JPH10309412A - Circulating purification facility - Google Patents

Circulating purification facility

Info

Publication number
JPH10309412A
JPH10309412A JP9117716A JP11771697A JPH10309412A JP H10309412 A JPH10309412 A JP H10309412A JP 9117716 A JP9117716 A JP 9117716A JP 11771697 A JP11771697 A JP 11771697A JP H10309412 A JPH10309412 A JP H10309412A
Authority
JP
Japan
Prior art keywords
purification
flow path
flow rate
roughness
trapping
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
JP9117716A
Other languages
Japanese (ja)
Inventor
Makoto Goto
誠 後藤
Masayuki Arakawa
眞行 荒川
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 JP9117716A priority Critical patent/JPH10309412A/en
Publication of JPH10309412A publication Critical patent/JPH10309412A/en
Pending legal-status Critical Current

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  • Filtration Of Liquid (AREA)

Abstract

PROBLEM TO BE SOLVED: To maintain a stable capture filtration capacity for a period of long time by the method wherein in a circulation purification facility to which a purification means of a different trapping mesh is arranged, a stable flow rate is made to flow to a purification means of a fine trapping mesh. SOLUTION: A purification tank 7a constitutes a purification means of a fine trapping mesh, and a purification tank 7b constitutes respectively a purification means of a rough trapping mesh. The purification tank 7a in order to improve a physical filtration capacity, and the purification tank 7b in order to make difficult to be clogged are suitable for securing a circulation flow rate. Then, to a downstream of the purification tank 7a, a constant flow rate valve 8a for making a stable flow rate flow to the purification tank 7a is arranged. When a power source is made to a circulating clarification facility main body 5, a circulation pump 6 is operated, bathing water in a bath tank 1 is sucked from a suction opening 2b through a water feed hose 3, sent to the purification tanks 7a, 7b, and purified. Since a constant flow rate valve 8a is arranged to the downstream of the purification tank 7a on which a spool filter of a fine mesh size is mounted, and a flow rate flowing to the purification tank 7a is specified, a stable flow rate flows to the purification tank 7b.

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、循環浄化装置に
関し、さらに詳細には、浴槽中の浴用水やプール中の温
水のように、使用により経時的に汚染される液体を循環
させながら、浄化をするための家庭用、業務用の循環浄
化装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a circulating purification apparatus, and more particularly to a circulating purification apparatus for circulating a liquid contaminated with use over time, such as bath water in a bathtub or hot water in a pool. The present invention relates to a circulating purification device for home use and business use.

【0002】[0002]

【従来の技術】従来、循環ポンプにより浴用水を循環さ
せ、浄化手段により浴用水の浄化を行う循環浄化装置に
おいては、浄化能力と循環流量を共に確保するために捕
捉粗さの異なる浄化手段を配設し、捕捉粗さの細かい浄
化手段に浄化能力の確保を期待し、捕捉粗さの粗い浄化
手段に循環流量の確保を期待していた。
2. Description of the Related Art Conventionally, in a circulating purifying apparatus in which bath water is circulated by a circulation pump and purifying water is purified by a purifying means, purifying means having different capture roughness are used in order to secure both the purifying ability and the circulating flow rate. It was expected that the purifying means with the fine trapped roughness would be able to secure the purification capacity, and the purifying means with the coarse trapped roughness would be required to secure the circulation flow rate.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、捕捉粗
さの細かい浄化手段は使用初期には浄化能力と共に流量
も多く確保できるが、流量が多く確保できるということ
は、それだけ汚物を早期に補集していることに繋がり、
短期間で目詰まりを起こして流量が確保できなくなると
共に、濾過も行われなくなるといった問題点があった。
However, the purifying means having a fine trapping roughness can secure a large flow rate in addition to the purifying ability in the early stage of use, but the fact that a large flow rate can be secured means that the waste is collected earlier. That leads to
There has been a problem that clogging occurs in a short period of time, so that a flow rate cannot be secured and filtration is not performed.

【0004】そこで、本発明は、捕捉粗さの細かい浄化
手段に安定した流量を流すことにより、安定した補集濾
過能力を長期に亘り維持することができる循環浄化装置
を提供することを目的としている。
Accordingly, an object of the present invention is to provide a circulating purification apparatus capable of maintaining a stable collection and filtration capability for a long period of time by flowing a stable flow rate through a purification means having a small capture roughness. I have.

