JPH09174080A - Circulating and purifying apparatus for contaminated solution - Google Patents

Circulating and purifying apparatus for contaminated solution

Info

Publication number
JPH09174080A
JPH09174080A JP7326368A JP32636895A JPH09174080A JP H09174080 A JPH09174080 A JP H09174080A JP 7326368 A JP7326368 A JP 7326368A JP 32636895 A JP32636895 A JP 32636895A JP H09174080 A JPH09174080 A JP H09174080A
Authority
JP
Japan
Prior art keywords
liquid
tank
contaminated
filter
contaminated liquid
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
JP7326368A
Other languages
Japanese (ja)
Inventor
Akihisa Suzuki
昭央 鈴木
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 JP7326368A priority Critical patent/JPH09174080A/en
Publication of JPH09174080A publication Critical patent/JPH09174080A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

  • Biological Treatment Of Waste Water (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a lightweight circulating and purifying apparatus preventing the lowering of decomposition action caused by the accumulation of a decomposition product on a base material having bacteria decomposing org. matter fixed thereto, capable of suitably purifying a contaminated liquid even immediately after the establishment of an apparatus or the washing of a base material, and good in handling properties. SOLUTION: A circulating and purifying apparatus is constituted so that a liquid 12 contaminated with the elapse of time is stored in a liquid storage means 10 and this contaminated liquid 12 is purified while circulated in the outside of the storage means 10 by a pump 44. In this case, a bacteria purifying means 40 decomposing org. matter contained in the contaminated liquid 12 by bacteria to purify the liquid 12 and a physical filter means 42 collecting and filtering the contaminant contained in the contaminated liquid 12 are provided and these means are connected to the circulating route of the contaminated liquid.

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. The present invention relates to a domestic / commercial circulation purification device for doing so.

【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、この汚染液体に含まれる汚染物質を捕集・
濾過する物理濾過手段とを備え、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 contaminated liquid circulating and purifying device for purifying while circulating the pump outside the means, a microbial purification means for decomposing and purifying organic matter contained in the contaminated liquid by microorganisms, and a pollutant contained in the contaminated liquid Collect
It is characterized in that it is provided with a physical filtering means for filtering, and each of these means is connected and connected in the circulation 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、この汚染液体に含まれる汚染物質を捕集・濾過する
物理濾過槽とを備え、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 designed to be purified while being circulated by pumping outside of, is filled with a granular synthetic polymer gel in which microorganisms that adsorb and decompose organic substances contained in the polluted liquids are present. It is characterized in that it is provided with a microbial purification tank and a physical filtration tank for collecting and filtering pollutants contained in the contaminated liquid, and these tanks are connected in a circulating path of the contaminated liquid.

【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9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10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
られて、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. Is to do. That is, as shown in FIG. 9, 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 suction 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. 10, the water supply / drainage unit 14 is detachably attached to the inner wall surface of the bathtub 10 by a suction cup 28 as an example, and is located below a general storage level of the bath water 12.

【0012】図9および図10に示す給排水ユニット1
4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が配設されて、給排水ユニット14を浴
槽10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10の内壁面に取付けた際に浴用水にそっくり浸漬さ
れる。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、
ここで浄化された後に、排水ホース18および吐出口3
4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 1 shown in FIGS. 9 and 10.
Reference numeral 4 denotes, for example, a rectangular box-shaped casing 30. On the front surface of the casing 30, a water suction port 32 for sucking the bath water in a vertical relationship and a discharge port 34 for returning the purified bath water to the bath 10 are provided. Further, the suction cup 28 is arranged on the back surface of the box-shaped case 30 so that the water supply / drainage unit 14 can be attached to the inner wall surface of the bathtub 10. 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 suction port 32 and the discharge port 34 are completely immersed in the bath water when the water supply / drainage unit 14 is attached to the inner wall surface of the bathtub 10. Then, when the circulation purification device described later is operated, the bath water in the bathtub 10 is absorbed by the water intake port 32 under the action of the circulation pump.
And flowing into the device body 20 via the water absorption hose 16,
After being purified here, the drain hose 18 and the discharge port 3
The cycle of returning to the bath 10 via 4 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に含まれる
垢等の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、該浴用水12に含まれる有機状また
は無機状の汚染物質を捕集・濾過する物理濾過槽42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14
に連通する吸水ホース16は、浴用水の循環ポンプ44
を介して物理濾過槽42の入口側に接続し、この物理濾
過槽42の出口側は、管路46を介して微生物浄化槽4
0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50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。なお浄化後の浴用水が浴槽10に帰還する管路
52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
48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
らの各センサは、図12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 main body 20 of the circulation purification apparatus includes a microbial purification tank 40 for adsorbing and decomposing and purifying organic matters such as dust contained in the bath water 12 which is contaminated with time by microorganisms, and a microbial purification tank for the bath. A physical filtration tank 42 for collecting and filtering organic or inorganic pollutants contained in the water 12 is provided, and these tanks are connected to each other through a pipe line through which the bath water 12 is circulated. That is, the water supply / drainage unit 14
The water suction hose 16 communicating with the
Is connected to the inlet side of the physical filtration tank 42 via the pipe, and the outlet side of the physical filtration tank 42 is connected via a pipe 46 to the microbial purification tank 4
It is connected to the inlet side of 0. Further, the outlet side of the microbial septic tank 40 is connected to an inlet side of an electric heating tank 50 for heating and raising the temperature of the bath water via a pipe line 48, and the outlet side of the electric heating tank 50 is connected to the inlet side via a pipe line 52. It is connected to the drain hose 18. A flow rate sensor 56 for detecting the flow rate of the bath water is inserted in the pipeline 52 through which the purified bath water returns to the bath 10. Further, in the pipeline 48 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. 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 a control circuit 62 shown in the control block of FIG. 12, and inputs information necessary for various controls of the apparatus main body 20 to the circuit 62.

