JPH09141283A - Circulation purifying device for contaminated liquid - Google Patents

Circulation purifying device for contaminated liquid

Info

Publication number
JPH09141283A
JPH09141283A JP7326371A JP32637195A JPH09141283A JP H09141283 A JPH09141283 A JP H09141283A JP 7326371 A JP7326371 A JP 7326371A JP 32637195 A JP32637195 A JP 32637195A JP H09141283 A JPH09141283 A JP H09141283A
Authority
JP
Japan
Prior art keywords
liquid
contaminated
contaminated liquid
tank
purification
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP7326371A
Other languages
Japanese (ja)
Inventor
Kazuo Kobayashi
和夫 小林
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.)
Brother Industries Ltd
Original Assignee
Brother Industries 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 Brother Industries Ltd filed Critical Brother Industries Ltd
Priority to JP7326371A priority Critical patent/JPH09141283A/en
Publication of JPH09141283A publication Critical patent/JPH09141283A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/467Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
    • C02F1/4672Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/42Nature of the water, waste water, sewage or sludge to be treated from bathing facilities, e.g. swimming pools
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Filtration Of Liquid (AREA)
  • Details Of Fluid Heaters (AREA)
  • Biological Treatment Of Waste Water (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a lightweight circulation purifying device capable of preventing the deterioration of decomposition action caused by the deposition of a decomposition product on a base material on which microorganisms decomposing organic materials are fixed and purifying a contaminated liquid even just after the device is newly installed or the base material is cleaned and excellent in handling. SOLUTION: In this circulation purifying device for storing the liquid 12 contaminated with time in a liquid storing means 10 and purifying and sterilizing the liquid 12 at the outside of the storing means 10 while being circulated by a pump 44, a biological puryifying means 40 for decomposing and purifying organic materials contained in the liquid 12 with microorganisms and an electrolyzing means 38 for electrolyzing the liquid 12 to accelerate the oxidation decomposition of the organic materials are provided and the each means 40, 38 is communicatively connected to each other in the circulation passage of the contaminated liquid 12.

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】この発明は汚染液体の循環浄
化装置に関し、更に詳細には、浴槽中の浴用水やプール
中の水の如く、使用により経時的に汚染される液体を循
環させつつ浄化・殺菌するための家庭用・業務用の循環
浄化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 an apparatus for circulating and purifying contaminated liquid, and more particularly, it purifies while circulating a liquid which is contaminated over time, such as bath water in a bathtub or water in a pool.・ It relates to household and commercial circulation purification devices for sterilization.

【0002】[0002]

【従来技術】例えば浴槽に貯留した浴用水は、入浴に伴
って垢や毛髪等の有機物その他埃や砂等が不可避的に混
入して経時的に汚染され、濁りや臭いその他ヌメリ等を
生じて入浴時の快適性が損なわれることが一般に知られ
ている。またプールにおいても事情は全く同じであっ
て、使用に伴いプール中の貯留水は経時的に汚染されて
水泳時の快適性を損なうと共に非衛生となる難点を有し
ている。この場合に、浴槽やプールの貯留水を使用の度
毎に新たな水に張り換えれば、前述した問題は生ずるこ
とがなく理想的であるが、水道水の使用コストや温湯に
沸かす際のコスト(例えば温水プールの場合)が嵩むと共
に水交換の手間が掛かり、また何時でも入浴や入泳を楽
しむことができない、等の諸欠点があった。
2. Description of the Related Art For example, bath water stored in a bathtub is unavoidably contaminated with dust, sand, and other organic substances such as dirt and hair during bathing, and is contaminated over time, resulting in turbidity, odor, and other sliminess. It is generally known that comfort during bathing is impaired. In addition, the situation is exactly the same in the pool as well, and with use, the stored water in the pool is contaminated over time, which impairs comfort during swimming and is unsanitary. In this case, if the stored water in the bathtub or pool is replaced with new water each time it is used, the problems described above will not occur, which is ideal, but the cost of using tap water and the cost of boiling it in hot water There are various drawbacks, such as the fact that (for example, in the case of a warm water pool) becomes bulky, it takes time to exchange water, and that it is impossible to enjoy bathing or swimming at any time.

【0003】このような問題に対する1つの解決提案と
して、一般に「24時間風呂」と称される風呂用の循環浄
化装置が知られている。この装置は、殊に家庭内での使
用を企図したもので、砕石、砂利その他粒状セラミック
の如き集合性基材に有用微生物を繁殖させたカートリッ
ジを内蔵し、浴用水を該カートリッジ中に強制的に循環
させ得るようになっている。また循環装置と浴槽との連
通路中に、例えばスポンジを材質とするフィルタが配設
されている。使用の際は、該装置に内蔵した循環ポンプ
を駆動して浴槽中の浴用水を吸引し、前記スポンジフィ
ルタで浴用水に混入している毛髪や糸屑等の大きなゴミ
を捕集・濾過する。次いで予備濾過された浴用水を前記
カートリッジに通過させ、ここで該浴用水中の垢や体脂
等の有機物を微生物で分解して、許容値以下まで清浄化
するようになっている。
As one solution proposal for such a problem, a circulation purification device for a bath generally known as a "24-hour bath" is known. This device is intended especially for domestic use and contains a cartridge in which useful microorganisms are propagated on an aggregate substrate such as crushed stone, gravel or other granular ceramic, and bath water is forced into the cartridge. It can be recycled. A filter made of, for example, sponge is provided in the communication path between the circulation device and the bath. At the time of use, the circulating pump incorporated in the device is driven to suck the bath water in the bathtub, and the sponge filter collects and filters large dust such as hair and thread waste mixed in the bath water. . Then, the pre-filtered bath water is passed through the cartridge, where organic substances such as dirt and body fat in the bath water are decomposed by microorganisms to be cleaned up to an allowable value or less.

【0004】[0004]

【発明が解決しようとする課題】しかし前述した従来技
術に係る浄化装置では、浴用水中の有機物を前記集合性
基材に繁殖させた微生物で分解すると、その分解作用に
より生成される微細な汚染物質が該基材の表面に付着す
る。このため微生物での浴用水の浄化を継続すると、前
記汚染物質が基材表面を膜状に覆ってしまい、微生物に
よる分解作用が大幅に低下してしまう難点が指摘され
る。また微生物の分解能力を超えた量や大きさの有機物
に対しては、これを完全に分解し尽くすまでに相当の時
間を要して基材表面に蓄積し、従って浄化能力の劣化や
流量の低下を招いていた。
However, in the above-described purification apparatus according to the prior art, when the organic matter in the bath water is decomposed by the microorganisms propagated on the aggregating base material, fine contaminants produced by the decomposition action. Adhere to the surface of the substrate. For this reason, it is pointed out that if the purification of the bath water with microorganisms is continued, the contaminants cover the surface of the base material in a film form, and the decomposition action of the microorganisms is significantly reduced. In addition, when the amount or size of organic matter exceeds the ability to decompose microorganisms, it takes a considerable amount of time to completely decompose the organic matter, and accumulates on the substrate surface. It was causing a decline.

【0005】また微生物の担体として機能する砕石や砂
利その他粒状セラミック等の集合性基材は、何れも水に
比べてかなり重いために、該基材を充填したカートリッ
ジの内部に浴用水を導入しても流動することがなく、従
って前記基材の表面に付着・堆積した有機物が浴用水の
流入作用で自然に剥落する働きは殆ど期待できない。こ
のため従来の装置では、カートリッジ中の集合性基材に
逆方向から水を強制流入させたり、水と共に空気を吹込
むエアレーションを該基材に施したりして略定期的に洗
浄する必要があった。また該装置からカートリッジを取
出して、内部の集合性基材を機械的に撹拌したり、ユー
ザーが手で撹拌したりする作業も機種によっては必要と
なっている。このように基材を定期洗浄する際には、浴
用水の連続浄化は中断されて入浴不能となり、また殆ど
の場合に浴槽から浴用水をかなり捨てざるを得ず、水の
節減およびコスト低減の見地からも大きな問題となって
いる。更に、微生物を繁殖させた集合性基材で浴用水を
充分に浄化するためには、該基材が水と接触する面積を
極力確保することが必要であり、従って相当量の基材を
用意することが望ましい。しかし該基材を構成する砕石
や砂利その他粒状セラミック等はかなり重いので、浄化
装置自体の重量も嵩んでしまい、取扱いに不便となる欠
点を有していた。
In addition, since aggregate base materials such as crushed stone, gravel and other granular ceramics, which function as a carrier for microorganisms, are considerably heavier than water, bath water is introduced into the cartridge filled with the base materials. However, it does not flow, and therefore, it is hardly expected that the organic substances adhered / deposited on the surface of the base material will be naturally peeled off by the inflow action of the bath water. For this reason, in the conventional device, it is necessary to wash water substantially forcibly by injecting water into the collective base material in the cartridge from the opposite direction or by aerating the base material with air. It was Further, depending on the model, it is also necessary to take out the cartridge from the apparatus and mechanically agitate the collective base material inside or the user manually agitate. In this way, when the base material is regularly cleaned, continuous purification of bath water is interrupted and bathing becomes impossible, and in most cases, the bath water has to be considerably discarded from the bath, which saves water and reduces costs. From a viewpoint, it is a big problem. Further, in order to sufficiently purify the bath water with the collective base material in which the microorganisms are propagated, it is necessary to secure the area where the base material comes into contact with water as much as possible, and therefore a considerable amount of base material is prepared. It is desirable to do. However, since the crushed stone, gravel, and other granular ceramics, etc. constituting the base material are considerably heavy, there is a drawback that the weight of the purifying device itself becomes heavy, which makes it inconvenient to handle.