【0005】[0005]

【課題を解決するための手段】この目的を達成するため
に、本発明の請求項1に記載の循環浄化装置は、液体を
循環させる循環流路内に捕捉粗さの粗い浄化手段と捕捉
粗さの細かい浄化手段とを配設したものを対象として、
特に、前記捕捉粗さの細かい浄化手段に関連させて液体
の流量を一定に保持するための定流量弁を設けている。
従って、捕捉粗さの細かい浄化手段を流れる流量が安定
し、長期に亘り安定した補集濾過能力が維持される。
In order to achieve the above object, a circulation purifying apparatus according to a first aspect of the present invention comprises a purifying means having a coarse trapping roughness in a circulation flow path for circulating a liquid. For those equipped with fine purification means,
In particular, a constant flow valve is provided for keeping the flow rate of the liquid constant in connection with the purifying means having a fine trapping roughness.
Therefore, the flow rate through the purifying means having a small trapping roughness is stabilized, and a stable collection and filtering ability is maintained for a long period of time.

【0006】また、請求項2に記載の循環浄化装置は、
前記循環流路に、それぞれ始端及び終端がその循環流路
に接続され、且つ捕捉粗さの細かい浄化手段を有する第
一の流路と、捕捉粗さの粗い浄化手段を有する第二の流
路とを並列に設け、前記定流量弁は、前記第一の流路に
設けられている。従って、前記第一の流路に設けられた
捕捉粗さの細かい浄化手段を流れる流量が安定し、長期
に亘り安定した補集濾過能力が維持されるとともに、前
記第二の流路により循環流量が確保される。
[0006] The circulating purification device according to claim 2 is
In the circulation flow path, the first end and the end are connected to the circulation flow path, respectively, and a first flow path having a purifying means with fine trapping roughness, and a second flow path having a purifying means with coarse trapping roughness Are provided in parallel, and the constant flow valve is provided in the first flow path. Accordingly, the flow rate through the purifying means having a small capture roughness provided in the first flow path is stabilized, and the collection and filtration capacity is maintained for a long period of time. Is secured.

【0007】また、請求項3に記載の循環浄化装置は、
前記循環流路に、それぞれ始端及び終端がその循環流路
に接続され、且つ捕捉粗さの細かい浄化手段を有する浄
化流路と、その捕捉粗さの細かい浄化手段を迂回するバ
イパス流路とを並列に設け、前記定流量弁は、前記浄化
流路に設けられている。従って、前記浄化流路に設けら
れた捕捉粗さの細かい浄化手段を流れる流量が安定し、
長期に亘り安定した補集濾過能力が維持されるととも
に、前記バイパス流路により循環流量が確保される。
[0007] The circulating purification apparatus according to claim 3 is
In the circulating flow path, the starting end and the end are connected to the circulating flow path, respectively, and a purifying flow path having a purifying means with a fine trapping roughness, and a bypass flow path bypassing the purifying means with a fine trapping roughness. Provided in parallel, the constant flow valve is provided in the purification flow path. Therefore, the flow rate through the purifying means having a small capture roughness provided in the purifying flow path is stable,
A stable collection and filtration capacity is maintained over a long period of time, and a circulation flow rate is secured by the bypass flow path.

【0008】また、請求項4に記載の循環浄化装置は、
前記循環流路に、前記定流量弁とは異なる他の定流量弁
を備えている。従って、前記循環流路を流れる総循環流
量が安定し、前記捕捉粗さの粗い浄化手段を流れる流量
も安定するので、その捕捉粗さの粗い浄化手段の補集濾
過能力も長期に亘り維持される。
[0008] The circulation purifying apparatus according to claim 4 is
The circulation flow path is provided with another constant flow valve different from the constant flow valve. Therefore, the total circulating flow rate flowing through the circulation flow path is stabilized, and the flow rate flowing through the purifying means having the coarse trapping roughness is also stabilized, so that the collection and filtering capacity of the purifying means having the coarse trapping roughness is also maintained for a long time. You.