【0014】(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4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.

【0015】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.

【0016】(物理濾過槽について)物理濾過槽42は、
浴用水12に含まれる微細な有機状や無機状をなす汚染
物質を物理的に捕集・濾過するためのもので、濾過材と
して所謂ワインディングフィルタが内部装填されてい
る。例えば図5に示す如く物理濾過槽42は、直立配置
される円筒状ケーシング80と、該ケーシング80の内
部に着脱自在に同心配置されるワインディングフィルタ
82と、該ケーシング80の底部に開設した流入口80
aおよび流出口80bとから基本的に構成される。ワイ
ンディングフィルタ82は、図示の如く筒状コア84に
線状素材86を過巻状に所要数巻回して構成され、該筒
状コア84の中心を貫通する中空部84aには多数の通
孔84bが穿設されている。また線状素材86として、
例えばポリプロピレン製のヤーンが好適に使用され、そ
の巻回密度としては、例えば10〜100μm程度が推
奨される。図示例のワインディングフィルタ82では、
約10〜20μmの巻回密度のものを採用した。なおワ
インディングフィルタ以外にも、不織布のフィルタやゼ
オライト、パームチットの如き物理的濾過材が適宜に使
用される。
(About physical filtration tank) The physical filtration tank 42 is
It is for physically collecting and filtering fine organic or inorganic pollutants contained in the bath water 12, and a so-called winding filter is internally loaded as a filtering material. For example, as shown in FIG. 5, the physical filtration tank 42 includes a cylindrical casing 80 that is vertically arranged, a winding filter 82 that is detachably concentrically arranged inside the casing 80, and an inlet port that is opened at the bottom of the casing 80. 80
It is basically composed of a and the outlet 80b. The winding filter 82 is constructed by winding a required number of windings of a linear material 86 around a cylindrical core 84 as shown in the drawing, and a large number of through holes 84b in a hollow portion 84a penetrating the center of the cylindrical core 84. Has been drilled. As the linear material 86,
For example, polypropylene yarn is preferably used, and its winding density is recommended to be, for example, about 10 to 100 μm. In the winding filter 82 of the illustrated example,
A winding density of about 10 to 20 μm was adopted. In addition to the winding filter, a non-woven fabric filter or a physical filter material such as zeolite or palm chit is appropriately used.

【0017】物理濾過槽42に流入口80aを介して流
入した浴用水は、ワインディングフィルタ82の外周か
ら該フィルタの半径方向内方に通過し、ここで該浴用水
に含まれる微細な汚染物質の物理的な捕集・濾過が行な
われる。このフィルタ82の細かい線材層を通過した浴
用水は、筒状コア84に穿設した多数の通孔84bを経
て中空部84aに出た後、この中空部84aに連通する
流出口80bを介して槽外へ流出する。また該濾過槽4
2へ流入した浴用水の一部は、前記ワインディングフィ
ルタ82を通過することなく槽外へそのまま流出する。
すなわち浴用水の一部は、物理濾過槽42におけるケー
シング内壁面とフィルタ外周面の間に画成される環状ス
ペースを上昇し、該ケーシング80の内頂部に衝突して
反転した後に、前記筒状コア84に設けた中空部84a
を下降して流出口80bから槽外へ流出する。ところで
ワインディングフィルタ82は、長期の使用により徐々
に目詰まりし、該フィルタ82を通過する浴用水の通水
抵抗も次第に増大することになる。この場合は、物理濾
過槽42へ流入した浴用水の内、前記フィルタ82およ
び筒状コア84の通孔84bを介することなく、前述の
如くそのまま環状スペースおよび中空部84aを経て槽
外へ流出する浴用水の割合も増加する。すなわちワイン
ディングフィルタ82が次第に目詰まりすると、該フィ
ルタ82をバイパスして直接流出口80bへ向かう浴用
水の割合も増加するので、フィルタ目詰まり時の浴用水
の循環量の低下が効果的に防止される。
The bath water flowing into the physical filtration tank 42 through the inflow port 80a passes from the outer periphery of the winding filter 82 to the inner side in the radial direction of the filter, where fine contaminants contained in the bath water are contained. Physical collection / filtration is performed. The bath water that has passed through the fine wire layer of the filter 82 exits into the hollow portion 84a through a large number of through holes 84b formed in the tubular core 84, and then through the outlet 80b that communicates with the hollow portion 84a. It flows out of the tank. Also, the filtration tank 4
A part of the bath water flowing into 2 flows out of the tank as it is without passing through the winding filter 82.
That is, a part of the bath water rises in an annular space defined between the inner wall surface of the casing and the outer peripheral surface of the filter in the physical filtration tank 42, collides with the inner top portion of the casing 80 and is inverted, and then the tubular shape is obtained. Hollow part 84a provided in the core 84
To flow out of the tank through the outlet 80b. By the way, the winding filter 82 is gradually clogged due to long-term use, and the water flow resistance of the bath water passing through the filter 82 also gradually increases. In this case, in the bath water that has flowed into the physical filtration tank 42, without passing through the filter 82 and the through hole 84b of the tubular core 84, as described above, it flows out of the tank through the annular space and the hollow portion 84a. The proportion of bath water also increases. That is, when the winding filter 82 is gradually clogged, the proportion of the bath water that bypasses the filter 82 and directly goes to the outflow port 80b also increases, so that the decrease in the circulation amount of the bath water when the filter is clogged is effectively prevented. It