【0006】また微生物が有機物に対して充分な分解力
を発揮するには、基材表面に微生物が適度に繁殖してい
ることが必要である。しかし前述した粒状セラミックに
代表される集合性基材は、内部に微生物を予め固定させ
ておくのが困難であるので、浄化装置を設置した後に浴
用水を循環させ、該浴用水に生息する微生物が基材表面
で自然に繁殖し定着するのを待たなければならない。更
に集合性基材を定期的に洗浄したときは、該基材に既に
繁殖・定着している微生物を必要以上に除去してしまい
かねない。微生物の繁殖および安定した定着には一般に
数日から数週間を要し、この間は微生物による浴用水の
浄化は殆ど期待できない。このため浄化装置を浴槽に新
設した後や、カートリッジ中の集合性基材を洗浄した後
は、浴用水の浄化作用は機能していないので水の汚れが
進行し、不快な濁りや臭いその他ヌメリ等を生ずる不都
合があった。そこで装置の新設後や基材の洗浄後は、微
生物による浄化が好適に行なわれるまで入浴を控えなけ
ればならず、更に微生物が該基材に安定的に繁殖するま
で浴用水を数回に亘って張り換える手間を要し、水使用
量が増大してコストも嵩む等の難点があった。
Further, in order for the microorganisms to exert a sufficient decomposing power for organic substances, it is necessary that the microorganisms are properly propagated on the surface of the base material. However, since it is difficult to immobilize microorganisms in advance in the collective substrate typified by the above-mentioned granular ceramics, the bath water is circulated after the purification device is installed, and the microorganisms living in the bath water are circulated. It has to wait for the spores to naturally propagate and settle on the substrate surface. Further, when the collective substrate is washed regularly, the microorganisms already propagated and fixed on the substrate may be removed more than necessary. Propagation of microorganisms and stable colonization generally take several days to several weeks, during which purification of bath water by microorganisms can hardly be expected. For this reason, after the cleaning device is newly installed in the bathtub or after cleaning the collective base material in the cartridge, the cleaning function of the bath water does not work, and water stains progress, causing unpleasant turbidity and odor. There was an inconvenience that caused such problems. Therefore, after new equipment is installed or after cleaning the base material, it is necessary to refrain from bathing until the microbes are properly purified, and bath water is used several times until the microbes are stably propagated on the base material. There is a problem in that it takes time and labor to re-install, the amount of water used increases, and the cost increases.

【0007】[0007]

【発明の目的】この発明は、前述した従来技術に係る汚
染液体の浄化装置に内在している課題を好適に解決する
べく提案されたものであって、有機物を分解する微生物
が定着する基材に分解生成物が堆積して分解作用が低下
するのを防止し、また装置の新設直後や基材の洗浄直後
であっても汚染液体を好適に浄化可能で、しかも軽量か
つ取扱い性の良好な循環浄化装置を提供することを目的
とする。
SUMMARY OF THE INVENTION The present invention has been proposed in order to suitably solve the problems inherent in the above-described conventional apparatus for purifying contaminated liquids, and is a base material on which microorganisms that decompose organic substances are fixed. It prevents degradation products from deteriorating due to the accumulation of decomposition products, and can clean the contaminated liquid appropriately even immediately after the installation of a new device or immediately after cleaning the substrate, and it is lightweight and easy to handle. An object is to provide a circulation purification device.

【0008】[0008]

【課題を解決するための手段】前記課題を克服し、所期
の目的を好適に達成するため本発明は、経時的に汚染さ
れる液体を液体貯留手段に貯留し、この汚染液体を該貯
留手段の外部でポンプ循環させつつ浄化および殺菌を行
なうようにした汚染液体の循環浄化装置において、前記
汚染液体に含まれる有機物を微生物により分解して浄化
する微生物浄化手段と、この汚染液体を電気分解して前
記有機物の酸化分解を促進する電解手段とを備え、これ
らの各手段を前記汚染液体の循環経路中で連通接続した
ことを特徴としている。
In order to overcome the above-mentioned problems and preferably achieve the intended purpose, the present invention stores a liquid contaminated with time in a liquid storage means and stores the contaminated liquid. In a circulation purification device for polluted liquids, which is purified and sterilized while being circulated by a pump outside the means, a microbial purification means for decomposing and purifying organic substances contained in the polluted liquid by microorganisms, and electrolysis of this polluted liquid And an electrolytic means for accelerating the oxidative decomposition of the organic matter, and each of these means is connected in a circulating path of the contaminated liquid.

【0009】同じく前記課題を克服し、所期の目的を好
適に達成するために本願の別の発明は、経時的に汚染さ
れる液体を液体貯留槽に貯留し、この汚染液体を該貯留
槽の外部でポンプ循環させつつ浄化および殺菌を行なう
ようにした汚染液体の循環浄化装置において、前記汚染
液体に含まれる有機物を吸着・分解して浄化する微生物
を存在させた粒状の合成高分子ゲルを充填してなる微生
物浄化槽と、この汚染液体を電気分解して前記有機物の
酸化分解を促進する電解槽とを備え、これらの各槽を前
記汚染液体の循環経路中で連通接続したことを特徴とし
ている。
Similarly, in order to overcome the above-mentioned problems and suitably achieve the intended purpose, another invention of the present application is to store a liquid contaminated with time in a liquid storage tank, and store the contaminated liquid in the storage tank. In a circulation purification device for polluted liquids, which is purified and sterilized while being pumped and circulated outside the pump, a granular synthetic polymer gel containing microorganisms that adsorbs and decomposes organic substances contained in the polluted liquids and purifies them. A microbial septic tank filled and an electrolytic cell for accelerating the oxidative decomposition of the organic matter by electrolyzing the contaminated liquid are provided, and each of these tanks is connected in a circulating path of the contaminated liquid. There is.

【0010】[0010]

【発明の実施の形態】次に、本発明に係る汚染液体の循
環浄化装置につき、好適な実施例を挙げて、添付図面を
参照しながら以下説明する。なお実施例として、家庭用
の浴槽に設ける循環浄化装置につき説明するが、これ以
外に屋外用プールや屋内用の温水プールにも好適に使用
し得ることは勿論である。
BEST MODE FOR CARRYING OUT THE INVENTION Next, a circulating liquid purification apparatus for a contaminated liquid according to the present invention will be described below with reference to the accompanying drawings with reference to preferred embodiments. It should be noted that although a circulation purifying apparatus provided in a domestic bathtub will be described as an example, it is needless to say that it can be suitably used for an outdoor pool and an indoor warm water pool.

【0011】(循環浄化装置の全体構造について)図1
は、本発明の一実施例に係る循環浄化装置の概略構成を
示し、この装置は浴槽10に貯留されて経時的に汚染さ
れる浴用水12を、該浴槽10の外部でポンプ循環させ
つつ浄化および殺菌を行なうものである。すなわち実施
例に係る循環浄化装置は、図5に示す如く、浴槽10に
着脱自在に配設される給排水ユニット14と、該ユニッ
ト14に吸水ホース16および排水ホース18を介して
接続する装置本体20とから基本的に構成されている。
この装置本体20は、例えば浴槽10の縁部に設置さ
れ、漏電ブレーカ22およびケーブル24を介して電源
供給がなされると共に、アースケーブル26で確実にア
ースされて漏電や感電に対する万全の保護が図られてい
る。給排水ユニット14は、図6に関して後述する如
く、一例として吸盤28により浴槽10の内壁面に着脱
自在に取付けられ、浴用水12の一般的な貯留レベルよ
り下方に位置している。
(Regarding Overall Structure of Circulation Purification Device) FIG.
1 shows a schematic configuration of a circulation purification apparatus according to an embodiment of the present invention, which purifies bath water 12 stored in a bath 10 and contaminated with time while pumping circulation of the bath water 12 outside the bath 10. And sterilization. That is, as shown in FIG. 5, the circulation purification device according to the embodiment has a water supply / drainage unit 14 detachably arranged in the bathtub 10, and a device body 20 connected to the unit 14 via a water absorption hose 16 and a drain hose 18. It is basically composed of and.
This device body 20 is installed, for example, at the edge of the bathtub 10 and is supplied with power via an earth leakage breaker 22 and a cable 24, and is surely grounded by an earth cable 26 to ensure complete protection against earth leakage and electric shock. Has been. As will be described later with reference to FIG. 6, the water supply / drainage unit 14 is detachably attached to the inner wall surface of the bathtub 10 by a suction cup 28, for example, and is located below a general storage level of the bath water 12.