【0009】[0009]

【発明の実施の形態】以下に、本発明の循環浄化装置に
ついて、好適な実施の形態を挙げて、添付図面を参照し
ながら以下説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, a circulating purification apparatus according to the present invention will be described with reference to the accompanying drawings by way of preferred embodiments.

【0010】図1は、発明の第一の実施の形態の循環浄
化装置の概略構成を示している。この装置は、浴槽1に
貯留されて経時的に汚染される浴用水を、この浴槽1の
外部でポンプ循環させながら浄化を行なうものである。
FIG. 1 shows a schematic configuration of a circulation purifying apparatus according to a first embodiment of the present invention. This apparatus purifies bath water which is stored in the bathtub 1 and is polluted with time while being pumped outside the bathtub 1.

【0011】すなわち、本実施の形態の循環浄化装置
は、温水貯留槽としての浴槽1に着脱自在に配設される
給排水ユニット2と、この給排水ユニット2に給水ホー
ス3と排水ホース4を介して接続する装置本体5とから
基本的に構成されている。
That is, the circulating purification apparatus of the present embodiment comprises a water supply / drainage unit 2 which is detachably disposed in a bathtub 1 as a hot water storage tank, and a water supply / drainage unit 2 which is connected to the water supply / drainage unit 2 via a water supply hose 3 and a drainage hose 4. It is basically composed of an apparatus main body 5 to be connected.

【0012】給排水ユニット2は、浴槽1の内壁面に着
脱自在に取り付けられ、浴用水の一般的な貯留水位より
下方に位置している。この給排水ユニット2は、装置本
体5内で浄化、殺菌された浴用水を浴槽1に戻す吐出口
2aと浴槽1より浴用水を吸い出す吸い込み口2bとか
ら構成されている。
The water supply / drainage unit 2 is detachably attached to the inner wall surface of the bathtub 1 and is located below a general storage level of bath water. The water supply / drain unit 2 includes a discharge port 2 a for returning bath water purified and sterilized in the apparatus main body 5 to the bathtub 1, and a suction port 2 b for sucking bathwater from the bathtub 1.

【0013】この給排水ユニット2内部では、浴用水を
装置本体5へ供給する給水ホース3が吸い込み口2b
に、また、装置本体5から浄化された浴用水を還流させ
るための排水ホース4が吐出口2aにそれぞれ接続され
て構成されている。これにより、後述の循環浄化装置を
稼働させた際に、浴槽1中の浴用水が循環ポンプ6によ
り吸い込み口2bと給水ホース3を介して装置本体5に
流入し、ここで浄化及び殺菌された後に、排水ホース4
及び吐出口2aを介して再び浴槽1に戻って循環するよ
うになっている。尚、給水ホース3及び排水ホース4は
本発明の循環流路を構成するものである。
In the water supply / drainage unit 2, a water supply hose 3 for supplying bath water to the apparatus main body 5 has a suction port 2b.
Further, a drain hose 4 for circulating purified bath water from the apparatus main body 5 is connected to the discharge port 2a. Thereby, when a circulating purification device described later is operated, bath water in the bathtub 1 flows into the device body 5 through the suction port 2b and the water supply hose 3 by the circulating pump 6, and is purified and sterilized therein. Later, drain hose 4
And circulates back to the bathtub 1 again through the discharge port 2a. In addition, the water supply hose 3 and the drainage hose 4 constitute a circulation channel of the present invention.