【0018】この物理濾過槽42には、筒状コア84の
中空部84aに常閉弁88を設け、ワインディングフィ
ルタ82が目詰まりして通水抵抗が次第に増大した場合
に、これに伴って次第に増加する浴用水の圧力により該
常閉弁88を徐々に開放し、該浴用水の一部を前記中空
部84aへバイパスさせるようにしてもよい。すなわち
ワインディングフィルタ82の筒状コア84には、図6
に示すように、その中空部84aの上部開口を圧縮バネ
90の弾力により閉成する常閉弁88が設けられてい
る。圧縮バネ90の弾性度は、フィルタ82が徐々に目
詰まりして次第に増大する通水抵抗が所定値を超えた場
合に、前記常閉弁88に外方から作用している水圧が該
圧縮バネ90を徐々に圧縮させ得る程度に設定されてい
る。従ってフィルタ82が次第に目詰まりして通水抵抗
が増大するにつれて、図7に示す如く浴用水は前記常開
弁88を次第に開放する。これにより浴用水の一部は、
前記ワインディングフィルタ82で濾過されることな
く、前記コア84における中空部84aの上部開口から
中空部84aに流入し、この中空部84aおよび流出口
80bを介して槽外へ流出される。
In this physical filtration tank 42, a normally closed valve 88 is provided in the hollow portion 84a of the cylindrical core 84, and when the winding filter 82 is clogged and the water flow resistance is gradually increased, it is gradually increased. The normally closed valve 88 may be gradually opened by the increasing pressure of the bath water to bypass a part of the bath water to the hollow portion 84a. That is, in the tubular core 84 of the winding filter 82, as shown in FIG.
As shown in FIG. 7, a normally closed valve 88 that closes the upper opening of the hollow portion 84a by the elastic force of the compression spring 90 is provided. The elasticity of the compression spring 90 is such that when the filter 82 is gradually clogged and the water resistance that increases gradually exceeds a predetermined value, the water pressure acting on the normally closed valve 88 from the outside is applied to the compression spring 90. It is set so that 90 can be gradually compressed. Therefore, as the filter 82 is gradually clogged and the water flow resistance increases, the bath water gradually opens the normally open valve 88 as shown in FIG. As a result, part of the bath water is
Without being filtered by the winding filter 82, it flows into the hollow portion 84a from the upper opening of the hollow portion 84a in the core 84, and flows out of the tank through the hollow portion 84a and the outlet port 80b.

【0019】図8は、物理濾過槽42の別の実施例を示
し、該物理濾過槽42に装填されるワインディングフィ
ルタ82は、その線状素材86の巻回ピッチが粗なもの
と、密なものとになるよう区分けして巻回されている。
すなわちワインディングフィルタ82の上部半体の線状
素材86は巻回ピッチが粗くなっており、また下部半体
の線状素材86は巻回ピッチが密になっている。このよ
うに線状素材86の巻回ピッチを区分けすると、巻回ピ
ッチの粗いフィルタ部分での水の通過抵抗は、巻回ピッ
チの密なフィルタ部分に比して軽微となる。従って物理
濾過槽42での濾過作用時に、ワインディングフィルタ
82の経時的な目詰まりに部分的な差を生ずることにな
り、通水抵抗が増大する時期を調節することが可能とな
る。
FIG. 8 shows another embodiment of the physical filtration tank 42. In the winding filter 82 loaded in the physical filtration tank 42, the winding pitch of the linear material 86 is coarse and dense. It is divided and wound so that it becomes a thing.
That is, the winding pitch of the upper half of the linear material 86 of the winding filter 82 is coarse, and the winding pitch of the lower half of the linear material 86 is dense. When the winding pitch of the linear material 86 is divided in this way, the passage resistance of water in the filter portion having a coarse winding pitch is smaller than that in the filter portion having a fine winding pitch. Therefore, during the filtration operation in the physical filtration tank 42, a partial difference occurs in the clogging of the winding filter 82 with time, and it is possible to adjust the time when the water flow resistance increases.

【0020】(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12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4
4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 when the water level does not reach the reference water level, an error is displayed on the display 94 shown in FIG.
Stop the operation of 4. 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.

