JPH10151483A - Purifying tank - Google Patents

Purifying tank

Info

Publication number
JPH10151483A
JPH10151483A JP31338296A JP31338296A JPH10151483A JP H10151483 A JPH10151483 A JP H10151483A JP 31338296 A JP31338296 A JP 31338296A JP 31338296 A JP31338296 A JP 31338296A JP H10151483 A JPH10151483 A JP H10151483A
Authority
JP
Japan
Prior art keywords
tank
treated
treated water
storage tank
water storage
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
JP31338296A
Other languages
Japanese (ja)
Inventor
Shinya Hirota
伸也 広田
Harumori Kawagoe
治衞 川越
Shin Matsugi
伸 真継
Takayoshi Nakaoka
敬善 中岡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Electric Works Co Ltd
Original Assignee
Matsushita Electric Works Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Works Ltd filed Critical Matsushita Electric Works Ltd
Priority to JP31338296A priority Critical patent/JPH10151483A/en
Publication of JPH10151483A publication Critical patent/JPH10151483A/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

Abstract

PROBLEM TO BE SOLVED: To surely adjust a treatment flow rate of treated water without hindrance. SOLUTION: This purifying tank is constituted so that a membrane separator 5 is provided within an aeration tank 4 aerobically and biologically treating water to be treated with activated sludge so as to be immersed in the water to be treated and a treated water storage tank 6 is provided so as to communicate with the aeration tank through the treated water piping 9 connected to the membrane separator and, further, the treated water storage tank communicates with a disinfection tank 8 through a discharge pipe 15 having a discharge pump 12 provided on the way thereof. In this case, a water level detection means 19 is provided to the treated water storage tank and a control part 10 controlling the operation of the discharge pump so as to realize the predetermined water head difference related to the aeration tank and the treated water storage tank on the basis of the water level detected by the water level detection means is provided.

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、浄化槽に関する
ものである。さらに詳しくは、この発明は、膜分離装置
が曝気槽と処理水貯留槽の水頭差を駆動源として被処理
水を固液分離し、処理水を処理水貯留槽に送る浄化槽に
おいて、処理水の処理流量を支障なく確実に調整するこ
とのできる浄化槽に関するものである。
TECHNICAL FIELD The present invention relates to a septic tank. More specifically, the present invention relates to a purification tank in which a membrane separation device separates water to be treated into solid and liquid by using a head difference between an aeration tank and a treated water storage tank as a driving source and sends the treated water to the treated water storage tank. The present invention relates to a septic tank capable of surely adjusting a processing flow rate without any trouble.

【0002】[0002]

【従来の技術】従来より、し尿や、日々の炊事、洗濯、
入浴等により生ずる生活雑排水をも浄化処理することの
できる浄化槽が提供されてきている。この浄化槽の一つ
に、たとえば図3に示した膜分離式の浄化槽がある。膜
分離式の浄化槽には、この図3に示すことができるよう
に、膜分離装置(5)が、活性汚泥により被処理水を好
気的に生物学的処理する曝気槽(4)に被処理水に浸漬
可能に内装されている。膜分離装置(5)は、曝気槽
(4)内の被処理水を固液分離するものであり、そのた
めの駆動源は、曝気槽(4)と処理水貯留槽(6)の間
の水頭差を利用している。この固液分離において、膜分
離装置(5)は、活性汚泥は曝気槽(4)に保持する一
方、濾過した膜透過液を処理水として、処理水配管
(9)を通じて曝気槽(4)に連通する処理水貯留槽
(6)に送る。
2. Description of the Related Art Conventionally, night soil, daily cooking, washing,
BACKGROUND ART Septic tanks capable of purifying household wastewater generated by bathing and the like have been provided. As one of the septic tanks, for example, there is a membrane separation type septic tank shown in FIG. As shown in FIG. 3, the membrane separation type septic tank is provided with a membrane separation device (5) in an aeration tank (4) for aerobically biologically treating the water to be treated with activated sludge. The interior is immersed in treated water. The membrane separation device (5) is for solid-liquid separation of the water to be treated in the aeration tank (4), and the driving source for the separation is a head between the aeration tank (4) and the treated water storage tank (6). Use the difference. In this solid-liquid separation, the membrane separation device (5) holds the activated sludge in the aeration tank (4) while treating the filtered membrane permeate as treated water into the aeration tank (4) through the treated water pipe (9). The water is sent to the treated water storage tank (6).