【0014】装置本体5には、図1に示すように、浴槽
1から浴用水を汲み上げ循環させる循環ポンプ6と、浴
用水に含まれる有機物やその他の汚染物質を吸着、分
解、濾過等により浄化する浄化槽7a、7bとを備えて
いる。そして、前記浄化槽7a、7bは、それぞれ並列
に設けられた第一の流路21、第二の流路22に配設さ
れている。この浄化槽7a、7bには糸巻きフィルター
が装填され、その巻回密度は浄化槽7aには10μm程
度の捕捉粗さのものを、7bには150μm程度の捕捉
粗さのものを採用している。つまり、浄化槽7aは物理
濾過能力向上に、7bは目詰まりが起こりにくく循環流
量の確保に適している。浄化槽7aの下流には、浄化槽
7aに安定した流量を流すための定流量弁8aが配設さ
れている。尚、浄化槽7aは本発明の捕捉粗さの細かい
浄化手段を、浄化槽7bは捕捉粗さの粗い浄化手段をそ
れぞれ構成するものである。
As shown in FIG. 1, a circulating pump 6 for pumping and circulating bath water from a bathtub 1 and purifying organic substances and other contaminants contained in the bath water by adsorption, decomposition, filtration, etc., as shown in FIG. Purification tanks 7a and 7b. The septic tanks 7a and 7b are arranged in a first flow path 21 and a second flow path 22 provided in parallel, respectively. The septic tanks 7a and 7b are loaded with a thread-wound filter, and the winding density of the septic tank 7a is about 10 μm and the trapping density is about 150 μm. In other words, the septic tank 7a is suitable for improving the physical filtration capacity, and the septic tank 7b is suitable for preventing clogging and ensuring a circulating flow rate. Downstream of the septic tank 7a, a constant flow valve 8a for flowing a stable flow rate to the septic tank 7a is provided. The septic tank 7a constitutes a purifying means of the present invention with fine trapping roughness, and the septic tank 7b constitutes a purifying means with coarse trapping roughness.

【0015】浄化槽7aと7bとの分流点の上流には、
三方弁9a、同じく、合流点の下流には三方弁9bが配
設され、三方弁9aの上流で分流し、浄化槽7a、7b
をバイパスする逆洗流路10が三方弁9bに連通し、三
方弁9aには排水流路11が配設されている。三方弁9
a、bにより通常流路が設定されているときは、循環ポ
ンプ6から吐出された浴用水は、三方弁9aを通って浄
化槽7a、7bに流入し、そこで不純物が除去された
後、三方弁9bを通って後述の流量調節弁12に至る。
一方、逆洗流路が設定されているときは、図2に示すよ
うに、循環ポンプ6から吐出された浴用水は、逆洗流路
10を流れ、三方弁9bから浄化槽7a,7bに流れ
る。浴用水はフィルターに目詰まりした不純物を除去
し、これと共に三方弁9aから排水流路11を流れ外部
に流出する。
Upstream of the branch point between the septic tanks 7a and 7b,
Similarly, a three-way valve 9a is provided downstream of the junction, and a three-way valve 9b is diverted upstream of the three-way valve 9a.
A backwash flow path 10 that bypasses the flow path communicates with the three-way valve 9b, and a drain water flow path 11 is provided in the three-way valve 9a. Three-way valve 9
When the normal flow path is set by a and b, the bath water discharged from the circulation pump 6 flows into the purification tanks 7a and 7b through the three-way valve 9a, and after the impurities are removed there, the three-way valve Through 9b, the flow reaches a flow control valve 12 described later.
On the other hand, when the backwash channel is set, as shown in FIG. 2, bath water discharged from the circulation pump 6 flows through the backwash channel 10 and flows from the three-way valve 9b to the purification tanks 7a and 7b. . The bath water removes impurities clogged in the filter, and at the same time, flows through the drain passage 11 from the three-way valve 9a to the outside.

【0016】また、装置本体5には、通常循環する浴用
水の一部を殺菌温度75℃以上に加熱する加熱手段とし
ての加熱槽13と、加熱された浴用水を所定時間1分間
以上殺菌温度に保持し殺菌を行う殺菌手段としての殺菌
槽14を配設した流路15と、この加熱槽13を回避し
て殺菌槽14より下流側に連通する流路16を備えてい
る。流路15と流路16との分岐点には流量調節弁12
が設けられており、この流量調節弁12により流路1
5、流路16への流量がそれぞれ調節される。前記三方
弁9a、b、循環ポンプ6、加熱槽13は図示外の制御
回路に接続されており、装置の起動停止、温水の殺菌処
理、逆洗排水処理等、種々の目的のために個別に制御さ
れる。
The apparatus main body 5 has a heating tank 13 as a heating means for heating a part of the circulating bath water to a sterilizing temperature of 75 ° C. or higher, and a sterilizing temperature of at least one minute for the heated bath water. And a flow path 16 provided with a sterilization tank 14 as sterilization means for holding and sterilizing, and a flow path 16 avoiding the heating tank 13 and communicating downstream from the sterilization tank 14. A flow control valve 12 is provided at a branch point between the flow path 15 and the flow path 16.
The flow control valve 12 controls the flow path 1.
5. The flow rate to the flow path 16 is adjusted respectively. The three-way valves 9a, b, the circulation pump 6, and the heating tank 13 are connected to a control circuit (not shown), and are individually provided for various purposes such as starting and stopping the apparatus, sterilizing warm water, and performing backwashing and draining. Controlled.