【0012】図5および図6に示す給排水ユニット14
は、例えば長方形の箱状ケーシング30からなり、該ケ
ーシング30の前面に上下の関係で浴用水を吸い出す吸
水口32および浄化後の浴用水を浴槽10に戻す吐出口
34が開設されている。また箱状ケース30の裏面には
前記吸盤28が配設され、給排水ユニット14を浴槽1
0の内壁面に取付け得るようになっている。前記吸水口
32は吸水ホース16を介して装置本体20に連通接続
すると共に、その開口部に例えばスポンジを材質とする
フィルタ36が着脱可能に設けられ、浴用水に混入して
いる大きめのゴミや毛髪その他の異物を捕集除去し得る
ようになっている。また前記吐出口34は、排水ホース
18を介して装置本体20に連通接続している。なお吸
水口32と吐出口34は、給排水ユニット14を浴槽1
0の内壁面に取付けた際に浴用水にそっくり浸漬される
ものである。そして、後述する循環浄化装置を稼働させ
た際に浴槽10中の浴用水は、循環ポンプの作用下に吸
水口32および吸水ホース16を介して装置本体20に
流入し、ここで浄化および殺菌された後に、排水ホース
18および吐出口34を介して前記浴槽10へ戻るサイ
クルを反復する。
The water supply / drainage unit 14 shown in FIGS. 5 and 6.
Is composed of, for example, a rectangular box-shaped casing 30, and a water suction port 32 for sucking bath water in a vertical relationship and a discharge port 34 for returning the purified bath water to the bath 10 are provided on the front surface of the casing 30. Further, the suction cup 28 is arranged on the back surface of the box-shaped case 30, and the water supply / drainage unit 14 is attached to the bathtub 1.
It can be attached to the inner wall surface of 0. The water suction port 32 is connected to the apparatus main body 20 through a water suction hose 16 and a filter 36 made of, for example, a sponge material is detachably provided at the opening of the water suction port 32 to remove large dusts mixed in the bath water. It is designed to collect and remove hair and other foreign matter. Further, the discharge port 34 is communicatively connected to the apparatus body 20 via the drain hose 18. The water inlet 32 and the outlet 34 connect the water supply / drainage unit 14 to the bathtub 1.
When it is attached to the inner wall surface of No. 0, it is completely immersed in bath water. Then, when the circulation purification device described later is operated, the bath water in the bathtub 10 flows into the device body 20 through the water suction port 32 and the water suction hose 16 under the action of the circulation pump, and is purified and sterilized there. After that, the cycle of returning to the bath 10 through the drain hose 18 and the discharge port 34 is repeated.

【0013】循環浄化装置における装置本体20は、図
1に示す如く、経時的に汚染する浴用水12を電気分解
して、該浴用水に含まれる垢等の有機物の酸化分解を促
進する電解槽38と、該浴用水12に含まれる有機物を
微生物により吸着・分解して浄化する微生物浄化槽40
とを備え、これら各槽は浴用水12が循環される管路を
介して連通接続されている。すなわち給排水ユニット1
4に設けた吸水ホース16は、浴用水の循環ポンプ44
を介して電解槽38の入口側に接続し、この電解槽38
の出口側は、管路46を介して微生物浄化槽40の入口
側に接続している。また微生物浄化槽40の出口側は、
管路48を介して浴用水を加熱昇温させる電気加熱槽5
0の入口側に接続し、この電気加熱槽50の出口側は、
管路52を介して前記排水ホース18に接続している。
なお浄化・殺菌後の浴用水が浴槽10に帰還する管路5
2には、該浴用水の流量を検出する流量センサ56が介
挿され、また電気加熱槽50の入口側に接続する管路4
8には、浴用水の温度を検出する温度センサ58が介挿
されている。更に電気加熱槽50の内部には、槽内の水
位を監視する水位センサ60が配設されている。これら
各センサは、図8の制御ブロックに示す制御回路62に
接続して、装置本体20の各種制御に必要な情報を該回
路62へ入力するようになっている。
As shown in FIG. 1, the apparatus body 20 of the circulation purification apparatus is an electrolytic cell for electrolyzing the bath water 12 which is contaminated with time, and promoting the oxidative decomposition of organic matter such as dust contained in the bath water 12. 38, and a microbial septic tank 40 for adsorbing and decomposing organic substances contained in the bath water 12 with microorganisms for purification
And each of these tanks are connected to each other via a pipe through which the bath water 12 is circulated. That is, the water supply / drainage unit 1
The water-absorbing hose 16 provided in No. 4 is a circulation pump 44 for bath water.
Is connected to the inlet side of the electrolytic cell 38 via
The outlet side of is connected to the inlet side of the microbial septic tank 40 via a pipe line 46. The outlet side of the microbial septic tank 40 is
Electric heating tank 5 for heating and raising the temperature of bath water via a pipe 48
0 is connected to the inlet side, and the outlet side of the electric heating tank 50 is
It is connected to the drain hose 18 via a pipe line 52.
In addition, the pipe 5 through which the bath water after purification and sterilization returns to the bathtub 10.
2, a flow rate sensor 56 for detecting the flow rate of the bath water is inserted, and a pipeline 4 connected to the inlet side of the electric heating tank 50.
A temperature sensor 58 for detecting the temperature of the bath water is inserted in FIG. Further, inside the electric heating tank 50, a water level sensor 60 for monitoring the water level in the tank is provided. Each of these sensors is connected to the control circuit 62 shown in the control block of FIG. 8 to input information necessary for various controls of the apparatus main body 20 to the circuit 62.

【0014】(電解槽について)電解槽38は、例えば図
4に示す如く、直立配置した箱型ケーシング64と、該
ケーシング内部に所要の間隔で配設した2つの電極部6
6,68とからなり、これに印加される直流電圧の極性
を選択することにより、一方の電極部66を陽極として
機能させると共に、他方の電極部68を陰極として機能
させ得るようになっている。また陽極66の材料として
は、アルミニウム、ステンレス、フェライト、白金、白
金被覆のチタン(Ti)等が好適に用いられ、陰極68に
は、アルミニウム、白金、白金被覆の(Ti)等が好適に
用いられる。これら電極材料の内でステンレスやアルミ
ニウムは、電気分解により材料自体が浴用水に溶出する
傾向を有する。この場合は、浴用水に溶出した金属イオ
ンを核として該浴用水中の有機物が凝集されるので、後
の行程での有機物の分解を容易にする働きが期待でき
る。本実施例では、陽極66および陰極68の双方に白
金被覆のチタン(Ti)が使用されている。なおケーシン
グ64は円筒状に構成してもよいし、また該ケーシング
64を一方の電極とするようにしてもよい。更に電極の
数も、複数対とする必要はなく、奇数本の配列とするよ
うにしてもよい。
(About Electrolyzer) As shown in FIG. 4, for example, the electrolyzer 38 includes an upright box-shaped casing 64 and two electrode portions 6 disposed inside the casing at a required interval.
6, 68, and by selecting the polarity of the DC voltage applied thereto, one electrode portion 66 can function as an anode and the other electrode portion 68 can function as a cathode. . As the material of the anode 66, aluminum, stainless steel, ferrite, platinum, platinum-coated titanium (Ti) or the like is preferably used, and as the cathode 68, aluminum, platinum, platinum-coated (Ti) or the like is preferably used. To be Among these electrode materials, stainless steel and aluminum tend to be eluted into the bath water by electrolysis. In this case, since the organic substances in the bath water are aggregated with the metal ions eluted in the bath water as nuclei, it can be expected that the organic substances can be easily decomposed in the subsequent process. In this embodiment, platinum-coated titanium (Ti) is used for both the anode 66 and the cathode 68. The casing 64 may have a cylindrical shape, or the casing 64 may serve as one of the electrodes. Furthermore, the number of electrodes does not have to be a plurality of pairs, and may be an odd number array.

【0015】(微生物浄化槽について)微生物浄化槽40
は、浴用水12に含まれる有機物を微生物の分解作用に
より吸着・分解して浄化するもので、本実施例では微生
物の担体として合成高分子ゲルが好適に使用される。こ
の合成高分子ゲルとしては、優れた耐水性と弾性および
柔軟性を有し、しかも高い含水性を有する粒状のポリビ
ニールアルコール(以下「PVA」という)ゲルが好適に用
いられる。例えば図3に示す如く、微生物浄化槽40
は、直立配置される円筒状ケーシング70と、該ケーシ
ング70の内部に配設され中心軸線に沿って延在する管
状の水流路72と、該ケーシング70の底部に開設した
流入口70aおよび流出口70bと、該ケーシング70
の内部に充填した所要量のPVAゲル74とから基本的
に構成される。前記流入口70aと流出口70bには、
粒状をなすPVAゲル74の外部流出を阻止するメッシ
ュ寸法に設定したフイルタ76が配設されている。従っ
て流入口70aを介してケーシング70に流入した浴用
水は、中心に位置する管状水流路72を上昇した後に反
転し、環状をなす水滞留部78を下降して流出口70b
から流出するものである。
(About microbiological septic tank) Microbiological septic tank 40
Is for adsorbing and decomposing and purifying the organic matter contained in the bath water 12 by the decomposing action of microorganisms, and in this embodiment, a synthetic polymer gel is preferably used as a carrier for microorganisms. As the synthetic polymer gel, granular polyvinyl alcohol (hereinafter referred to as "PVA") gel having excellent water resistance, elasticity and flexibility and having high water content is preferably used. For example, as shown in FIG.
Is an upright cylindrical casing 70, a tubular water channel 72 disposed inside the casing 70 and extending along a central axis, an inflow port 70a and an outflow port opened at the bottom of the casing 70. 70b and the casing 70
It is basically composed of a required amount of PVA gel 74 filled inside. The inlet 70a and the outlet 70b are
A filter 76 having a mesh size that prevents the granular PVA gel 74 from flowing out is provided. Therefore, the bath water that has flowed into the casing 70 through the inflow port 70a reverses after rising in the centrally located tubular water flow path 72 and descending the annular water retention portion 78, and then outflow port 70b.
It is something that flows out from.