【0003】処理水は、次いで、処理水貯留槽(6)か
ら放流ポンプ(12)によって汲み上げられ、放流管
(15)を通じて消毒槽(8)に送られ、この後に槽外
に放流される。このような膜分離式の浄化槽には、沈殿
分離槽(1)及び嫌気濾床槽(2)が排水流入側に設け
られており、処理後には、処理水は、移送ポンプ(3)
により曝気槽(4)に送られる。符号14は、汚泥の移
送流路を形成する汚泥移送管である。
[0003] The treated water is then pumped up from a treated water storage tank (6) by a discharge pump (12), sent to a disinfection tank (8) through a discharge pipe (15), and then discharged outside the tank. In such a membrane type septic tank, a sedimentation separation tank (1) and an anaerobic filter bed tank (2) are provided on the drainage inflow side, and after treatment, treated water is transferred to a transfer pump (3).
To the aeration tank (4). Reference numeral 14 denotes a sludge transfer pipe that forms a transfer passage for sludge.

【0004】曝気槽(4)には、さらに、散気管(7)
が設けられてもおり、これに接続したブロア(16)か
ら送気された空気が、この散気管(7)を通じて曝気槽
(4)に送り込まれ、好気状態が形成されるようにして
いる。曝気槽(4)では、好気状態において被処理水の
活性汚泥処理が行われる。そして、浄化槽では、沈殿分
離槽(1)、嫌気濾床槽(2)及び曝気槽(4)の水位
を、嫌気濾床槽(2)及び曝気槽(4)の各々に設けた
水位検知手段(11)(13)で検知し、検知した水位
に応じて移送ポンプ(3)の動作を制御部(10)で制
御するようにしてもいる。制御部(10)には、移送ポ
ンプ(3)の動作制御の基準として、各槽(1)(2)
(4)における上下限水位(L1)(L2)が設定され
ている。
The aeration tank (4) further includes a diffuser (7)
Is provided, and the air sent from the blower (16) connected thereto is sent to the aeration tank (4) through the air diffuser (7) so that an aerobic state is formed. . In the aeration tank (4), activated sludge treatment of the water to be treated is performed in an aerobic state. In the septic tank, the water levels of the sedimentation separation tank (1), the anaerobic filter bed tank (2) and the aeration tank (4) are determined by water level detection means provided in each of the anaerobic filter tank (2) and the aeration tank (4). (11) The operation of the transfer pump (3) is controlled by the control unit (10) according to the detected water level detected by the control unit (13). The control unit (10) includes, as a reference for operation control of the transfer pump (3), each tank (1) (2)
The upper and lower water levels (L1) and (L2) in (4) are set.

【0005】[0005]

【発明が解決しようとする課題】たとえばこの図3に示
すことのできる従来の膜分離式の浄化槽は、前述の通り
に、膜分離装置(5)による被処理水の固液分離及び処
理水の処理水貯留槽(6)への移送の駆動源を曝気槽
(4)と処理水貯留槽(6)の間の水頭差から得ている
ため、ポンプ等の駆動手段が不要となり、構造が簡略化
され、コスト低減に寄与することができるという利点を
有しているが、その反面、被処理水の固液分離及び処理
水の移送は曝気槽(4)と処理水貯留槽(6)の間の水
頭差に左右される。水頭差が大きい場合には大きな駆動
力が得られるが、小さい場合には駆動力は低下する。し
たがって、処理水の処理流量を調整する場合には、その
調整は、曝気槽(4)と処理水貯留槽(6)の間の水頭
差を制御することによって実現することができる。
As shown in FIG. 3, for example, the conventional septic tank of the membrane separation type, as shown in FIG. Since the driving source for transfer to the treated water storage tank (6) is obtained from the head difference between the aeration tank (4) and the treated water storage tank (6), a driving means such as a pump is unnecessary, and the structure is simplified. And has the advantage of being able to contribute to cost reduction. On the other hand, the solid-liquid separation of the water to be treated and the transfer of the treated water are performed in the aeration tank (4) and the treated water storage tank (6). Between head differences. When the head difference is large, a large driving force is obtained, but when the difference is small, the driving force decreases. Therefore, when adjusting the treatment flow rate of the treated water, the adjustment can be realized by controlling the head difference between the aeration tank (4) and the treated water storage tank (6).