【0017】ところで、本実施の形態では、加熱槽13
内に設置されたヒーター13aへの通電時は常に75℃
以上の浴用水が生成されるとともに、流路16を流れる
浴用水との合流後には、入浴可能な適温となるように、
流路15と流路16に対する浴用水の分配比が流量調節
弁12により調節され、ヒーター13aに印加する電圧
あるいは電流の値が制御される。
In the present embodiment, the heating tank 13
75 ° C when power is supplied to the heater 13a
The above bath water is generated, and after merging with the bath water flowing through the flow path 16, the bathing water is adjusted to an appropriate temperature so that it can be bathed.
The distribution ratio of the bath water to the flow path 15 and the flow path 16 is adjusted by the flow control valve 12, and the value of the voltage or current applied to the heater 13a is controlled.

【0018】次に、前記各構成の動作について説明す
る。
Next, the operation of each component will be described.

【0019】図1において、装置本体5に電源が投入さ
れると、循環ポンプ6が稼働し、浴槽1中の浴用水が、
吸い込み口2bから給水ホース3を通り吸い込まれ、浄
化槽7a、7bに送られ浄化される。目の細かい糸巻き
フィルターが装填された浄化槽7aの下流には定流量弁
8aが配設され、安定した流量が流れる。これにより、
浄化槽7aは長期に亘り安定した補集濾過能力を発揮す
る。
In FIG. 1, when the power is turned on to the apparatus main body 5, the circulating pump 6 is operated, and the bath water in the bathtub 1 is discharged.
The water is sucked through the water supply hose 3 from the suction port 2b and sent to the purification tanks 7a and 7b for purification. A constant flow rate valve 8a is provided downstream of the septic tank 7a loaded with a finely wound filter, so that a stable flow rate flows. This allows
The septic tank 7a exhibits a stable collection and filtering ability over a long period of time.

【0020】逆洗運転時は、浴用水が逆洗流路10を流
れ、三方弁9bから、浄化槽7a、7bへ逆方向から流
入する。このとき、循環ポンプ6から吐出された浴用水
は、フィルターに付着した汚物を除去し三方弁9aから
排水流路11を流れ外部に流出する。
During the backwash operation, bath water flows through the backwash channel 10 and flows from the three-way valve 9b into the purification tanks 7a and 7b from the opposite direction. At this time, the bath water discharged from the circulation pump 6 removes dirt adhering to the filter, flows through the drain passage 11 from the three-way valve 9a, and flows out to the outside.

【0021】ところで、通常運転時、浄化された浴用水
の一部は、流路15を流れ、加熱槽13で所定の殺菌温
度75℃以上に加熱され、殺菌槽14に一時的に貯留さ
れる。このため、加熱槽13で加熱されてから流路16
に合流するまでの時間(例えば1分間以上)殺菌温度の
75℃に維持することができるので、確実に殺菌するこ
とができる。
During normal operation, a part of the purified bath water flows through the flow path 15, is heated to a predetermined sterilization temperature of 75 ° C. or higher in the heating tank 13, and is temporarily stored in the sterilizing tank 14. . Therefore, after being heated in the heating tank 13, the flow path 16
Since it can be maintained at the sterilization temperature of 75 ° C. (for example, 1 minute or more) until it merges with the water, sterilization can be surely performed.

【0022】一方、流路16を流れる浴用水は、殺菌槽
14の下流で流路15と合流し、入浴可能な適温40℃
程度になり、排水ホース4を流れ、吐出口2aから浴槽
1へと環流する。このため、熱殺菌を行いながら、多量
の浴用水を循環させることができる。
On the other hand, the bath water flowing through the flow path 16 joins the flow path 15 downstream of the sterilization tank 14 and has a suitable temperature of 40 ° C.
It flows through the drain hose 4 and returns to the bathtub 1 from the discharge port 2a. Therefore, a large amount of bath water can be circulated while performing heat sterilization.