【0016】前記PVAゲル74としては、浴用水に含
まれる垢や体脂等の有機物を分解する有用微生物を、予
め内包するように包括固定処理されているものを使用す
るのが望ましい。この種の有用微生物として、例えばシ
ュードモナス(Pseudomonas)属、アスペルギルス(Asperg
illus)属、サッカロマイセス(Saccharomycetes)属の如
き微生物や酵素、その他排水処理に用いられる活性汚
泥、硝化菌、脱窒菌等が挙げられる。このような有用微
生物がPVAゲル74に包括固定処理されていることに
よって、装置を使い始めた時点から直ちに微生物による
有機物の分解が行なわれる。PVAゲル74の夫々は直
径数mm程度の粒状をなし、該PVAゲル74は前記ケ
ーシング70の略20%〜50%程度を占める分量とな
るよう充填されている。すなわち、PVAゲル74の充
填量をこの程度に調節することにより、前記ケーシング
70に流入した浴用水は該PVAゲル74を自由に流動
させ得るので、微生物で分解した後に生成される残渣物
がPVAゲル74の表面に付着する不都合が回避され
る。なおPVAゲル74として、微生物の包括固定処理
がなされていないゲルを用いる場合は、微生物が自然に
PVAゲル74に着床して繁殖するのを待つことにな
る。
As the PVA gel 74, it is desirable to use a PVA gel that has been entrapped and fixed in advance so as to include useful microorganisms that decompose organic substances such as dirt and body fat contained in bath water. Examples of useful microorganisms of this kind include Pseudomonas spp., Aspergillus spp.
illus) and Saccharomycetes, microorganisms and enzymes, and other activated sludge used for wastewater treatment, nitrifying bacteria, denitrifying bacteria and the like. By comprehensively immobilizing such useful microorganisms on the PVA gel 74, the organic substances are decomposed by the microorganisms immediately after the start of using the apparatus. Each of the PVA gels 74 is in the form of particles having a diameter of about several mm, and the PVA gels 74 are filled so as to occupy about 20% to 50% of the casing 70. That is, by adjusting the filling amount of the PVA gel 74 to this extent, the bath water flowing into the casing 70 can freely flow the PVA gel 74, so that the residue produced after being decomposed by microorganisms is PVA. The disadvantage of adhering to the surface of the gel 74 is avoided. When a gel that has not been subjected to entrapping immobilization of microorganisms is used as the PVA gel 74, it waits for the microorganisms to naturally land on the PVA gel 74 and propagate.

【0017】(電気加熱槽について)電気加熱槽50は内
部に電熱ヒータ92を備え、前記循環ポンプ44で該加
熱槽50に供給される浴用水は、該ヒータ92により適
切温度にまで昇温される。電気加熱槽50における浴用
水の水位は、これに設けた前記水位センサ60により監
視され、基準水位に達していない場合は、図8に示すデ
ィスプレイ94にエラー表示を行なって前記ポンプ44
の運転を停止させる。また電気加熱槽50へ供給される
浴用水の温度は、加熱槽50の流入側管路48に介挿し
た前記温度センサ58で監視し、該センサ58の検出結
果に基づき電熱ヒータ92をオン・オフして浴用水を入
浴に適した温度に維持する。更に、浴用水が循環されて
いるか否かは、電気加熱槽50の下流側に連通する管路
52に介挿した前記流量センサ56により監視される。
なお本発明に係る循環浄化装置を、図示例の浴槽や温水
プールに設置する場合は電気加熱槽50は必須となる
が、通常のプール等に設置される循環浄化装置に関して
は、該電気加熱槽50を設ける必要はない。
(About Electric Heating Tank) The electric heating tank 50 has an electric heater 92 therein, and the bath water supplied to the heating tank 50 by the circulation pump 44 is heated to an appropriate temperature by the heater 92. It The water level of the bath water in the electric heating tank 50 is monitored by the water level sensor 60 provided therein, and if the reference water level is not reached, an error is displayed on the display 94 shown in FIG.
Stop driving. The temperature of the bath water supplied to the electric heating tank 50 is monitored by the temperature sensor 58 inserted in the inflow side conduit 48 of the heating tank 50, and the electric heater 92 is turned on based on the detection result of the sensor 58. Turn off to maintain bath water at temperature suitable for bathing. Further, whether or not the bath water is circulated is monitored by the flow rate sensor 56 inserted in the pipe line 52 communicating with the downstream side of the electric heating tank 50.
Note that the electric heating tank 50 is indispensable when the circulation purification device according to the present invention is installed in the bathtub or the hot water pool of the illustrated example, but regarding the circulation purification device installed in a normal pool or the like, the electric heating tank is used. It is not necessary to provide 50.

【0018】(オゾナイザについて)前述した電解槽3
8,微生物浄化槽40および電気加熱槽50を連通接続
する管路系中に、図8に示すオゾナイザ96を別途介挿
するようにしてもよい。後述するように、電解槽38で
浴用水を電気分解する際にもオゾンが発生し殺菌作用が
果たされるが、更にオゾナイザ96を別途用いることに
よって一層確実に殺菌を行なうことができる。オゾナイ
ザ96の配設個所は、浴用水が循環する管路内であれば
よいが、微生物浄化槽40の内部に生息している微生物
の働きを阻害しない位置に配設することが望ましい。な
お、浴用水の循環管路とオゾナイザ96は、図8に示す
ソレノイド弁99を介して接続され、該ソレノイド弁9
9の開放により管路中の浴用水にオゾンの注入がなさ
れ、またソレノイド弁99の閉成により浴用水へのオゾ
ン注入が停止される。
(Regarding the ozonizer) The electrolytic cell 3 described above
8. The ozonizer 96 shown in FIG. 8 may be separately inserted in the pipeline system that connects the microbial purification tank 40 and the electric heating tank 50 to each other. As will be described later, ozone is also generated when the bath water is electrolyzed in the electrolytic bath 38, and the sterilizing action is achieved. However, by additionally using the ozonizer 96, sterilization can be performed more reliably. The location of the ozonizer 96 may be in a pipeline through which the bath water circulates, but it is desirable that the ozonizer 96 is disposed at a position that does not inhibit the action of the microorganisms inhabiting the inside of the microorganism purification tank 40. The bath water circulation line and the ozonizer 96 are connected via a solenoid valve 99 shown in FIG.
When 9 is opened, ozone is injected into the bath water in the pipeline, and when the solenoid valve 99 is closed, ozone injection into the bath water is stopped.

【0019】(装置の制御ブロックについて)図8は、本
発明に係る循環浄化装置の電気的構成部分を個別に制御
するブロックを概略的に示し、制御回路62に前述した
流量センサ56,温度センサ58および水位センサ60
が接続されて、夫々の検出情報を該制御回路62に入力
している。またメモリ(RAM)98には、循環浄化装置
を自動的に稼働させるに必要な各種の情報や指令データ
が格納され、制御回路62との間で信号交換がなされる
ようになっている。なお前記ソレノイド弁99の開閉
は、制御回路62から制御指令を受けた弁駆動回路89
により駆動される。同様に前記循環ポンプ44はポンプ
駆動回路45により駆動され、電熱ヒータ92はヒータ
駆動回路93により駆動される。また電解槽38は電解
槽駆動回路39により駆動され、オゾナイザ96はオゾ
ナイザ駆動回路97により駆動され、更にディスプレイ
94はディスプレイ駆動回路95により適時の駆動がな
される。
(Regarding Control Block of Device) FIG. 8 schematically shows a block for individually controlling the electrical components of the circulation purification device according to the present invention, and the flow rate sensor 56 and the temperature sensor described above are included in the control circuit 62. 58 and water level sensor 60
Are connected to input respective detection information to the control circuit 62. The memory (RAM) 98 stores various kinds of information and command data necessary for automatically operating the circulation purification device, and exchanges signals with the control circuit 62. The solenoid valve 99 is opened and closed by a valve drive circuit 89 which receives a control command from the control circuit 62.
Driven by Similarly, the circulation pump 44 is driven by a pump drive circuit 45, and the electric heater 92 is driven by a heater drive circuit 93. The electrolytic cell 38 is driven by the electrolytic cell drive circuit 39, the ozonizer 96 is driven by the ozonizer drive circuit 97, and the display 94 is driven by the display drive circuit 95 in a timely manner.

【0020】(循環浄化装置の作用について)次に、この
ように構成した実施例に係る循環浄化装置の作用を、図
7に示すフローチャートを参照しながら説明する。循環
浄化装置の稼働に先立って前記メモリ(RAM)98に
は、浴用水の温度値の設定、電解槽38での電解の
開始・終了時刻の設定、オゾナイザ96での処理の開
始・終了時刻の設定が予めなされている。前記メモリ
(RAM)に入力されるこれら設定値は、前記ディスプレ
イ94に表示されて、視覚的に容易に確認し得るように
なっている。また浴槽10には、浴用水が所要の湯張り
レベルまで貯留されているものとする。
(Operation of Circulation Purification Device) Next, the operation of the circulation purification device according to the embodiment thus constructed will be described with reference to the flow chart shown in FIG. Prior to the operation of the circulation purification device, the temperature value of the bath water is set in the memory (RAM) 98, the start and end times of electrolysis in the electrolytic bath 38 are set, and the start and end times of the processing in the ozonizer 96 are set. Settings are made in advance. The memory
These set values input to the (RAM) are displayed on the display 94 so that they can be easily visually confirmed. Further, it is assumed that bath water is stored in the bathtub 10 to a required level of filling water.