【0006】特開平6−218237号公報には、その
一方策として、集水口を上下に昇降自在としたオーバー
フロー管を膜分離槽に設け、その集水口の位置により膜
分離槽内の水位を調整することが開示されている。しか
しながら、膜分離槽、すなわち、曝気槽(4)内の被処
理水は高濃度の活性汚泥であるため、オーバーフロー管
には目詰まりが発生しやすく、確実な水位調整は難しい
という問題がある。
Japanese Unexamined Patent Publication No. Hei 6-218237 discloses, as one of the measures, an overflow pipe having a water collecting port capable of moving up and down in a membrane separation tank, and adjusting the water level in the membrane separation tank according to the position of the water collecting port. Is disclosed. However, since the water to be treated in the membrane separation tank, that is, the aeration tank (4) is activated sludge having a high concentration, the overflow pipe is liable to be clogged, and there is a problem that it is difficult to reliably control the water level.

【0007】この発明は、以上の通りの事情に鑑みてな
されたものであり、従来の浄化槽における処理水の流量
調整についての課題を解決し、処理水の処理流量を支障
なく確実に調整することのできる浄化槽を提供すること
を目的としている。
SUMMARY OF THE INVENTION The present invention has been made in view of the circumstances described above, and has been made to solve the problem of adjusting the flow rate of treated water in a conventional septic tank, and to surely adjust the treated flow rate of treated water without hindrance. It aims to provide a septic tank that can be used.

【0008】[0008]

【課題を解決するための手段】この発明は、上記の課題
を解決するものとして、被処理水を活性汚泥により好気
的に生物学的処理する曝気槽に、膜分離装置が被処理水
に浸漬可能に内装され、この膜分離装置に接続された処
理水配管を介して処理水貯留槽が曝気槽と連通して設け
られ、さらに処理水貯留槽は、放流ポンプを管路途中に
設けた放流管を介して消毒槽に連通し、前記膜分離装置
は、曝気槽と処理水貯留槽の間の水頭差を駆動源として
被処理水を固液分離し、処理水を処理水貯留槽に送る一
方、活性汚泥は曝気槽に保持する浄化槽において、処理
水貯留槽に水位検知手段が設けられ、この水位検知手段
による水位検知に基づいて、曝気槽と処理水貯留槽に関
する予め定められた設定水頭差が実現されるように前記
放流ポンプの動作を制御する制御部が設けられているこ
とを特徴とする浄化槽を提供する(請求項1)。
The present invention solves the above-mentioned problems by providing an aeration tank for aerobically biologically treating water to be treated with activated sludge, and a membrane separation device for treating water to be treated. A treated water storage tank is provided in communication with the aeration tank through a treated water pipe connected to the membrane separation device, and the treated water storage tank is provided with a discharge pump in the middle of the pipeline. The membrane separation device communicates with the disinfection tank via a discharge pipe, and the membrane separation device performs solid-liquid separation of the water to be treated using the head difference between the aeration tank and the treated water storage tank as a driving source, and transfers the treated water to the treated water storage tank. On the other hand, the activated sludge is held in the aeration tank, and in the purification tank, a water level detecting means is provided in the treated water storage tank. Based on the water level detection by the water level detecting means, predetermined settings for the aeration tank and the treated water storage tank are set. Operation of the discharge pump so that a head difference is realized To provide a septic tank, characterized in that the control unit that controls are provided (claim 1).

【0009】またこの発明は、被処理水を活性汚泥によ
り好気的に生物学的処理する曝気槽に、膜分離装置が被
処理水に浸漬可能に内装され、この膜分離装置に接続さ
れた処理水配管を介して処理水貯留槽が曝気槽と連通し
て設けられ、さらに処理水貯留槽は、放流ポンプを管路
途中に設けた放流管を介して消毒槽に連通し、前記膜分
離装置は、曝気槽と処理水貯留槽の間の水頭差を駆動源
として被処理水を固液分離し、処理水を処理水貯留槽に
送る一方、活性汚泥は曝気槽に保持する浄化槽におい
て、処理水配管の管路途中に流量検知手段が設けられ、
この流量検知手段による処理流量の検知に基づいて、予
め定められた設定流量が実現されるように前記放流ポン
プの動作を制御する制御部が設けられていることを特徴
とする浄化槽を提供するものでもある(請求項2)。
According to the present invention, a membrane separation device is provided in an aeration tank for aerobically biologically treating the water to be treated with activated sludge so as to be immersed in the water to be treated, and is connected to the membrane separation device. A treated water storage tank is provided in communication with the aeration tank via a treated water pipe, and the treated water storage tank is further connected to a disinfection tank through a discharge pipe provided in the middle of the pipe, and the membrane separation is performed. The apparatus separates the water to be treated into solid and liquid by using the head difference between the aeration tank and the treated water storage tank as a driving source and sends the treated water to the treated water storage tank, while the activated sludge is held in the aeration tank in a purification tank. Flow rate detecting means is provided in the middle of the treated water pipe,
A purifying tank provided with a control unit for controlling the operation of the discharge pump so that a predetermined set flow rate is realized based on the detection of the processing flow rate by the flow rate detection means. (Claim 2).