【0023】次に、本発明の第二の実施の形態について
説明する。
Next, a second embodiment of the present invention will be described.

【0024】図3は、第二の実施の形態の循環浄化装置
の概略構成を示している。
FIG. 3 shows a schematic configuration of a circulation purification apparatus according to the second embodiment.

【0025】ここでは、先述の実施の形態とは異なる浄
化槽及び定流量弁の配置について説明する。
Here, the arrangement of the septic tank and the constant flow valve different from the above-described embodiment will be described.

【0026】循環ポンプ6の下流には、浄化槽7aを有
する浄化流路23と、前記浄化槽を迂回するために前記
浄化流路23とは並列に設けられたバイパス流路24と
を設け、これらに対し直列に浄化槽7bが配設されてい
る。浄化流路23には定流量弁8aが設けられ、通過流
量が一定に保たれている。前記浄化槽7bの下流側に
は、総循環流量が規制されるように定流量弁8bが配設
されている。
Downstream of the circulation pump 6, there is provided a purification passage 23 having a purification tank 7a, and a bypass passage 24 provided in parallel with the purification passage 23 to bypass the purification tank. On the other hand, a septic tank 7b is arranged in series. The purification flow path 23 is provided with a constant flow rate valve 8a, and the flow rate is kept constant. A constant flow valve 8b is provided downstream of the septic tank 7b so that the total circulation flow is regulated.

【0027】次に、前記構成の動作について説明する。Next, the operation of the above configuration will be described.

【0028】図3において、循環ポンプ6から送り出さ
れた浴用水は、三方弁9aを通り分流され、一部が浄化
槽7aにより濾過される。浄化槽7aの下流には定流量
弁8aが配設され、浄化槽7aを流れる流量が規定され
ているので、長期に亘り安定した補集濾過能力を得られ
る。ここで濾過された浴用水は、浄化槽7aをバイパス
した浴用水と合流した後、浄化槽7bに通水され、比較
的大きめの汚物が補集濾過される。浄化槽7bの下流に
配設された定流量弁8bにより、浄化槽7bには安定し
た流量が流れるため、長期に亘り安定した補集濾過能力
と、総循環流量を維持することができる。
In FIG. 3, the bath water sent from the circulation pump 6 is diverted through a three-way valve 9a, and a part of the water is filtered by a purification tank 7a. The constant flow rate valve 8a is provided downstream of the septic tank 7a, and the flow rate flowing through the septic tank 7a is regulated, so that a stable collection and filtering ability can be obtained over a long period of time. The filtered bath water joins the bath water that bypasses the septic tank 7a, and then flows through the septic tank 7b, where relatively large waste is collected and filtered. The constant flow rate valve 8b provided downstream of the septic tank 7b allows a stable flow rate to flow through the septic tank 7b, so that a stable collection and filtration capacity and a total circulation flow rate can be maintained over a long period of time.

【0029】本発明の構成は以上の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。
The configuration of the present invention is not limited to the above-described embodiment, and various changes can be made without departing from the scope of the invention.

【0030】例えば、本実施の形態では、浄化手段とし
て、糸巻きフィルターを採用したが、濾過材はこれに限
定されるものではなく、砂、珪藻土、麦飯石、セラミッ
クボール、活性炭等でも良い。
For example, in this embodiment, a thread-wound filter is used as the purifying means, but the filtering material is not limited to this, and may be sand, diatomaceous earth, barley stone, ceramic balls, activated carbon, or the like.

【0031】また、浄化槽7a、7bが配設された流路
に開閉弁等を設け個別に逆洗洗浄しても良い。
Further, an on-off valve or the like may be provided in the flow path in which the purification tanks 7a and 7b are provided, and backwashing may be individually performed.

【0032】また、浄化手段を3個以上配設しても良
い。
Further, three or more purifying means may be provided.