【0021】図7のステップS1において、循環浄化装
置に備えた運転キー(図示せず)がオン(ON)しているか否
かを確認し、結果が肯定(YES)であれば循環ポンプ44
が駆動され、浴槽10中の浴用水が図1に示す管路系を
循環し始める。そして循環ポンプ44を駆動した状態で
次の操作を待機する。この待機中にステップS2に移行
し、電気加熱槽50の水位が規定値になっているか否か
を確認し、結果が否定(NO)であれば、ディスプレイ94
にエラー表示を行なって、循環ポンプ44の駆動を停止
する。また結果が肯定(YES)であればステップS3に移行
し、管路中を流れる浴用水の流量が規定値に達している
か否かを確認し、結果が否定(NO)であれば、同じくディ
スプレイ94にエラー表示を行なって、循環ポンプ44
の駆動を停止する。また結果が肯定(YES)であれば、次
のステップS4に移行する。なお前記水位センサ60お
よび流量センサ56での確認が肯定(YES)されると、循
環ポンプ44での運転が継続され、浴槽10からの浴用
水は電解槽38,微生物浄化槽40および電気加熱槽5
0の順で循環した後、該浴槽10へ再び帰還するサイク
ルを反復する。この場合における微生物浄化槽40での
分解浄化のプロセスは後述する。
In step S 1 of FIG. 7, it is confirmed whether or not an operation key (not shown) provided in the circulation purification device is turned on (ON), and if the result is affirmative (YES), the circulation pump 44
Is driven, and the bath water in the bath 10 starts to circulate in the pipeline system shown in FIG. Then, the circulating pump 44 is driven and the next operation is awaited. During this standby, the process proceeds to step S 2 to check whether the water level in the electric heating tank 50 has reached the specified value, and if the result is negative (NO), display 94
An error message is displayed on the display and the drive of the circulation pump 44 is stopped. The result goes to step S 3, if affirmative (YES), checks whether the flow rate of the bath water flowing through the conduit in the has reached a prescribed value, if the result is negative (NO), the process also An error is displayed on the display 94, and the circulation pump 44
Stop driving. If the result is affirmative (YES), the process proceeds to the next step S 4 . When the confirmation by the water level sensor 60 and the flow rate sensor 56 is affirmative (YES), the operation of the circulation pump 44 is continued, and the bath water from the bath 10 is electrolyzed by the electrolysis tank 38, the microorganism purification tank 40 and the electric heating tank 5.
After circulating in the order of 0, the cycle of returning to the bathtub 10 again is repeated. The process of decomposition and purification in the microbial septic tank 40 in this case will be described later.

【0022】ステップS4では、電気加熱槽50に流入
する浴用水の温度がメモリ(RAM)98への設定値より
低いか否かを確認し、結果が肯定(YES)であれば、電熱
ヒータ92をオンして該加熱槽50で水温を上昇させ
る。またステップS4での結果が否定(NO)であれば、前
記電熱ヒータ92をオフ(OFF)して次のステップS5に移
行する。このステップS5では、先にメモリ(RAM)9
8に設定した電解槽38での処理時刻になっているか否
かを確認し、結果が否定(NO)であれば、図8に示す電解
槽駆動回路39を引続きオフ(OFF)とし、また結果が肯
定(YES)であれば、電解槽駆動回路39をオン(ON)して
電解槽38の電解作用を開始する。この電解槽38での
電解プロセスは後述する。次にステップS6に移行し
て、オゾナイザ96の処理時刻になっているか否かを確
認する。その結果が否定(NO)であれば、図8に示すオゾ
ナイザ駆動回路97および弁駆動回路89を引続きオフ
(OFF)とし、また結果が肯定(YES)であれば、オゾナイザ
駆動回路97と弁駆動回路89をオン(ON)して管路中の
浴用水へのオゾンの注入を行なう。次いでステップS7
で運転キーがオフ(OFF)されているか否かを確認し、結
果が否定(NO)であれば、先のステップS2に戻って前述
した確認作業を反復する。また該ステップS7での結果
が肯定(YES)であれば、循環ポンプ44の運転を停止す
る。
In step S 4 , it is confirmed whether or not the temperature of the bath water flowing into the electric heating tank 50 is lower than the value set in the memory (RAM) 98. If the result is affirmative (YES), the electric heater Turn on 92 to raise the water temperature in the heating tank 50. If the result of step S 4 is negative (NO), the electric heater 92 is turned off (OFF) and the process proceeds to step S 5 . In this step S 5 , first the memory (RAM) 9
It is confirmed whether the processing time in the electrolytic cell 38 set to 8 is reached, and if the result is negative (NO), the electrolytic cell drive circuit 39 shown in FIG. 8 is continuously turned off (OFF), and the result Is positive (YES), the electrolytic cell drive circuit 39 is turned on (ON) to start the electrolytic action of the electrolytic cell 38. The electrolysis process in this electrolysis tank 38 will be described later. Next, in step S 6 , it is confirmed whether or not the processing time of the ozonizer 96 is reached. If the result is negative (NO), the ozonizer drive circuit 97 and valve drive circuit 89 shown in FIG. 8 are continuously turned off.
If the result is affirmative (YES), the ozonizer drive circuit 97 and the valve drive circuit 89 are turned on (ON) to inject ozone into the bath water in the pipeline. Then step S 7
It is confirmed whether or not the driving key is turned off in step (2), and if the result is negative (NO), the process returns to the previous step S 2 and the above-mentioned confirmation work is repeated. Also if the result at the step S 7 is affirmative (YES), it stops the operation of the circulation pump 44.

【0023】(電解槽でのプロセスについて)図1におい
て浴槽10から吸引された浴用水は、電解槽38に流入
して所要の直流電圧が印加されている陽極66および陰
極68に接触する。このため浴用水は電気分解され、陽
極66の近傍に酸素ガスを生ずると共に、該陽極66の
周囲に存在する浴用水の水素イオン濃度は高くなって酸
性となる。また陰極68の近傍には水素ガスを生ずると
共に、該陰極68の周囲に存在する浴用水の水素イオン
濃度は低くなってアルカリ性となる。しかも陽極66の
側では、浴用水に含まれる垢や体脂のような有機物が酸
化分解されて微小化する。このため次工程に位置する微
生物浄化槽40での微生物による分解が助長される。ま
た、酸化分解された有機物の一部は不溶性となってコロ
ニー状態に凝集する。
(About Process in Electrolyzer) Bath water sucked from the bath 10 in FIG. 1 flows into the electrolyzer 38 and comes into contact with the anode 66 and the cathode 68 to which a required DC voltage is applied. Therefore, the bath water is electrolyzed to generate oxygen gas in the vicinity of the anode 66, and the hydrogen ion concentration of the bath water existing around the anode 66 becomes high and becomes acidic. Further, hydrogen gas is generated in the vicinity of the cathode 68, and the concentration of hydrogen ions in the bath water existing around the cathode 68 is lowered to become alkaline. Moreover, on the side of the anode 66, organic substances such as dirt and body fat contained in the bath water are oxidatively decomposed and become minute. Therefore, decomposition by microorganisms in the microbial septic tank 40 located in the next step is promoted. In addition, a part of the oxidatively decomposed organic matter becomes insoluble and aggregates in a colony state.

【0024】更に陽極66の近傍には、オゾン(O3)や
過酸化水素(H22)の形で活性酸素が生成される。この
ため浴用水中の雑菌は、この活性酸素により相当の程度
殺菌されるに至る。更に電気分解により前記陽極66の
近傍は強酸性になり、また前記陰極68の近傍は強アル
カリ性になるので、このような水素イオン濃度(pH)の
変化によっても殺菌効果が発揮される。なお、陽極66
の近傍に生ずる酸素ガスおよび酸性化した水と、陰極6
8の近傍に生ずる水素ガスおよびアルカリ性化した水は
明確な分離状態で存在するものでなく、浴用水中に気水
が混在した状態で存在するものである。この電解分解に
より一部殺菌がなされ、かつ微細化した有機物を凝集さ
せた浴用水は、電解槽38から下流側の管路46を経て
微生物浄化槽40に供給される。
Further, in the vicinity of the anode 66, active oxygen is produced in the form of ozone (O 3 ) or hydrogen peroxide (H 2 O 2 ). Therefore, various bacteria in the bath water are sterilized to a considerable extent by this active oxygen. Furthermore, since the vicinity of the anode 66 becomes strongly acidic and the vicinity of the cathode 68 becomes strongly alkaline due to electrolysis, the sterilizing effect is exhibited even by such a change in the hydrogen ion concentration (pH). The anode 66
Oxygen gas and acidified water generated in the vicinity of the
Hydrogen gas and alkalized water generated in the vicinity of 8 do not exist in a clearly separated state, but exist in a state where steam water is mixed in the bath water. The bath water, which is partially sterilized by this electrolytic decomposition and in which finely divided organic substances are aggregated, is supplied from the electrolytic cell 38 to the microbial purification tank 40 via the downstream pipe line 46.