【0010】[0010]

【発明の実施の形態】以下、図面に沿って実施例をも示
しつつ、この発明の浄化槽についてさらに詳しく説明す
る。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the septic tank of the present invention will be described in more detail with reference to the accompanying drawings and embodiments.

【0011】[0011]

【実施例】図1は、この発明の浄化槽の一実施例を示し
た構成図である。たとえばこの図1に示した例において
は、図3に示した従来型の浄化槽を踏襲しつつ、一部改
良が加えられている。すなわち、処理水貯留槽(6)に
水位検知手段(19)が設けられている。制御部(1
0)は、この水位検知手段(19)で検知した水位検知
に基づいて放流ポンプ(12)の動作を制御する。制御
部(10)には、曝気槽(4)と処理水貯留槽(6)に
関して所定の水頭差が予め設定されており、この設定水
頭差が実現されるように放流ポンプ(12)の動作を制
御する。制御部(10)に設定される水頭差は、処理水
貯留槽(6)の水位が曝気槽(4)の水位以下となるこ
とを前提としている。
FIG. 1 is a block diagram showing one embodiment of a septic tank according to the present invention. For example, in the example shown in FIG. 1, some improvements are added while following the conventional septic tank shown in FIG. That is, a water level detecting means (19) is provided in the treated water storage tank (6). Control unit (1
0) controls the operation of the discharge pump (12) based on the water level detection detected by the water level detection means (19). A predetermined head difference is preset in the control unit (10) for the aeration tank (4) and the treated water storage tank (6), and the operation of the discharge pump (12) is performed so that the set head difference is realized. Control. The head difference set in the control unit (10) is based on the premise that the water level in the treated water storage tank (6) is lower than the water level in the aeration tank (4).

【0012】つまり、この図1に示した例では、処理水
貯留槽(6)の水位を制御することにより、曝気槽
(4)と処理水貯留槽(6)の間の水頭差を制御し、処
理水の処理流量を調整するようにしている。前記したオ
ーバーフロー管による制御の場合と相違して、水位制御
の対象は、処理水貯留槽(6)内の処理水であり、この
処理水は、膜分離装置(5)で処理された後のものであ
り、水質は良好で、目詰まりの問題は発生しない。処理
水の処理流量は支障なく確実に調整される。
That is, in the example shown in FIG. 1, by controlling the water level of the treated water storage tank (6), the head difference between the aeration tank (4) and the treated water storage tank (6) is controlled. The processing flow rate of the treated water is adjusted. Unlike the case of the control using the overflow pipe described above, the target of the water level control is the treated water in the treated water storage tank (6), and this treated water is treated after being treated by the membrane separation device (5). The water quality is good and no clogging problem occurs. The processing flow rate of the treated water is adjusted without any trouble.

【0013】なお、このような浄化槽には、処理水配管
(9)に弁(17)及び絞り(18)を並列に接続し、
膜分離装置(5)通過後の処理水を、弁(17)が開の
場合にここを通じて処理水配管(9)を介して処理水貯
留槽(6)に移送することができる。絞り(18)は、
処理水の流れを制御するために設けられているものであ
り、たとえば、固定の絞りが好ましく適用される。弁
(17)については、電動弁等のその開閉が自動的に制
御されるタイプを採用することができる。この場合の弁
(17)の開閉制御は制御部(10)で行うことができ
る。
In addition, in such a septic tank, a valve (17) and a throttle (18) are connected in parallel to a treated water pipe (9),
The treated water after passing through the membrane separation device (5) can be transferred to the treated water storage tank (6) via the treated water piping (9) through the treated water pipe (9) when the valve (17) is open. The aperture (18)
This is provided to control the flow of the treated water, and for example, a fixed throttle is preferably applied. As for the valve (17), a type in which the opening and closing of a motor-operated valve or the like is automatically controlled can be adopted. In this case, the opening and closing control of the valve (17) can be performed by the control unit (10).