【0033】更に、第二の実施形態においては、浄化槽
7a、7bを直列に配設したが、図4に示すように、並
列に配設しても良い。この場合、定流量弁8bに関して
も浄化槽7bの直後に並列に配設しても良い。
Further, in the second embodiment, the septic tanks 7a and 7b are arranged in series, but they may be arranged in parallel as shown in FIG. In this case, the constant flow valve 8b may also be disposed in parallel immediately after the septic tank 7b.

【0034】[0034]

【発明の効果】以上説明したことから明らかなように、
本発明の請求項1に記載の循環浄化装置は、液体を循環
させる循環流路内に捕捉粗さの粗い浄化手段と捕捉粗さ
の細かい浄化手段とを配設したものを対象として、特
に、前記捕捉粗さの細かい浄化手段に関連させて液体の
流量を一定に保持するための定流量弁を設けている。従
って、捕捉粗さの細かい浄化手段を流れる流量が安定
し、長期に亘り安定した補集濾過能力が維持される。
As is apparent from the above description,
The circulating purification device according to claim 1 of the present invention is intended for a device in which a purifying means having a coarse trapping roughness and a purifying means having a fine trapping roughness are disposed in a circulation flow path for circulating a liquid, A constant flow valve for maintaining a constant flow rate of the liquid is provided in association with the purifying means having a fine trapping roughness. Therefore, the flow rate through the purifying means having a small trapping roughness is stabilized, and a stable collection and filtering ability is maintained for a long period of time.

【0035】また、請求項2に記載の循環浄化装置は、
前記循環流路に、それぞれ始端及び終端がその循環流路
に接続され、且つ捕捉粗さの細かい浄化手段を有する第
一の流路と、捕捉粗さの粗い浄化手段を有する第二の流
路とを並列に設け、前記定流量弁は、前記第一の流路に
設けられている。従って、前記第一の流路に設けられた
捕捉粗さの細かい浄化手段を流れる流量が安定し、長期
に亘り安定した補集濾過能力が維持されるとともに、前
記第二の流路により循環流量が確保される。
Further, the circulating purification device according to claim 2 is
In the circulation flow path, the first end and the end are connected to the circulation flow path, respectively, and a first flow path having a purifying means with fine trapping roughness, and a second flow path having a purifying means with coarse trapping roughness Are provided in parallel, and the constant flow valve is provided in the first flow path. Accordingly, the flow rate through the purifying means having a small capture roughness provided in the first flow path is stabilized, and the collection and filtration capacity is maintained for a long period of time. Is secured.

【0036】また、請求項3に記載の循環浄化装置は、
前記循環流路に、それぞれ始端及び終端がその循環流路
に接続され、且つ捕捉粗さの細かい浄化手段を有する浄
化流路と、その捕捉粗さの細かい浄化手段を迂回するバ
イパス流路とを並列に設け、前記定流量弁は、前記浄化
流路に設けられている。従って、前記浄化流路に設けら
れた捕捉粗さの細かい浄化手段を流れる流量が安定し、
長期に亘り安定した補集濾過能力が維持されるととも
に、前記バイパス流路により循環流量が確保される。
The circulating purification device according to claim 3 is
In the circulating flow path, the starting end and the end are connected to the circulating flow path, respectively, and a purifying flow path having a purifying means with a fine trapping roughness, and a bypass flow path bypassing the purifying means with a fine trapping roughness. Provided in parallel, the constant flow valve is provided in the purification flow path. Therefore, the flow rate through the purifying means having a small capture roughness provided in the purifying flow path is stable,
A stable collection and filtration capacity is maintained over a long period of time, and a circulation flow rate is secured by the bypass flow path.

【0037】また、請求項4に記載の循環浄化装置は、
前記循環流路に、前記定流量弁とは異なる他の定流量弁
を備えている。従って、前記循環流路を流れる総循環流
量が安定し、前記捕捉粗さの粗い浄化手段を流れる流量
も安定するので、その捕捉粗さの粗い浄化手段の補集濾
過能力も長期に亘り維持される。
Further, the circulation purifying apparatus according to claim 4 is
The circulation flow path is provided with another constant flow valve different from the constant flow valve. Therefore, the total circulating flow rate flowing through the circulation flow path is stabilized, and the flow rate flowing through the purifying means having the coarse trapping roughness is also stabilized, so that the collection and filtering capacity of the purifying means having the coarse trapping roughness is also maintained for a long time. You.