【0025】ところで電解槽38で電気分解を行なう
と、前述したアルカリ性水の生成により陰極68の近傍
のpH値が上昇し、浴用水に含まれるカルシウムイオン
やマグネシウムイオンが該陰極68の表面に析出する。
このように陰極68の表面がこれら析出物により層状に
被覆されると、結果的に電解作用が次第に低下する不都
合を来す。そこで本実施例では、電気分解を開始した後
の電解槽38への通水量を流量センサ56で積算計測
し、その計測値が前記メモリ(RAM)に予め設定してお
いた通水量に達すると、陰極68および陽極66に逆極
性の直流電圧を印加し、該陰極68を被覆していた析出
物を溶解させることにより清浄化を行なっている。なお
浴用水の通水量の積算に代えて、通水時間の積算を電極
における極性変換の関数として採用してもよい。
When electrolysis is carried out in the electrolytic cell 38, the pH value in the vicinity of the cathode 68 rises due to the generation of the alkaline water described above, and calcium ions and magnesium ions contained in the bath water are deposited on the surface of the cathode 68. To do.
When the surface of the cathode 68 is coated with these deposits in a layered manner as described above, there is a disadvantage that the electrolytic action is gradually reduced. Therefore, in the present embodiment, the amount of water flowing into the electrolytic cell 38 after the start of electrolysis is integrated and measured by the flow rate sensor 56, and when the measured value reaches the amount of water flowing preset in the memory (RAM). Cleaning is performed by applying a DC voltage of opposite polarity to the cathode 68 and the anode 66, and dissolving the deposit covering the cathode 68. It should be noted that instead of integrating the water flow rate of the bath water, the water flow time may be integrated as a function of polarity conversion in the electrodes.

【0026】(微生物浄化槽でのプロセスについて)先に
述べた如く微生物浄化槽40には、予めバクテリア等の
微生物を繁殖固定させたPVAゲル74が、浴用水の流
入により自由流動し得る程度の分量で充填されている。
従って、上流側の電解槽38から浴用水が管路46を経
て微生物浄化槽40に供給されると、図3に示す如く、
前記PVAゲル74は浴用水の流勢により翻弄され激し
く流動する。使用により汚染された浴用水がPVAゲル
74に接触すると、これに繁殖固定させた微生物は水中
の垢や体脂等の有機物を分解して汚泥状の汚染残査とす
る。なお本実施例で、微生物浄化槽40に供給される浴
用水は、上流側の電解槽38での電気分解を経ているた
めにかなり微細化しており、従って微生物による分解作
用が効果的に促進される。また分解により発生した汚泥
状の汚染残査は、前記PVAゲル74に膜状に付着しよ
うとするが、該PVAゲル74は槽中で激しく流動して
いるので付着が極めて困難となる。仮に該汚染物質がP
VAゲル74に付着しても、該PVAゲルの流動により
容易に剥落させられてしまう。従ってPVAゲル74は
目詰まりを生ずることがなく、これらPVAゲル74に
対する洗浄処理や交換等の定期的なメンテナンスは不要
となる。また、PVAゲル74が激しく流動するため
に、微生物浄化槽40に供給される浴用水に対する実効
接触面積を大きく確保でき、浴用水に対し充分な浄化力
を発揮し得る等の利点がある。
(Regarding Process in Microbial Septic Tank) As described above, in the microbial septic tank 40, the PVA gel 74 in which microorganisms such as bacteria have been propagated and fixed in advance is provided in an amount such that the PVA gel 74 can freely flow due to the inflow of bath water. It is filled.
Therefore, when bath water is supplied from the upstream electrolyzer 38 to the microbial septic tank 40 via the pipe line 46, as shown in FIG.
The PVA gel 74 is violently fluidized by being swirled by the flow of bath water. When the bath water contaminated by use comes into contact with the PVA gel 74, the microorganisms propagated and fixed on the PVA gel 74 decompose organic matter such as dirt and body fat in the water to produce sludge-like contaminated residue. In the present embodiment, the bath water supplied to the microbial septic tank 40 is considerably fined because it has undergone electrolysis in the upstream electrolyzer 38, and therefore the decomposition action by the microorganisms is effectively promoted. . Further, the sludge-like contamination residue generated by the decomposition tends to adhere to the PVA gel 74 in a film form, but the PVA gel 74 is violently flowing in the tank, so that the adhesion becomes extremely difficult. If the pollutant is P
Even if it adheres to the VA gel 74, it is easily peeled off due to the flow of the PVA gel. Therefore, the PVA gel 74 does not become clogged, and periodical maintenance such as cleaning processing and replacement of these PVA gels 74 becomes unnecessary. Further, since the PVA gel 74 flows violently, it is possible to secure a large effective contact area for the bath water supplied to the microbial septic tank 40, and it is possible to exert a sufficient purification power for the bath water.

【0027】更にPVAゲル74の成分の一部は浴用水
に溶出する傾向を示すが、この溶出した成分は水中の有
機物の一部に対し凝集剤として機能し、該有機物の一部
を凝集させるに至る。そして部分的に凝集した有機物
は、微生物によっても分解されなかった有機物や、分解
により発生した汚泥状の汚染残査と共に浴用水に分散さ
れて混在する。なお本実施例では、PVAゲル74の内
部に微生物が包括固定処理されたものを用いたために、
微生物浄化槽40に充填したPVAゲル74に微生物が
繁殖するのを待つ必要はなく、使い始めから微生物によ
る有機物の浄化能力が充分に発揮される。すなわち循環
浄化装置を設置した当初から充分に有機物の分解作用が
行なわれ、浴用水が始めのうちひどく濁ったり、またヌ
メリを生じたりすることなく、清浄な浴用水での入浴を
楽しみ得るものである。但し、微生物の包括固定処理が
なされていないPVAゲル74であっても、先に述べた
如くゲル成分の溶出による一部の有機物の凝集効果はあ
るので、微生物が繁殖するまでの間でも相当程度の浄化
効果が得られる。
Further, some of the components of the PVA gel 74 tend to be eluted in the bath water. The eluted components function as a flocculant for a part of the organic matter in the water and cause a part of the organic matter to coagulate. Leading to. Then, the partially aggregated organic matter is dispersed and mixed in the bath water together with the organic matter which is not decomposed by the microorganisms and the sludge-like pollution residue generated by the decomposition. In this example, since the PVA gel 74 used was one in which microorganisms were entrapped and fixed,
It is not necessary to wait for the microorganisms to propagate in the PVA gel 74 filled in the microorganism purification tank 40, and the ability of the microorganisms to purify organic substances can be sufficiently exhibited from the beginning of use. That is, since the decomposition of organic substances is sufficiently performed from the beginning of the installation of the circulation purification device, the bath water can be enjoyed bathing with clean bath water without becoming cloudy or slimy at the beginning. is there. However, even with PVA gel 74 that has not been subjected to entrapping immobilization of microorganisms, the elution of gel components has the effect of aggregating some organic substances as described above, so even before the microorganisms proliferate. The purification effect of is obtained.

【0028】(電気加熱槽でのプロセスについて)微生物
浄化槽40で有機物の浄化がなされた浴用水は、温度セ
ンサ58を設置した管路48を経て電気加熱槽50へ供
給される。温度センサ58は管路48を通過する浴用水
の温度を計測監視し、該センサ58の検出結果が図8に
示すメモリ(RAM)98での設定値よりも低い場合は、
前記制御回路62がヒータ駆動回路93を制御して電熱
ヒータ92をオンする。逆に温度センサ58の検出結果
がメモリ(RAM)98での設定値よりも高い場合は、制
御回路62がヒータ駆動回路93を制御して電熱ヒータ
92をオフする。このようにして電気加熱槽50におけ
る浴用水は、常に入浴に適した温度に維持された状態
で、管路52および排水ホース18を経て浴槽10に帰
還させられる。
(Regarding Process in Electric Heating Tank) The bath water in which the organic substances have been purified in the microbial purification tank 40 is supplied to the electric heating tank 50 via the conduit 48 in which the temperature sensor 58 is installed. The temperature sensor 58 measures and monitors the temperature of the bath water passing through the pipe 48, and when the detection result of the sensor 58 is lower than the set value in the memory (RAM) 98 shown in FIG.
The control circuit 62 controls the heater driving circuit 93 to turn on the electric heater 92. On the contrary, when the detection result of the temperature sensor 58 is higher than the set value in the memory (RAM) 98, the control circuit 62 controls the heater drive circuit 93 to turn off the electric heater 92. In this way, the bath water in the electric heating tank 50 is always returned to the bath 10 via the conduit 52 and the drain hose 18 while being kept at a temperature suitable for bathing.