【0021】(オゾナイザについて)前述した微生物浄化
槽40,電気加熱槽50および物理濾過槽42を連通接
続する管路系に、図12に示すオゾナイザ96を別途介
挿するようにしてもよい。このオゾナイザ96を用いる
ことによって、浴用水に含まれる有害菌を確実に殺菌す
ることができる。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12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99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 Ozonizer) The ozonizer 96 shown in FIG. 12 may be separately inserted in the pipe line system that connects and connects the microbial purification tank 40, the electric heating tank 50, and the physical filtration tank 42 described above. By using this ozonizer 96, harmful bacteria contained in the bath water can be surely sterilized. 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 pipe and the ozonizer 96 are connected via a solenoid valve 99 shown in FIG. 12, and by opening the solenoid valve 99, ozone is injected into the bath water in the pipe, and the solenoid valve 99 Closing will stop ozone injection into the bath water.

【0022】(装置の制御ブロックについて)図12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6
0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、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.
The block for individually controlling the electrical components of the circulation purification apparatus according to the present invention is schematically shown, and the flow rate sensor 56, the temperature sensor 58, and the water level sensor 6 described above in the control circuit 62.
0 is connected to input the 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. Also, the Ozonizer 96
Are driven by the ozonizer drive circuit 97, and the display 94 is driven by the display drive circuit 95 in a timely manner.

【0023】(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
11に示すフローチャートを参照しながら説明する。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、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 purification device, the memory (RAM) 98 is
The temperature value of the bath water and the start / end time of the process in the ozonizer 96 are set 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.

【0024】図11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4
4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を確
認し、結果が否定(NO)であれば、同じくディスプレイ9
4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からの浴用水は物理濾過槽
42,微生物浄化槽40および電気加熱槽50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および物理濾過
槽42での浄化・濾過のプロセスは後述する。
In step S 1 of FIG. 11, 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 4
4 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 is at the specified value. If the result is negative (NO), an error is displayed on the display 94 to drive the circulation pump 44. To stop.
The result goes to step S 3, if affirmative (YES), to check 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 display 9
An error message is displayed on 4 and the drive of the circulation pump 44 is stopped. If the result is affirmative (YES), the next step S 4
Move to If 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 bathtub 10 is filtered by the physical filtration tank 42, the microorganism purification tank 40 and the electric heating tank. After circulation in the order of 50, the cycle of returning to the bath 10 again is repeated. The process of purification / filtration in the microbial purification tank 40 and the physical filtration tank 42 in this case will be described later.

【0025】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での設定値より
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、オゾナイザ96での処
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12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S6で運転キーがオフ(OF
F)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S6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 , it is confirmed whether or not the processing time in the ozonizer 96 has come. The result is negative
If (NO), the ozonizer drive circuit 97 and valve drive circuit 89 shown in FIG. 12 are continuously turned off (OFF), and if the result is affirmative (YES), the ozonizer drive circuit 97 and valve drive circuit 89 are turned on. Turn it ON to inject ozone into the bath water in the pipeline. Next, in step S 6 , the operation key is turned off (OF
F) is confirmed, and if the result is negative (NO), the process returns to the previous step S 2 and the above-mentioned confirmation work is repeated. If the result of step S 6 is affirmative (YES), the operation of the circulation pump 44 is stopped.

【0026】(物理濾過槽でのプロセスに関して)循環ポ
ンプ44により浴槽10から吸い上げられた浴用水は、
管路を介して物理濾過槽42に流入する。図5に示すよ
うに、物理濾過槽42の流入口80aから槽内に流入し
た浴用水の多くは、ワインディングフィルタ82の外周
から該フィルタの半径方向内方に通過し、ここで該浴用
水に含まれる垢等の有機物や微細な汚染物質の多くが物
理的に捕集・濾過される。また物理濾過槽42へ流入し
た浴用水の一部は、物理濾過槽42のケーシング内壁面
とフィルタ82の外周面との間に画成される環状スペー
スを上昇し、該ケーシング内頂部で反転させられた後
に、筒状コア84の中空部84aを下降して流出口80
bから管路46を介して次段の微生物浄化槽40へ流入
する。また浴用水の一部は、前述の如くワインディング
フィルタ82を経ることなくバイパスし、流出口80b
で浄化された浴用水と合流している。
The bath water sucked up from the bath 10 by the circulation pump 44 (for the process in the physical filtration tank) is
It flows into the physical filtration tank 42 via a pipeline. As shown in FIG. 5, most of the bath water that has flowed into the tank from the inflow port 80a of the physical filtration tank 42 passes from the outer periphery of the winding filter 82 to the inside of the filter in the radial direction of the filter, where it is converted into the bath water. Most of the organic substances such as dirt and fine pollutants contained are physically collected and filtered. Further, a part of the bath water flowing into the physical filtration tank 42 rises in an annular space defined between the inner wall surface of the casing of the physical filtration tank 42 and the outer peripheral surface of the filter 82, and is inverted at the inner top of the casing. After that, the hollow portion 84a of the tubular core 84 is lowered and the outlet port 80
It flows into the next-stage microbial septic tank 40 from b through the pipe line 46. Further, a part of the bath water is bypassed without passing through the winding filter 82 as described above, and the outflow port 80b is provided.
It joins with the bath water purified in.