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

【図1】本発明の第一の実施の形態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 first embodiment of the present invention.

【図2】本発明の第一の実施の形態の浄化槽洗浄時のバ
ルブ位置を示す概略図である。
FIG. 2 is a schematic diagram showing a valve position at the time of cleaning the septic tank according to the first embodiment of the present invention.

【図3】本発明の第二の実施の形態の基本構成を示す概
略図である。
FIG. 3 is a schematic diagram showing a basic configuration of a second embodiment of the present invention.

【図4】本発明の第二の実施の形態の変形例の基本構成
を示す概略図である。
FIG. 4 is a schematic diagram showing a basic configuration of a modified example of the second embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 浴槽 3 給水ホース 4 排水ホース 5 装置本体 6 循環ポンプ 7a 浄化槽 7b 浄化槽 8a 定流量弁 8b 定流量弁 21 第一の流路 22 第二の流路 23 浄化流路 24 バイパス流路 DESCRIPTION OF SYMBOLS 1 Bath tub 3 Water supply hose 4 Drain hose 5 Device main body 6 Circulation pump 7a Purification tank 7b Purification tank 8a Constant flow valve 8b Constant flow valve 21 First flow path 22 Second flow path 23 Purification flow path 24 Bypass flow path

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 液体を循環させる循環流路内に捕捉粗さ
の粗い浄化手段と捕捉粗さの細かい浄化手段とを配設し
た循環浄化装置において、 前記捕捉粗さの細かい浄化手段に関連させて液体の流量
を一定に保持するための定流量弁を設けたことを特徴と
する循環浄化装置。
1. A circulating purification apparatus in which a purifying means having a coarse trapping roughness and a purifying means having a fine trapping roughness are arranged in a circulation flow path for circulating a liquid, wherein the purifying means is associated with the purifying means having a fine trapping roughness. And a constant flow valve for maintaining a constant flow rate of the liquid.
【請求項2】 前記循環流路に、それぞれ始端及び終端
がその循環流路に接続され、且つ捕捉粗さの細かい浄化
手段を有する第一の流路と、捕捉粗さの粗い浄化手段を
有する第二の流路とを並列に設け、 前記定流量弁は、前記第一の流路に設けられたことを特
徴とする請求項1に記載の循環浄化装置。
2. A circulating flow path having a first flow path having a starting end and an ending end connected to the circulating flow path, respectively, and having a purifying means with fine trapping roughness, and a purifying means with coarse trapping roughness. The circulating purification device according to claim 1, wherein a second flow path is provided in parallel, and the constant flow valve is provided in the first flow path.
【請求項3】 前記循環流路に、それぞれ始端及び終端
がその循環流路に接続され、且つ捕捉粗さの細かい浄化
手段を有する浄化流路と、その捕捉粗さの細かい浄化手
段を迂回するバイパス流路とを並列に設け、 前記定流量弁は、前記浄化流路に設けられたことを特徴
とする請求項1に記載の循環浄化装置。
3. A purifying flow channel having a purifying means having a fine trapping roughness, a starting end and a terminating end being connected to the circulating flow channel, respectively, and bypassing the purifying means having a fine trapping roughness. The circulation purification device according to claim 1, wherein a bypass flow path is provided in parallel, and the constant flow valve is provided in the purification flow path.
【請求項4】 前記循環流路には、前記定流量弁とは異
なる他の定流量弁を更に備えたことを特徴とする請求項
2若しくは3に記載の循環浄化装置。
4. The circulation purifying apparatus according to claim 2, wherein the circulation flow path further includes another constant flow valve different from the constant flow valve.
JP9117716A 1997-05-08 1997-05-08 Circulating purification facility Pending JPH10309412A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9117716A JPH10309412A (en) 1997-05-08 1997-05-08 Circulating purification facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9117716A JPH10309412A (en) 1997-05-08 1997-05-08 Circulating purification facility

Publications (1)

Publication Number Publication Date
JPH10309412A true JPH10309412A (en) 1998-11-24

Family

ID=14718534

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9117716A Pending JPH10309412A (en) 1997-05-08 1997-05-08 Circulating purification facility

Country Status (1)

Country Link
JP (1) JPH10309412A (en)

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