【0014】また、処理水配管(9)には、その管路途
中に流量検知手段(20)を設けることもできる。流量
検知手段(20)は、処理水配管(9)を流れる処理水
の流量を検知するものであり、制御部(10)に予め設
定された設定流量を検知する。場合によっては、流量検
知手段(20)による流量検知は、処理流量の制御にフ
ィードバックすることもできる。すなわち、所定の処理
流量を制御部(10)に予め設定しておき、これが実現
されるように放流ポンプ(12)の動作を制御する。上
記水位検知手段(19)による流量制御と併用すること
によって、より正確な処理流量の調整が可能となる。
The treated water pipe (9) may be provided with a flow rate detecting means (20) in the middle of the pipe. The flow rate detecting means (20) detects a flow rate of the treated water flowing through the treated water pipe (9), and detects a set flow rate preset in the control unit (10). In some cases, the flow rate detection by the flow rate detection means (20) can be fed back to the control of the processing flow rate. That is, a predetermined processing flow rate is set in the control unit (10) in advance, and the operation of the discharge pump (12) is controlled so as to realize this. By using it together with the flow rate control by the water level detecting means (19), it is possible to more accurately adjust the processing flow rate.

【0015】さらに、処理水配管(9)には、弁(1
7)及び絞り(18)と同様に、補助ポンプ(21)を
並列接続することができる。この補助ポンプ(21)
は、制御部(10)に予め設定された設定流量を確保す
るために設けられるものであり、停止中に処理水が逆流
しないような構造が採用される。膜分離装置(5)の駆
動源を曝気槽(4)と処理水貯留槽(6)の水頭差とし
ている浄化槽にあっては、たとえば、施工時、膜分離装
置(5)の洗浄時等には、処理水配管(9)には空気が
入り込み、処理水が流れにくく、又は流れなくなるが、
このような時に、制御部(10)は、一時的に補助ポン
プ(21)を作動させて呼び水運転し、設定処理流量を
確保する。処理水配管(9)を流れる処理水の流量が設
定処理流量になったか否かは、前記した処理水配管
(9)の管路途中に設けられた流量検知手段(20)に
よって確認することができる。この流量検知手段(2
0)が設定処理流量を検知した後には、制御部(10)
は、補助ポンプ(21)を停止させる。
Furthermore, a valve (1) is connected to the treated water pipe (9).
Similar to 7) and the throttle (18), an auxiliary pump (21) can be connected in parallel. This auxiliary pump (21)
Is provided to secure a set flow rate set in advance in the control unit (10), and a structure is adopted in which the treated water does not flow backward during stoppage. In a septic tank in which the driving source of the membrane separation device (5) is the head difference between the aeration tank (4) and the treated water storage tank (6), for example, during construction, when cleaning the membrane separation device (5), etc. Means that air enters the treated water pipe (9) and the treated water hardly flows or stops flowing,
In such a case, the control unit (10) temporarily activates the auxiliary pump (21) to perform the priming operation and secure the set processing flow rate. Whether or not the flow rate of the treated water flowing through the treated water pipe (9) has reached the set treatment flow rate can be confirmed by the flow rate detecting means (20) provided in the middle of the treated water pipe (9). it can. This flow detecting means (2
After 0) detects the set processing flow rate, the control unit (10)
Stops the auxiliary pump (21).

【0016】たとえば以上の構成を有する図1に示した
浄化槽については、膜処理装置(5)に関する運転動作
は以下に示すことができる。 補助ポンプ(21)が作動し、曝気槽(4)内の被
処理水を吸引し、処理水流量検知手段(20)が設定処
理流量を検知するまで呼び水運転する。設定処理流量を
検知した後に補助ポンプ(21)は停止する。
For example, for the septic tank shown in FIG. 1 having the above configuration, the operation of the membrane processing apparatus (5) can be described as follows. The auxiliary pump (21) is operated, the water to be treated in the aeration tank (4) is sucked, and the priming operation is performed until the treated water flow rate detecting means (20) detects the set treatment flow rate. After detecting the set processing flow rate, the auxiliary pump (21) stops.