【0029】(各構成の変更例について)本発明の構成
は、以上に述べた実施形態に限定されるものではなく、
その要旨を逸脱しない範囲で種々の変更を加えることが
できる。例えば図2に示す如く、浴用水の流れる方向に
微生物浄化槽40,電解槽38および電気加熱槽50を
順に配設するようにしてもよい。この場合は、殺菌作用
を果し得る電解槽38が浴槽10に近接して位置するの
で、該浴槽10へ帰還する浴用水に含まれる雑菌や微生
物の数を更に低減させると共に、ヌメリの発生をより効
果的に抑制し得るものである。なお電解槽38での電気
分解により、陽極66の近傍に生成される活性酸素(過
酸化水素)は、浴用水に含まれる雑菌だけでなく有機物
を分解する有用微生物までも殺す能力を有している。従
って図1の如く電解槽38を微生物浄化槽40の上流側
に配設する場合は、この活性酸素を含む浴用水が該微生
物浄化槽40に流入して、PVAゲル74に繁殖固定さ
せた有用微生物を死滅させることも懸念される。勿論、
活性酸素の寿命は極めて短いので、図1に示す例の場合
であっても、電解槽38と微生物浄化槽40との間を適
当に離すように配慮しておけば全く問題はない。しかし
図2のように、微生物浄化槽40を電解槽38の上流側
に配置する構成とすれば、これら微生物浄化槽40と電
解槽38は極めて近接的に設置することもでき、装置全
体をコンパクト化するのに寄与し得る。
(Regarding Modifications of Each Configuration) The configuration of the present invention is not limited to the above-mentioned embodiment,
Various changes can be made without departing from the spirit of the invention. For example, as shown in FIG. 2, you may make it arrange | position the microorganism purification tank 40, the electrolytic cell 38, and the electric heating tank 50 in order in the flowing direction of bath water. In this case, the electrolytic cell 38 capable of performing a sterilizing action is located close to the bath 10, so that the number of bacteria and microorganisms contained in the bath water returning to the bath 10 can be further reduced and slime can be prevented. It can be suppressed more effectively. The active oxygen (hydrogen peroxide) generated in the vicinity of the anode 66 by electrolysis in the electrolytic cell 38 has the ability to kill not only the bacteria contained in the bath water but also useful microorganisms that decompose organic substances. There is. Therefore, when the electrolytic cell 38 is arranged on the upstream side of the microbial purification tank 40 as shown in FIG. 1, the bath water containing the active oxygen flows into the microbial purification tank 40, and the useful microorganisms propagated and fixed on the PVA gel 74 are fixed. There is also concern that it will be destroyed. Of course,
Since the life of active oxygen is extremely short, even in the case of the example shown in FIG. 1, there is no problem at all if the electrolytic cell 38 and the microbial purification tank 40 are properly separated. However, as shown in FIG. 2, if the microbial purification tank 40 is arranged on the upstream side of the electrolysis tank 38, the microbial purification tank 40 and the electrolysis tank 38 can be installed very close to each other, and the entire apparatus can be made compact. Can contribute to.

【0030】図2に示す電解槽38において、その流入
側管路46と流出側管路48を2点鎖線で示す管路49
でバイパスし、浴用水の一部が該電解槽38を通過する
ことなく下流の電気加熱槽50へ流入する構成としても
よい。これは、電解槽38における電極間距離を狭くす
る場合に効果的である。すなわち電解槽38は、その電
極66,68の距離を狭めることによって、低電圧の直
流印加で浴用水の電気分解をより効率的に行なうことが
できる。これによれば、直流電源に対する負荷を軽減さ
せることができると共に、万一の感電事故の心配もなく
なり安全性が高まる。しかし反面で、電解槽38におけ
る浴用水の流路抵抗が増大し、循環ポンプ44に対する
負荷が逆に大きくなる問題を有している。このような場
合に、前述した如く電解槽38への流入側にバイパス管
路49を設けてやれば、全体的な流路抵抗は低く抑える
ことができ、直流電源に対する負荷の軽減に加えて、循
環ポンプ44の負荷も低減させ得るものである。
In the electrolytic cell 38 shown in FIG. 2, the inflow side pipe line 46 and the outflow side pipe line 48 are shown by a two-dot chain line line 49.
Alternatively, a part of the bath water may flow into the downstream electric heating tank 50 without passing through the electrolytic tank 38. This is effective in reducing the distance between the electrodes in the electrolytic cell 38. That is, in the electrolytic bath 38, by narrowing the distance between the electrodes 66, 68, electrolysis of bath water can be more efficiently performed by applying a low voltage DC. According to this, it is possible to reduce the load on the DC power source, and there is no fear of an electric shock accident, so that safety is improved. However, on the other hand, there is a problem in that the flow path resistance of the bath water in the electrolytic cell 38 increases, and the load on the circulation pump 44 increases conversely. In such a case, if the bypass conduit 49 is provided on the inflow side to the electrolytic cell 38 as described above, the overall flow path resistance can be suppressed low, and in addition to reducing the load on the DC power supply, The load on the circulation pump 44 can also be reduced.

【0031】[0031]

【発明の効果】以上に説明した如く、本願の請求項1に
記載の循環浄化装置によれば、電解手段への通電により
汚染液体が電気分解され、活性酸素が発生して殺菌を行
なうと共に、汚染液体中の有機物が酸化分解される。微
生物浄化手段では、微生物により汚染液体に含まれる有
機物を分解して該液体を浄化する。そして電解手段の作
用と微生物浄化手段の作用とが相俟って、汚染液体の殺
菌および該液体に含まれる有機物の分解がなされ、汚染
液体の効率的な清浄化が達成される。また本願の請求項
2に記載の循環浄化装置によれば、電解槽への通電によ
り汚染液体が電気分解され、活性酸素が発生して殺菌を
行なうと共に、汚染液体中の有機物が酸化分解される。
微生物浄化槽では、粒状の合成高分子ゲルに存在させた
微生物により、汚染液体に含まれる有機物を分解して該
液体を浄化する。そして電解槽の作用と微生物浄化槽の
作用とが相俟って、汚染液体の殺菌および該液体に含ま
れる有機物の分解がなされ、汚染液体の効率的な清浄化
が達成される。
As described above, according to the circulation purifying apparatus of the first aspect of the present invention, the contaminated liquid is electrolyzed by the energization of the electrolyzing means, active oxygen is generated, and sterilization is performed. Organic substances in the contaminated liquid are oxidatively decomposed. The microbial purification means decomposes the organic matter contained in the contaminated liquid by microorganisms to purify the liquid. The action of the electrolyzing means and the action of the microbial purification means work together to sterilize the contaminated liquid and decompose organic substances contained in the liquid, thereby achieving efficient cleaning of the contaminated liquid. Further, according to the circulation purification apparatus of the second aspect of the present application, the contaminated liquid is electrolyzed by energizing the electrolytic cell, active oxygen is generated and sterilized, and the organic matter in the contaminated liquid is oxidatively decomposed. .
In the microbial septic tank, microorganisms present in the granular synthetic polymer gel decompose the organic matter contained in the contaminated liquid to purify the liquid. Then, the action of the electrolytic cell and the action of the microbial purification tank are combined to sterilize the contaminated liquid and decompose organic matter contained in the liquid, thereby achieving efficient cleaning of the contaminated liquid.

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

【図1】本発明の好適実施例に係る循環浄化装置の基本
構成を示す概略図である。
FIG. 1 is a schematic diagram showing a basic configuration of a circulation purification device according to a preferred embodiment of the present invention.

【図2】本発明の別の好適実施例に係る循環浄化装置の
概略図である。
FIG. 2 is a schematic view of a circulation purification device according to another preferred embodiment of the present invention.

【図3】微生物浄化槽の概略構造を示す縦断面図であ
る。
FIG. 3 is a vertical sectional view showing a schematic structure of a microbial septic tank.

【図4】電解槽の概略構造を示す縦断面図である。FIG. 4 is a vertical sectional view showing a schematic structure of an electrolytic cell.

【図5】浴室に本願に係る汚染液体の循環浄化装置を設
置した状態を示す概略斜視図である。
FIG. 5 is a schematic perspective view showing a state in which a circulation purification device for polluted liquid according to the present application is installed in a bathroom.

【図6】循環浄化装置の一部を構成する給排水ユニット
を、浴槽内壁面に取付けた状態で示す縦断面図である。
FIG. 6 is a vertical cross-sectional view showing a water supply / drainage unit which constitutes a part of the circulation purification device, in a state where the water supply / drainage unit is attached to the inner wall surface of the bath.

【図7】循環浄化装置の制御の流れを示すフローチャー
ト図である。
FIG. 7 is a flowchart showing a control flow of the circulation purification device.

【図8】循環浄化装置の電気的構成部分を、個別に制御
し得る制御ブロックを示す概略図である。
FIG. 8 is a schematic diagram showing a control block that can individually control electrical components of the circulation purification device.