【0027】なおフィルタ82は、先に述べた如く、そ
の使用に伴い次第に目詰まりを生じて通水抵抗が徐々に
増大して行く。このように通水抵抗が徐々に増大する
と、物理濾過槽42に流入した浴用水の内で、該フィル
タ82を経て濾過がなされる浴用水の量に対して、該フ
ィルタ82をバイパスして流出口80bへ直接向かう浴
用水の占める割合が増加する。このためフィルタ82の
目詰まりによる浴用水の循環量の低下が効果的に防止さ
れる。また図6および図7に関して説明したように、筒
状コア84の中空部84aに常閉弁88を設け、ワイン
ディングフィルタ82が徐々に目詰まりして通水抵抗が
増大すると、これに伴い増加する浴用水の圧力により該
常閉弁88をバネ90の弾力に抗して徐々に開放し、浴
用水を前記中空部84aへバイパスさせるようにしても
よい。更に図8に関して説明したように、ワインディン
グフィルタ82における線状素材86の巻回ピッチを、
粗なものと密なものとになるよう区分けしておけば、該
フィルタ82の経時的な目詰まりに部分的な差を生じ、
通水抵抗が一挙に増大してしまうことがなく好適であ
る。なおフィルタ82における通水抵抗の増大を、例え
ば前述した流量センサ56により検出し、その検出値を
前記メモリ(RAM)98に記憶させた許容抵抗値と比較
して、該フィルタ82の交換時期を前記ディスプレイ9
4によりユーザーへ知らせるようにしてもよい。
As described above, the filter 82 is gradually clogged with its use, and the water flow resistance gradually increases. When the water resistance gradually increases in this manner, the amount of bath water that has been filtered through the filter 82 in the bath water that has flowed into the physical filtration tank 42 bypasses the filter 82 and flows. The proportion of the bath water that goes directly to the outlet 80b increases. Therefore, the decrease in the circulation amount of the bath water due to the clogging of the filter 82 is effectively prevented. Further, as described with reference to FIGS. 6 and 7, the normally closed valve 88 is provided in the hollow portion 84a of the tubular core 84, and when the winding filter 82 is gradually clogged and the water flow resistance increases, the water resistance increases accordingly. The normally closed valve 88 may be gradually opened against the elasticity of the spring 90 by the pressure of the bath water to bypass the bath water to the hollow portion 84a. Further, as described with reference to FIG. 8, the winding pitch of the linear material 86 in the winding filter 82 is set to
If the filter 82 is divided into a coarse one and a dense one, a partial difference occurs in the clogging of the filter 82 with time.
It is preferable because the water flow resistance does not increase at once. An increase in water flow resistance in the filter 82 is detected by, for example, the above-described flow rate sensor 56, and the detected value is compared with the allowable resistance value stored in the memory (RAM) 98 to determine the replacement time of the filter 82. The display 9
You may make it notify to a user by 4.

【0028】(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、上流側の物理濾過槽42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4に示すよう
に、前記PVAゲル74は浴用水の流勢により翻弄され
て激しく流動する。使用により汚染された浴用水がPV
A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。なお分解により発生した汚泥状の汚染残査
は、PVAゲル74に膜状に付着しようとするが、該P
VA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。また、仮に汚染残渣がPVAゲル74
に付着しても、該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。加えてPV
Aゲル74が激しく流動するため、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
きて、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, the microbial septic tank 40 is filled with an amount such that the PVA gel 74 in which microorganisms such as bacteria have been propagated and fixed in advance can freely flow due to the inflow of bath water. Has been done. Therefore, when the bath water is supplied from the physical filtration tank 42 on the upstream side to the microbial purification tank 40 through the pipe line 46, the PVA gel 74 is violently moved by the flow of the bath water as shown in FIG. To do. Bath water contaminated by use is PV
Upon contact with the A gel 74, the microorganisms propagated and fixed on the A gel 74 decompose organic matter such as dirt and body fat in the water to produce sludge-like contamination residues. The sludge-like pollution residue generated by the decomposition tends to adhere to the PVA gel 74 in a film form.
Since the VA gel 74 is violently flowing in the tank, the attachment becomes extremely difficult. Also, if the contamination residue is PVA gel 74,
Even if it adheres to, it will be easily peeled off due to the flow of the 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. In addition PV
Since the A gel 74 flows violently, there is an advantage that a large effective contact area for the bath water supplied to the microbial septic tank 40 can be secured and a sufficient purifying power for the bath water can be exhibited.

【0029】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、ヌメリ
を生じたりすることがなく、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 into the bath water, and the eluted components function as a flocculant for a portion of the organic matter in the water and cause a portion of the organic matter to flocculate. 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 organic substances are sufficiently decomposed from the beginning of the installation of the circulation purification device, the bath water does not become turbid or slimy at the beginning, and it is possible to enjoy bathing with clean bath water. 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.

【0030】(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12
に示すメモリ(RAM)98での設定値よりも低い場合
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 pipe line 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 the detection result of the sensor 58 is shown in FIG.
If it is lower than the set value in the memory (RAM) 98 shown in FIG. 2, the control circuit 62 controls the heater drive 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 maintained at a temperature suitable for bathing.