【0017】 放流ポンプ(12)が作動し、処理水
貯留槽(6)の水位を所定の水位とする。この水位は、
制御部(10)に予め設定しておくことができる。 弁(17)を開とし、水位検知手段(19)で処理
水貯留槽(6)内の水位を監視しながら、設定水頭差が
実現されるように、放流ポンプ(12)の運転が制御さ
れる。この時、流量検知手段(20)で処理水の流量を
監視し、設定処理流量が合わせて実現されるように、放
流ポンプ(12)の運転を制御することもできる。
The discharge pump (12) operates to set the water level in the treated water storage tank (6) to a predetermined water level. This water level
It can be set in the control unit (10) in advance. The operation of the discharge pump (12) is controlled so that the valve (17) is opened and the water level in the treated water storage tank (6) is monitored by the water level detection means (19) so that the set head difference is realized. You. At this time, the flow rate of the treated water can be monitored by the flow rate detecting means (20), and the operation of the discharge pump (12) can be controlled so that the set treated flow rate is realized.

【0018】なお、被処理水の吸引停止時には、弁(1
9)は閉じ、補助ポンプ(21)は停止している。図2
は、この発明の浄化槽の別の例を示した構成図である。
この図2に示した例では、曝気槽(4)と処理水貯留槽
(6)の間の水頭差を制御するのではなく、処理水配管
(9)を流れる処理水の流量を直接制御することにより
処理流量を調整するようにしている。そのために、処理
水配管(9)の管路途中に流量検知手段(20)が設け
られており、制御部(10)には所定の処理流量が設定
されている。
When the suction of the water to be treated is stopped, the valve (1
9) is closed and the auxiliary pump (21) is stopped. FIG.
FIG. 2 is a configuration diagram showing another example of the septic tank of the present invention.
In the example shown in FIG. 2, instead of controlling the head difference between the aeration tank (4) and the treated water storage tank (6), the flow rate of treated water flowing through the treated water pipe (9) is directly controlled. Thus, the processing flow rate is adjusted. For this purpose, a flow rate detection means (20) is provided in the middle of the treated water pipe (9), and a predetermined treatment flow rate is set in the control unit (10).

【0019】なお、図1の例に採用された水位検知手段
(19)は省略されている。そして、制御部(10)
は、流量検知手段(20)による流量検知に基づいて放
流ポンプ(12)の動作を制御する。放流ポンプ(1
2)が作動すると、処理水貯留槽(6)内の処理水は、
放流管(15)を経由して消毒槽(8)に移送される。
その結果、処理水貯留槽(6)の水位が低下し、曝気槽
(4)との水頭差が大きくなる。この時の水頭差にした
がって曝気槽(4)からは被処理水が処理水貯留槽
(6)に向かって移動し、膜分離装置(5)による被処
理水の固液分離と処理水の移送が行われるので、流量検
知手段(20)による流量検知によっても処理水の流量
が調整されることとなる。
The water level detecting means (19) employed in the example of FIG. 1 is omitted. And the control unit (10)
Controls the operation of the discharge pump (12) based on the flow rate detection by the flow rate detection means (20). Discharge pump (1
When 2) operates, the treated water in the treated water storage tank (6)
It is transferred to the disinfection tank (8) via the discharge pipe (15).
As a result, the water level in the treated water storage tank (6) decreases, and the head difference from the aeration tank (4) increases. According to the head difference at this time, the water to be treated moves from the aeration tank (4) toward the treated water storage tank (6), and the solid-liquid separation of the treated water and the transfer of the treated water by the membrane separation device (5). Is performed, the flow rate of the treated water is also adjusted by the flow rate detection by the flow rate detection means (20).

【0020】また、この図2の例の場合にも、図1に示
した例と同様に、弁(17)及び絞り(18)とともに
補助ポンプ(21)を処理水配管(9)に並列に接続す
ることができる。たとえば以上の構成を有する図2に示
した浄化槽については、膜処理装置(5)に関する運転
動作は以下に示すことができる。
Also in the case of the example shown in FIG. 2, similarly to the example shown in FIG. 1, the auxiliary pump (21) together with the valve (17) and the throttle (18) are connected in parallel to the treated water pipe (9). Can be connected. For example, with respect to the septic tank having the above-described configuration and shown in FIG. 2, the operation of the membrane processing apparatus (5) can be described below.

