分解し、次
亜塩素酸などの塩素化合物を生成した後、この生成物を
前記循環流路に混入する水浄化装置。
1. A circulating means for circulating water in a circulation channel, an aggregating means for aggregating suspended matter in water, a filtering means for filtering a suspended substance in water, and supplying chlorine ions to a chlorine compound supplying means. The chlorine compound supply means electrolyzes the supplied chlorine ions in a stagnant state to generate a chlorine compound such as hypochlorous acid, and then mixes the product into the circulation channel. Water purification equipment.
【請求項2】塩素化合物供給手段は、水供給手段から供
給された水と塩素イオン供給手段から供給された塩素イ
オンとの混合液を滞留状態で電解する構成とした請求項
1記載の水浄化装置。
2. The water purification system according to claim 1, wherein the chlorine compound supply means is configured to electrolyze a mixed solution of water supplied from the water supply means and chlorine ions supplied from the chloride ion supply means in a stagnant state. apparatus.
【請求項3】塩素化合物供給手段を5〜45℃の温度範
囲で動作させる請求項1または2記載の水浄化装置。
3. The water purifier according to claim 1, wherein the chlorine compound supply means is operated in a temperature range of 5 to 45 ° C.
【請求項4】塩素化合物供給手段は、凝集手段の動作終
了後に生成した塩素化合物を循環流路に混入する請求項
1ないし3のいずれか1項記載の水浄化装置。
4. The water purification apparatus according to claim 1, wherein the chlorine compound supply means mixes the chlorine compound generated after the operation of the aggregating means into the circulation channel.
【請求項5】循環流路に第1のバルブを設け、水槽と塩
素化合物供給手段の閉ループ循環回路を形成し、塩素化
合物供給手段によって生成された塩素化合物が所定時間
凝集手段とろ過手段を通過しない構成にした請求項1な
いし4のいずれか1項記載の水浄化装置。
5. A first valve is provided in a circulation flow path to form a closed loop circulation circuit of a water tank and a chlorine compound supply means, and a chlorine compound generated by the chlorine compound supply means passes through the aggregation means and the filtration means for a predetermined time. The water purification device according to any one of claims 1 to 4, wherein the water purification device is not configured.
【請求項6】循環流路に第2のバルブを設けてろ過手段
に堆積した凝集塊を逆流洗浄することで除去した後、塩
素化合物供給手段によって生成された塩素化合物を循環
流路に混入する請求項1ないし5のいずれか1項記載の
水浄化装置。
6. A second valve is provided in the circulation channel to remove agglomerates deposited on the filtration unit by backwashing, and then the chlorine compound generated by the chlorine compound supply unit is mixed into the circulation channel. The water purification device according to any one of claims 1 to 5.
【請求項7】水槽水の塩素化合物濃度を検知する塩素化
合物検知手段を設け、前記塩素化合物検知手段の出力信
号に応じて塩素化合物供給手段を制御する請求項1ない
し6のいずれか1項記載の水浄化装置。
7. The apparatus according to claim 1, further comprising chlorine compound detecting means for detecting a chlorine compound concentration in the tank water, and controlling the chlorine compound supplying means in accordance with an output signal of said chlorine compound detecting means. Water purification equipment.
【請求項8】水槽水の汚れを検知する汚れ検知手段を設
け、前記汚れ検知手段の出力信号に応じて凝集手段及び
塩素化合物供給手段を制御する請求項1ないし7のいず
れか1項記載の水浄化装置。
8. The method according to claim 1, further comprising the step of: detecting dirt in the aquarium water, and controlling the aggregating means and the chlorine compound supplying means in accordance with an output signal of the dirt detecting means. Water purification device.
JP26620998A 1998-09-21 1998-09-21 Water purification equipment Expired - Fee Related JP3887969B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26620998A JP3887969B2 (en) 1998-09-21 1998-09-21 Water purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26620998A JP3887969B2 (en) 1998-09-21 1998-09-21 Water purification equipment

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Publication Number Publication Date
JP2000093970A true JP2000093970A (en) 2000-04-04
JP3887969B2 JP3887969B2 (en) 2007-02-28

Family

ID=17427786

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Application Number Title Priority Date Filing Date
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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6699381B2 (en) 2000-10-27 2004-03-02 Omega Co., Ltd. Water purification/sterilization method and device therefor
WO2005077831A1 (en) * 2004-02-12 2005-08-25 Denkai Giken Co. Electrochemical water treatment method and device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6699381B2 (en) 2000-10-27 2004-03-02 Omega Co., Ltd. Water purification/sterilization method and device therefor
WO2005077831A1 (en) * 2004-02-12 2005-08-25 Denkai Giken Co. Electrochemical water treatment method and device

Also Published As

Publication number Publication date
JP3887969B2 (en) 2007-02-28

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