【0031】(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,物理濾過槽42および電気加熱槽5
0を順に配設するようにしてもよい。このように、微生
物浄化槽40を物理濾過槽42の上流側に配設すると、
該微生物浄化槽40で分解されず水中に残留した有機
物、生成された汚泥状の汚染残査その他不溶性の有機物
が、該物理濾過槽42のフィルタ82で良好に捕集・濾
過され、浄化された浴用水は物理濾過槽42から管路5
2および排水ホース18を経て浴槽10に帰還させられ
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, the microbial purification tank 40, the physical filtration tank 42, and the electric heating tank 5 are arranged in the flowing direction of the bath water.
You may make it arrange | position 0 in order. Thus, when the microbial septic tank 40 is arranged on the upstream side of the physical filtration tank 42,
For a purified bath, organic substances remaining in water that are not decomposed in the microbial septic tank 40, sludge-like contaminated residues and other insoluble organic substances that have been well collected and filtered by the filter 82 of the physical filtration tank 42 and purified Water passes from physical filtration tank 42 to conduit 5
2 and the drain hose 18 to be returned to the bathtub 10.

【0032】また図2に示す物理濾過槽42において、
浴用水の流入側管路46と流出側管路48を管路51で
バイパスし、この浴用水の一部が該物理濾過槽42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、物理濾過槽42に設けた前記フィ
ルタ82が経時的に目詰まりして通水抵抗が増大する
と、この濾過槽42から流出する浴用水の量が低下する
と共に、循環ポンプ44に対する負荷が増大する、とい
う問題に対する解決策である。すなわち物理濾過槽42
への流入側にバイパス管路51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るので、電気加熱槽
50へ向かう浴用水の量の低下を防止し、併せて循環ポ
ンプ44の負荷も低減させ得るものである。
In the physical filtration tank 42 shown in FIG.
The bath water inflow side pipe line 46 and the outflow side pipe line 48 are bypassed by a pipe line 51, and a part of this bath water flows into the downstream electric heating tank 50 without passing through the physical filtration tank 42. Good. This is because when the filter 82 provided in the physical filtration tank 42 is clogged with time and the water flow resistance increases, the amount of bath water flowing out from the filtration tank 42 decreases and the load on the circulation pump 44 increases. It is a solution to the problem of increasing. That is, the physical filtration tank 42
If the bypass conduit 51 is provided on the inflow side to, the overall flow resistance can be suppressed to a low level, so that a decrease in the amount of bath water going to the electric heating tank 50 is prevented, and at the same time, the circulation pump 44 is also provided. The load of can also be reduced.

【0033】更に図3は、図1に示す循環浄化装置の基
本構造において、物理濾過槽42を最終段に増設した例
を示すものである。すなわち、物理濾過槽42,微生物
浄化槽40および電気加熱槽50の順で配設した装置に
関して、この電気加熱槽50で温度調節された浴用水
を、終段に増設した物理濾過槽42に管路52を介して
導びき、浴用水に含まれる未分解の残留有機物、汚泥状
の汚染残査その他不溶性の有機物等を再びフィルタ82
で捕集・濾過するようになっている。このように物理的
な濾過処理を2段階に行なうことによって、浄化度の更
に向上した浴用水が最終段の物理濾過槽42から管路5
4および排水ホース18を経て浴槽10に戻される。
Further, FIG. 3 shows an example in which the physical filtration tank 42 is added to the final stage in the basic structure of the circulation purification apparatus shown in FIG. That is, regarding the apparatus in which the physical filtration tank 42, the microbial purification tank 40, and the electric heating tank 50 are arranged in this order, the bath water whose temperature is adjusted in the electric heating tank 50 is piped to the physical filtration tank 42 added to the final stage. The undissolved residual organic matter, sludge-like contaminated residue and other insoluble organic matter contained in the bath water are again filtered through the filter 82.
It collects and filters with. By performing the physical filtration treatment in two stages in this manner, the bath water having a further improved degree of purification can be obtained from the final stage physical filtration tank 42 to the pipe line 5.
4 and the drain hose 18 and returned to the bathtub 10.

【0034】[0034]

【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、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。また物理濾過手段では、分解された有機物
から生成される汚泥状の汚染残渣や、分解し切れなかっ
た有機物等を捕集・濾過する。これら微生物浄化手段の
作用と物理濾過手段の作用とが相俟って、汚染液体に含
まれる有機物の分解および汚染残渣や未分解有機物等の
濾過がなされるので、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、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。また物理濾過槽では、分解され
た有機物から生成される汚泥状の汚染残渣や、分解し切
れなかった有機物等を捕集・濾過する。そして微生物浄
化槽の作用と物理濾過槽の作用とが相俟って、汚染液体
に含まれる有機物の分解並びに汚染残渣や未分解有機物
等の濾過がなされ、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 purification apparatus of the first aspect of the present application, the microorganism purification means decomposes the organic matter contained in the contaminated liquid by the microorganisms to purify the liquid. The physical filtration means collects and filters sludge-like contaminated residues generated from decomposed organic substances and organic substances that have not been decomposed. The action of these microbial purification means and the action of the physical filtration means work together to decompose organic substances contained in the contaminated liquid and to filter contaminated residues and undecomposed organic substances, so that the contaminated liquid can be efficiently cleaned. Is achieved. Further, according to the circulation purification apparatus of the second aspect of the present application, in the microbial purification tank, the microorganisms present in the granular synthetic polymer gel decompose the organic matter contained in the contaminated liquid to purify the liquid. The physical filtration tank collects and filters sludge-like polluted residues produced from decomposed organic substances and organic substances that have not been decomposed. The action of the microbial septic tank and the action of the physical filtration tank are combined to decompose organic substances contained in the contaminated liquid and to filter contaminated residues and undecomposed organic substances, thereby achieving efficient cleaning of the contaminated liquid. It