【0021】 補助ポンプ(21)が作動し、曝気槽
(4)内の被処理水を吸引し、流量検知手段(20)が
設定処理流量を検知するまで呼び水運転する。設定処理
流量を検知した後に補助ポンプ(21)は停止する。 弁(17)を開とし、流量検知手段(20)で処理
流量の監視を続行しながら、設定処理流量が実現される
ように放流ポンプ(12)の運転が制御される。
[0021] The auxiliary pump (21) operates to suck the water to be treated in the aeration tank (4), and performs a priming operation until the flow rate detecting means (20) detects the set processing flow rate. After detecting the set processing flow rate, the auxiliary pump (21) stops. The operation of the discharge pump (12) is controlled such that the set processing flow rate is realized while the valve (17) is opened and the monitoring of the processing flow rate is continued by the flow rate detection means (20).

【0022】もちろんこの発明は、以上の例によって限
定されるものではない。水位検知手段及び流量検知手段
の構成、構造等の細部については様々な態様が可能であ
ることは言うまでもない。
Of course, the present invention is not limited by the above examples. It goes without saying that various aspects are possible for details such as the configuration and structure of the water level detecting means and the flow rate detecting means.

【0023】[0023]

【発明の効果】以上詳しく説明した通り、この発明によ
って、膜分離装置が曝気槽と処理水貯留槽の水頭差を駆
動源として被処理水を固液分離し、処理水を処理水貯留
槽に送る浄化槽において、処理水の処理流量を支障なく
確実に調整することができる。
As described above in detail, according to the present invention, the membrane separation apparatus separates the water to be treated into solid and liquid by using the head difference between the aeration tank and the treated water storage tank as a driving source, and transfers the treated water to the treated water storage tank. In the septic tank to be sent, the treatment flow rate of the treated water can be surely adjusted without any trouble.

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

【図1】この発明の浄化槽の一実施例を示した構成図で
ある。
FIG. 1 is a configuration diagram showing one embodiment of a septic tank according to the present invention.

【図2】この発明の浄化槽の別の例を示した構成図であ
る。
FIG. 2 is a configuration diagram showing another example of the septic tank of the present invention.

【図3】従来の膜分離式の浄化槽を示した構成図であ
る。
FIG. 3 is a configuration diagram showing a conventional membrane separation type septic tank.

【符号の説明】[Explanation of symbols]

1 沈殿分離槽 2 嫌気濾床槽 3 移送ポンプ 4 曝気槽 5 膜分離装置 6 処理水貯留槽 7 散気管 8 消毒槽 9 処理水配管 10 制御部 11,13,19 水位検知手段 12 放流ポンプ 14 移送管 15 放流管 16 ブロア 17 弁 18 絞り 20 流量検知手段 21 補助ポンプ Reference Signs List 1 sedimentation separation tank 2 anaerobic filter bed tank 3 transfer pump 4 aeration tank 5 membrane separation device 6 treated water storage tank 7 diffuser tube 8 disinfection tank 9 treated water pipe 10 control unit 11, 13, 19 water level detecting means 12 discharge pump 14 transfer Pipe 15 Discharge pipe 16 Blower 17 Valve 18 Restrictor 20 Flow rate detecting means 21 Auxiliary pump