【符号の説明】[Explanation of symbols]

10 浴槽 12 浴用水 14 給排水ユニット 16 吸水ホース 18 排水ホース 20 装置本体 22 漏電ブレーカ 24 ケーブル 26 アースケーブル 28 吸盤 30 箱状ケーシング 32 吸水口 34 吐出口 36 フィルタ 38 電解槽 39 電解槽駆動回路 40 微生物浄化槽 44 循環ポンプ 45 ポンプ駆動回路 46 管路 48 管路 49 バイパス管 50 電気加熱槽 52 管路 56 流量センサ 58 温度センサ 60 水位センサ 62 制御回路 64 箱型ケーシング 66,68 電極部 70 円筒状ケーシング 70a 流入口 70b 流出口 72 管状水流路 74 合成高分子ゲル(PVAゲル) 76 フイルタ 78 水滞留部 89 弁駆動回路 92 電熱ヒータ 93 ヒータ駆動回路 94 ディスプレイ 95 ディスプレイ駆動回路 96 オゾナイザ 97 オゾナイザ駆動回路 98 メモリ(RAM) 99 ソレノイド弁 10 Bathtub 12 Bath Water 14 Water Supply / Drainage Unit 16 Water Absorption Hose 18 Drain Hose 20 Equipment Main Body 22 Earth Leak Breaker 24 Cable 26 Earth Cable 28 Suction Cup 30 Box Casing 32 Water Suction Port 34 Discharge Port 36 Filter 38 Electrolysis Tank 39 Electrolysis Tank Drive Circuit 40 Microbial Purification Tank 44 Circulation pump 45 Pump drive circuit 46 Pipe line 48 Pipe line 49 Bypass pipe 50 Electric heating tank 52 Pipe line 56 Flow rate sensor 58 Temperature sensor 60 Water level sensor 62 Control circuit 64 Box type casing 66,68 Electrode section 70 Cylindrical casing 70a Flow Inlet 70b Outlet 72 Tubular water flow path 74 Synthetic polymer gel (PVA gel) 76 Filter 78 Water retention part 89 Valve drive circuit 92 Electric heater 93 Heater drive circuit 94 Display 95 Display drive circuit 96 Ozonizer 9 Ozonizer driving circuit 98 memory (RAM) 99 Solenoid valve

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/50 510 C02F 1/50 550D 520 550L 531 560A 540 560B 550 560F 560H 560 560Z 1/78 3/10 A F24H 9/00 W B01D 35/02 J 1/78 C02F 1/46 101Z 3/10 102 E04H 4/12 E04H 3/20 B F24H 9/00 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C02F 1/50 510 C02F 1/50 550D 520 550L 531 560A 540 560B 550 560F 560H 560 560Z 1/78 3 / 10 A F24H 9/00 W B01D 35/02 J 1/78 C02F 1/46 101Z 3/10 102 E04H 4/12 E04H 3/20 B F24H 9/00

Claims (12)

【特許請求の範囲】[Claims] 【請求項1】 経時的に汚染される液体を液体貯留手段
に貯留し、この汚染液体を該貯留手段の外部でポンプ循
環させつつ浄化および殺菌を行なうようにした汚染液体
の循環浄化装置において、 前記汚染液体に含まれる有機物を微生物により分解して
浄化する微生物浄化手段と、 この汚染液体を電気分解して前記有機物の酸化分解を促
進する電解手段とを備え、 これらの各手段を前記汚染液体の循環経路中で連通接続
したことを特徴とする汚染液体の循環浄化装置。
1. A circulation purification device for a contaminated liquid, wherein a liquid contaminated with time is stored in a liquid storage means, and the contaminated liquid is circulated and pumped outside the storage means for purification and sterilization. Microorganism purification means for decomposing and purifying organic matter contained in the contaminated liquid by microorganisms, and electrolysis means for electrolyzing this contaminated liquid to promote oxidative decomposition of the organic matter are provided. A circulation purification device for polluted liquid, characterized by being connected in communication in the circulation path of the.
【請求項2】 経時的に汚染される液体を液体貯留槽に
貯留し、この汚染液体を該貯留槽の外部でポンプ循環さ
せつつ浄化および殺菌を行なうようにした汚染液体の循
環浄化装置において、 前記汚染液体に含まれる有機物を吸着・分解して浄化す
る微生物を存在させた粒状の合成高分子ゲルを充填して
なる微生物浄化槽と、 この汚染液体を電気分解して前記有機物の酸化分解を促
進する電解槽とを備え、 これらの各槽を前記汚染液体の循環経路中で連通接続し
たことを特徴とする汚染液体の循環浄化装置。
2. A circulation purification device for a contaminated liquid, wherein a liquid contaminated with time is stored in a liquid storage tank, and the contaminated liquid is purified and sterilized while being circulated by a pump outside the storage tank. A microbial septic tank filled with a granular synthetic polymer gel containing microorganisms that adsorb and decompose organic matter contained in the contaminated liquid to purify it, and promote oxidative decomposition of the organic matter by electrolyzing the contaminated liquid. And a respective electrolytic tank, and each of these tanks is connected in the circulation path of the contaminated liquid so as to be circulated and purified.
【請求項3】 前記合成高分子ゲルの充填量は、前記微
生物浄化槽に流入する汚染液体により自由に流動し得る
程度に調節されている請求項2に記載の汚染液体の循環
浄化装置。
3. The circulating purifying apparatus for polluted liquid according to claim 2, wherein the filling amount of the synthetic polymer gel is adjusted so that the polluted liquid flowing into the microorganism purification tank can freely flow.
【請求項4】 前記合成高分子ゲルは、その内部に有機
物の吸着・分解を行なう微生物が包括固定処理されてい
る請求項2または3に記載の汚染液体の循環浄化装置。
4. The circulating purification apparatus for contaminated liquid according to claim 2 or 3, wherein the synthetic polymer gel is entrapped with microorganisms that adsorb and decompose organic substances.
【請求項5】 前記微生物浄化槽は汚染液体の流入口お
よび流出路を備え、これら流入口および流出路に前記粒
状の合成高分子ゲルの外部流出を阻止するメッシュのフ
イルタが配設されている請求項2〜4の何れかに記載の
汚染液体の循環浄化装置。
5. The microbial septic tank is provided with an inlet and an outlet for a contaminated liquid, and a mesh filter for preventing the granular synthetic polymer gel from flowing out is disposed in the inlet and the outlet. Item 5. A circulation purification device for contaminated liquid according to any one of items 2 to 4.
【請求項6】 前記電解槽への汚染液体の流入路には、
該電解槽を回避して下流側の槽に連通するバイパス流路
が設けられている請求項2に記載の汚染液体の循環浄化
装置。
6. The inflow passage of the contaminated liquid to the electrolytic cell,
The circulation purification device for contaminated liquid according to claim 2, wherein a bypass flow path is provided which communicates with a downstream side tank while avoiding the electrolytic cell.
【請求項7】 前記電解槽は2つの電極部を備え、一方
の電極部は陽極として機能すると共に他方の電極部は陰
極として機能するようになっている請求項2および6の
何れかに記載の汚染液体の循環浄化装置。
7. The electrolytic cell is provided with two electrode portions, one electrode portion functions as an anode and the other electrode portion functions as a cathode. Circulation purification equipment for polluted liquids.
【請求項8】 前記電解槽における2つの電極部は、汚
染液体の通過量や通過時間に応じて、その極性を交互に
切換え得るようになっている請求項2,6および7の何
れかに記載の汚染液体の循環浄化装置。
8. The two electrode parts in the electrolytic cell are capable of alternately switching their polarities according to the amount and time of passage of a contaminated liquid. The circulating purification apparatus for polluted liquid described.
【請求項9】 前記汚染液体が循環する方向に、前記電
解槽および微生物浄化槽が順に配置されている請求項2
に記載の汚染液体の循環浄化装置。
9. The electrolytic cell and the microbial septic tank are sequentially arranged in the direction in which the contaminated liquid circulates.
The circulating purification apparatus for polluted liquid according to 1.
【請求項10】 前記汚染液体が循環する方向に、前記
微生物浄化槽および電解槽が順に配置されている請求項
2に記載の汚染液体の循環浄化装置。
10. The circulating purification apparatus for polluted liquid according to claim 2, wherein the microbial purification tank and the electrolytic cell are sequentially arranged in a direction in which the polluted liquid circulates.
【請求項11】 前記電解槽および微生物浄化槽を連通
接続する液体循環路の適宜個所にオゾン発生装置が配設
されている請求項2,9および10の何れかに記載の汚
染液体の循環浄化装置。
11. An apparatus for circulating and purifying a contaminated liquid according to claim 2, 9 or 10, wherein an ozone generator is disposed at an appropriate position in a liquid circulation path that connects and connects the electrolytic cell and the microbial purification tank. .
【請求項12】 前記電解槽および微生物浄化槽が連通
される液体循環路の適宜個所に、汚染液体を加熱昇温さ
せる電気加熱槽が介装されている請求項2に記載の汚染
液体の循環浄化装置。
12. The circulating purification of a contaminated liquid according to claim 2, wherein an electric heating tank for heating and raising the temperature of the contaminated liquid is provided at an appropriate position of a liquid circulation path communicating with the electrolytic cell and the microbial purification tank. apparatus.
JP7326371A 1995-11-20 1995-11-20 Circulation purifying device for contaminated liquid Pending JPH09141283A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7326371A JPH09141283A (en) 1995-11-20 1995-11-20 Circulation purifying device for contaminated liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7326371A JPH09141283A (en) 1995-11-20 1995-11-20 Circulation purifying device for contaminated liquid

Publications (1)

Publication Number Publication Date
JPH09141283A true JPH09141283A (en) 1997-06-03

Family

ID=18187059

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7326371A Pending JPH09141283A (en) 1995-11-20 1995-11-20 Circulation purifying device for contaminated liquid

Country Status (1)

Country Link
JP (1) JPH09141283A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006300421A (en) * 2005-04-21 2006-11-02 Sanyo Electric Co Ltd Refrigerating device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006300421A (en) * 2005-04-21 2006-11-02 Sanyo Electric Co Ltd Refrigerating device
JP4703246B2 (en) * 2005-04-21 2011-06-15 三洋電機株式会社 Refrigeration equipment

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