【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】本発明の更に別の好適実施例に係る循環浄化装
置の概略図である。
FIG. 3 is a schematic view of a circulation purification device according to still another preferred embodiment of the present invention.

【図4】微生物浄化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 a microbial septic tank.

【図5】物理濾過槽の概略構造を示す縦断面図である。FIG. 5 is a vertical sectional view showing a schematic structure of a physical filtration tank.

【図6】図5に示す物理濾過槽のフィルタに常閉弁を配
設した状態で示す部分断面図であって、弁体がバネ圧に
より閉成した状態になっている。
6 is a partial cross-sectional view showing a state in which a normally closed valve is provided in the filter of the physical filtration tank shown in FIG. 5, in which the valve body is closed by spring pressure.

【図7】図5に示す物理濾過槽のフィルタに常閉弁を配
設した状態で示す部分断面図であって、バネ圧に抗して
水圧が弁体を押し下げた結果、該弁体が開放した状態に
なっている。
7 is a partial cross-sectional view showing a state in which a normally closed valve is provided in the filter of the physical filtration tank shown in FIG. 5, and as a result of the water pressure pushing down the valve body against the spring pressure, the valve body is It is open.

【図8】フィルタの目が、粗なものと密なものとになる
よう区分けしてなる物理濾過槽の縦断面図である。
FIG. 8 is a vertical cross-sectional view of a physical filtration tank in which a filter is divided into a coarse filter and a dense filter.

【図9】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. 9 is a schematic perspective view showing a state in which the circulation purification device for polluted liquid according to the present application is installed in a bathroom.

【図10】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. 10 is a vertical cross-sectional view showing a water supply / drainage unit that constitutes a part of the circulation purification device in a state where it is attached to the inner wall surface of the bath.

【図11】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. 11 is a flowchart showing a control flow of the circulation purification device.

【図12】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. 12 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 箱状ケース 32 吸水口 34 吐出口 36 フィルタ 40 微生物浄化槽 42 物理濾過槽 44 循環ポンプ 45 ポンプ駆動回路 46 管路 48 管路 50 電気加熱槽 51 バイパス管 52 管路 54 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 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 80 円筒状ケーシング 80a 流入口 80b 流出口 82 ワインディングフィルタ 84 筒状コア 84a 中空部 84b 通孔 86 線状素材 88 常閉弁 89 弁駆動回路 90 圧縮バネ 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 drainage hose 20 device body 22 earth leakage breaker 24 cable 26 earth cable 28 suction cup 30 box-shaped case 32 water inlet 34 discharge outlet 36 filter 40 microbial purification tank 42 physical filtration tank 44 circulation pump 45 Pump drive circuit 46 Pipe line 48 Pipe line 50 Electric heating tank 51 Bypass pipe 52 Pipe line 54 Pipe line 56 Flow rate sensor 58 Temperature sensor 60 Water level sensor 62 Control circuit 70 Cylindrical casing 70a Inlet port 70b Outlet port 72 Tubular water flow channel 74 Composite Polymer gel (PVA gel) 76 Filter 78 Water retention part 80 Cylindrical casing 80a Inlet 80b Outlet 82 Winding filter 84 Cylindrical core 84a Hollow part 84b Through hole 86 Linear material 88 Normally closed valve 89 Valve drive circuit 9 The compression spring 92 electric heater 93 heater drive circuit 94 display 95 display driving circuit 96 ozonizer 97 ozonizer driving circuit 98 memory (RAM) 99 Solenoid valve

Claims (13)