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中岡 敬善 大阪府門真市大字門真1048番地 松下電工 株式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takayoshi Nakaoka 1048 Odakadoma, Kadoma City, Osaka Matsushita Electric Works, Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 被処理水を活性汚泥により好気的に生物
学的処理する曝気槽に、膜分離装置が被処理水に浸漬可
能に内装され、この膜分離装置に接続された処理水配管
を介して処理水貯留槽が曝気槽と連通して設けられ、さ
らに処理水貯留槽は、放流ポンプを管路途中に設けた放
流管を介して消毒槽に連通し、前記膜分離装置は、曝気
槽と処理水貯留槽の間の水頭差を駆動源として被処理水
を固液分離し、処理水を処理水貯留槽に送る一方、活性
汚泥は曝気槽に保持する浄化槽において、処理水貯留槽
に水位検知手段が設けられ、この水位検知手段による水
位検知に基づいて、曝気槽と処理水貯留槽に関する予め
定められた設定水頭差が実現されるように前記放流ポン
プの動作を制御する制御部が設けられていることを特徴
とする浄化槽。
1. An aeration tank for aerobically biologically treating water to be treated with activated sludge, in which a membrane separation device is installed so as to be immersed in the water to be treated, and a treated water pipe connected to the membrane separation device. The treated water storage tank is provided in communication with the aeration tank via, and the treated water storage tank further communicates with the disinfection tank via a discharge pipe provided in the middle of a discharge pump, and the membrane separation device includes: Using the head difference between the aeration tank and the treated water storage tank as a drive source, the water to be treated is separated into solid and liquid, and the treated water is sent to the treated water storage tank, while the activated sludge is stored in the purification tank held in the aeration tank. A tank is provided with a water level detecting means, and based on the water level detection by the water level detecting means, control for controlling the operation of the discharge pump such that a predetermined set head difference between the aeration tank and the treated water storage tank is realized. A septic tank provided with a part.
【請求項2】 被処理水を活性汚泥により好気的に生物
学的処理する曝気槽に、膜分離装置が被処理水に浸漬可
能に内装され、この膜分離装置に接続された処理水配管
を介して処理水貯留槽が曝気槽と連通して設けられ、さ
らに処理水貯留槽は、放流ポンプを管路途中に設けた放
流管を介して消毒槽に連通し、前記膜分離装置は、曝気
槽と処理水貯留槽の間の水頭差を駆動源として被処理水
を固液分離し、処理水を処理水貯留槽に送る一方、活性
汚泥は曝気槽に保持する浄化槽において、処理水配管の
管路途中に流量検知手段が設けられ、この流量検知手段
による処理流量の検知に基づいて、予め定められた設定
流量が実現されるように前記放流ポンプの動作を制御す
る制御部が設けられていることを特徴とする浄化槽。
2. An aeration tank for aerobically biologically treating the water to be treated with activated sludge, in which a membrane separation device is provided so as to be immersed in the water to be treated, and a treated water pipe connected to the membrane separation device. The treated water storage tank is provided in communication with the aeration tank via, and the treated water storage tank further communicates with the disinfection tank via a discharge pipe provided in the middle of a discharge pump, and the membrane separation device includes: The water to be treated is separated into solid and liquid by using the head difference between the aeration tank and the treated water storage tank as a drive source, and the treated water is sent to the treated water storage tank. A flow rate detecting means is provided in the middle of the pipeline, and a control unit for controlling the operation of the discharge pump is provided based on the detection of the processing flow rate by the flow rate detecting means so that a predetermined set flow rate is realized. A septic tank characterized by being.
JP31338296A 1996-11-25 1996-11-25 Purifying tank Pending JPH10151483A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31338296A JPH10151483A (en) 1996-11-25 1996-11-25 Purifying tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31338296A JPH10151483A (en) 1996-11-25 1996-11-25 Purifying tank

Publications (1)

Publication Number Publication Date
JPH10151483A true JPH10151483A (en) 1998-06-09

Family

ID=18040598

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31338296A Pending JPH10151483A (en) 1996-11-25 1996-11-25 Purifying tank

Country Status (1)

Country Link
JP (1) JPH10151483A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001334282A (en) * 2000-05-29 2001-12-04 Shinko Pantec Co Ltd Apparatus and method for treating wastewater
WO2008095236A1 (en) * 2007-02-06 2008-08-14 Econova Ip Pty Ltd Domestic wastewater treatment system
JP2009039610A (en) * 2007-08-07 2009-02-26 Kasuga Techs Co Ltd Recycling device for sludge water
WO2017209353A1 (en) * 2016-05-31 2017-12-07 박병선 Water treatment apparatus using external housing-type membrane bioreactor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001334282A (en) * 2000-05-29 2001-12-04 Shinko Pantec Co Ltd Apparatus and method for treating wastewater
WO2008095236A1 (en) * 2007-02-06 2008-08-14 Econova Ip Pty Ltd Domestic wastewater treatment system
JP2009039610A (en) * 2007-08-07 2009-02-26 Kasuga Techs Co Ltd Recycling device for sludge water
JP4516981B2 (en) * 2007-08-07 2010-08-04 株式会社春日テックス Sludge water recycling equipment.
WO2017209353A1 (en) * 2016-05-31 2017-12-07 박병선 Water treatment apparatus using external housing-type membrane bioreactor

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