【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、 この汚染液体に含まれる汚染物質を捕集・濾過する物理
濾過手段とを備え、 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 circulating liquid purification apparatus for contaminated liquid, wherein liquid contaminated with time is stored in a liquid storage means, and the contaminated liquid is purified while being circulated by a pump outside the storage means. A microbial purification means for decomposing and purifying organic matter contained in the liquid by microorganisms and a physical filtration means for collecting and filtering the pollutants contained in the contaminated liquid are provided, and each of these means is provided with a circulation path of the contaminated liquid. A circulating purification device for contaminated liquid, characterized by being connected internally.
【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、 この汚染液体に含まれる汚染物質を捕集・濾過する物理
濾過槽とを備え、 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 circulating liquid purification apparatus for contaminated liquid, wherein a liquid contaminated with time is stored in a liquid storage tank, and the contaminated liquid is purified 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 substances contained in a liquid to purify it, and a physical filtration tank that collects and filters pollutants contained in the contaminated liquid. And a circulation purification apparatus for polluted liquid, characterized in that each of these tanks is connected in a circulating path for the polluted liquid.
【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】 前記物理濾過槽への汚染液体の流入路に
は、該物理濾過槽を回避して下流側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 circulation of the contaminated liquid according to claim 2, wherein the inflow path of the contaminated liquid to the physical filtration tank is provided with a bypass flow path that is connected to a downstream side while avoiding the physical filtration tank. Purification device.
【請求項7】 前記物理濾過槽は、中空部に多数の通孔
を有するコアに線状素材を巻回してなるワインディング
フィルタが濾過材として装填され、該物理濾過槽に流入
する汚染液体は、主として該フィルタに外周から流入し
て濾過された後に前記コアの通孔および中空部を経て流
出し、また該フィルタでの通水抵抗が増大するにつれ
て、前記フィルタおよびコアの通孔を介することなく前
記中空部のみから流出する汚染液体の割合も増加するよ
うになっている請求項2または6に記載の汚染液体の循
環浄化装置。
7. The physical filtration tank is loaded with a winding filter, which is obtained by winding a linear material around a core having a large number of through holes in a hollow portion, as a filtering material, and the contaminated liquid flowing into the physical filtration tank is Mainly flows into the filter from the outer periphery, is filtered and then flows out through the through hole and the hollow portion of the core, and as the water flow resistance in the filter increases, without passing through the through hole of the filter and the core. 7. The contaminated liquid circulation purification apparatus according to claim 2, wherein the ratio of the contaminated liquid flowing out only from the hollow portion is also increased.
【請求項8】 前記ワインディングフィルタの中空コア
は、その一方の開口部にバネ圧で常には該開口部を開成
する弁体を備え、該フィルタの目詰まりにより液体通過
時の抵抗が増大するにつれて、前記物理濾過槽に流入す
る汚染液体の圧力も次第に増加し、この圧力増加に伴い
前記弁体が前記バネ圧に抗して次第に開放することによ
り、前記フィルタおよびコアの通孔を介することなく該
開口部からコア中空部のみを経て流出する汚染液体の割
合も増加す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 winding core of the winding filter is provided with a valve element at one of its openings which constantly opens the opening with spring pressure, and as the filter becomes clogged, the resistance at the passage of liquid increases. The pressure of the contaminated liquid flowing into the physical filtration tank also gradually increases, and with this increase in pressure, the valve body gradually opens against the spring pressure, without passing through the through hole of the filter and the core. 8. The circulating purification apparatus for polluted liquid according to claim 2, wherein the proportion of the polluted liquid flowing out from the opening only through the hollow core portion is increased.
【請求項9】 前記ワインディングフィルタは、その線
状素材の巻回ピッチが粗なものと密なものとになるよう
区分けし、該フィルタの経時的な目詰まりに伴なう液体
通過抵抗の増大時期を調節し得るようにした請求項2,
6,7および8の何れかに記載の汚染液体の循環浄化装
置。
9. The winding filter is divided so that the winding pitch of its linear material is coarse and dense, and the liquid passage resistance increases with the clogging of the filter over time. Claim 2 wherein the timing can be adjusted,
6. The circulating purification apparatus for contaminated liquid according to any one of 6, 7, and 8.
【請求項10】 前記汚染液体が循環する方向に、前記
物理濾過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。
10. The circulating purification apparatus for polluted liquid according to claim 2, wherein the physical filtration tank and the microbial purification tank are sequentially arranged in a direction in which the polluted liquid circulates.
【請求項11】 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物理濾過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。
11. The contaminated liquid circulation purification apparatus according to claim 2, wherein the microbial purification tank and the physical filtration tank are arranged in order in a direction in which the contaminated liquid circulates.
【請求項12】 前記微生物浄化槽および物理濾過槽を
連通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に記載の汚染液体の循環浄化装置。
12. The circulation purification apparatus for polluted liquid according to claim 2, wherein an ozone generator is arranged at an appropriate position in a liquid circulation path that connects the microorganism purification tank and the physical filtration tank.
【請求項13】 前記微生物浄化槽および物理濾過槽が
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。
13. The circulation of the 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 the liquid circulation path communicating with the microbial purification tank and the physical filtration tank. Purification device.
JP7326368A 1995-10-23 1995-11-20 Circulating and purifying apparatus for contaminated solution Pending JPH09174080A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7326368A JPH09174080A (en) 1995-10-23 1995-11-20 Circulating and purifying apparatus for contaminated solution

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP27415795 1995-10-23
JP7-274157 1995-10-23
JP7326368A JPH09174080A (en) 1995-10-23 1995-11-20 Circulating and purifying apparatus for contaminated solution

Publications (1)

Publication Number Publication Date
JPH09174080A true JPH09174080A (en) 1997-07-08

Family

ID=26550918

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7326368A Pending JPH09174080A (en) 1995-10-23 1995-11-20 Circulating and purifying apparatus for contaminated solution

Country Status (1)

Country Link
JP (1) JPH09174080A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190099662A (en) * 2018-02-19 2019-08-28 (주)넥썸 Apparatus for removing moisture of cooling fluid for chiller

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190099662A (en) * 2018-02-19 2019-08-28 (주)넥썸 Apparatus for removing moisture of cooling fluid for chiller

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