JPH09225484A - Membrane separation device and water purifying tank - Google Patents

Membrane separation device and water purifying tank

Info

Publication number
JPH09225484A
JPH09225484A JP3647396A JP3647396A JPH09225484A JP H09225484 A JPH09225484 A JP H09225484A JP 3647396 A JP3647396 A JP 3647396A JP 3647396 A JP3647396 A JP 3647396A JP H09225484 A JPH09225484 A JP H09225484A
Authority
JP
Japan
Prior art keywords
tank
water
inner tank
nitrification
membrane module
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
JP3647396A
Other languages
Japanese (ja)
Inventor
Yasuyoshi Sugiyama
靖芳 杉山
Tatsuro Yamamoto
達郎 山本
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.)
Inax Corp
Original Assignee
Inax Corp
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 Inax Corp filed Critical Inax Corp
Priority to JP3647396A priority Critical patent/JPH09225484A/en
Publication of JPH09225484A publication Critical patent/JPH09225484A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a membrane separation device capable of widening the membrane surface area. SOLUTION: Water in a raw water storage tank 7 flows in a denitrificating tank 9 through an advection cylinder 8, flows in a nitrification tank 11 through an advection cylinder 10 and is aerated by a diffusing pipe 12, to which air is supplied by a blower 13. A separation membrane module 16 is provided in an inner tank 15 and the water permeates the membrane to take out a permeated water by sucking the inside of the separation membrane module 16 with a pump 17. The nitrificated water in the inner tank 15 is aerated by diffusing pipe 19, to which air is supplied from a blower 18. A part of the water in the inner tank 15 is returned to the denitrificating tank 9 by an airlift pump 20.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は汚水等を処理するた
めの膜分離装置及び浄化槽に関する。
TECHNICAL FIELD The present invention relates to a membrane separation device and a septic tank for treating wastewater and the like.

【0002】[0002]

【従来の技術】汚水を処理する浄化槽に分離膜を組み込
むことがある(特開平4−354592号公報、特開平
6−218247号公報など)。前者の特開平4−35
4592号公報には、沈殿分離槽又は嫌気性濾床槽と、
接触曝気槽と、該接触曝気槽から硝化液を該沈殿分離槽
又は嫌気性濾床槽へ戻す汚水返送管と、該接触曝気槽内
に設けられた分離膜モジュールとを備えた汚水処理装置
が記載されている。
2. Description of the Related Art Separation membranes are sometimes incorporated in septic tanks for treating sewage (JP-A-4-354592, JP-A-6-218247, etc.). The former JP-A-4-35
4592 discloses a precipitation separation tank or an anaerobic filter bed tank;
A sewage treatment apparatus comprising a contact aeration tank, a sewage return pipe for returning the nitrification liquid from the contact aeration tank to the precipitation separation tank or the anaerobic filter bed tank, and a separation membrane module provided in the contact aeration tank. Have been described.

【0003】ところで、汚水処理装置内の槽同士の間で
揚水させる場合にエアリフトを用いることがある。例え
ば、実開平2−61495号公報には、沈殿槽のような
一次処理槽と、接触曝気槽のような二次処理槽とを備え
た汚水処理装置において、該一次処理槽内の水を水位調
整槽へエアリフトによって揚水し、この水位調整槽内の
水をエアリフトによって二次処理槽へ揚水することが記
載されている。
By the way, an air lift is sometimes used to pump water between tanks in a sewage treatment apparatus. For example, Japanese Utility Model Publication No. 2-61495 discloses a sewage treatment apparatus including a primary treatment tank such as a settling tank and a secondary treatment tank such as a contact aeration tank. It is described that water is pumped to the adjusting tank by an air lift, and water in the water level adjusting tank is pumped to a secondary treatment tank by an air lift.

【0004】[0004]

【発明が解決しようとする課題】従来の浄化槽において
は、分離膜モジュールを設置した槽内の水位が変動する
ため、分離膜モジュールは該槽内の下限水位よりも下位
に配置される。このため、分離膜モジュールの膜面積を
大きくとることが難しい。
In the conventional septic tank, since the water level in the tank in which the separation membrane module is installed varies, the separation membrane module is placed below the lower limit water level in the tank. Therefore, it is difficult to increase the membrane area of the separation membrane module.

【0005】本発明は、膜面積を大きくとることができ
る膜分離装置及び浄化槽を提供することを目的とする。
An object of the present invention is to provide a membrane separation device and a septic tank which can have a large membrane area.

【0006】[0006]

【課題を解決するための手段】本発明の膜分離装置は、
水を透過処理する分離膜モジュールを有した膜分離装置
において、外槽と、該外槽の内部に設置された内槽と、
該外槽の水を該内槽に供給し、該内槽から水を該外槽に
オーバーフローさせて該内槽の水位を一定にするポンプ
とを備え、前記分離膜モジュールが該内槽の内部に設置
されていることを特徴とするものである。
The membrane separation device of the present invention comprises:
In a membrane separation device having a separation membrane module that permeates water, an outer tank, an inner tank installed inside the outer tank,
A pump that supplies water from the outer tank to the inner tank and overflows water from the inner tank to the outer tank to keep the water level in the inner tank constant; It is characterized by being installed in.

【0007】本発明の浄化槽は、脱窒槽と、硝化槽と、
該硝化槽で硝化処理された水を透過処理する分離膜モジ
ュールとを備えた浄化槽において、該硝化槽内に内槽を
設けると共に、硝化槽内の硝化処理水を該内槽に供給
し、該内槽からオーバーフローさせて該内槽の水位を一
定にするポンプを設け、前記分離膜モジュールを該内槽
に設置したことを特徴とするものである。
The septic tank of the present invention comprises a denitrification tank, a nitrification tank, and
In a septic tank equipped with a separation membrane module for permeating nitrification-treated water in the nitrification tank, an inner tank is provided in the nitrification tank, and the nitrification-treated water in the nitrification tank is supplied to the inner tank. A pump for overflowing from the inner tank to keep the water level in the inner tank constant is provided, and the separation membrane module is installed in the inner tank.

【0008】かかる膜分離装置及び浄化槽においては、
内槽の水位が常に一定(オーバーフロー水位)になるた
め、内槽内の上部まで分離膜を広げることができ、分離
膜モジュールの膜面積を大きくとることができる。
In the membrane separation device and the septic tank,
Since the water level in the inner tank is always constant (overflow water level), the separation membrane can be spread to the upper part in the inner tank, and the membrane area of the separation membrane module can be increased.

【0009】本発明の浄化槽において、内槽内の水位が
一定であるため、該内槽内の硝化水を脱窒槽にエアリフ
トポンプによって揚水して返送する場合、このエアリフ
トポンプの送水量が一定量となる。
In the septic tank of the present invention, since the water level in the inner tank is constant, when the nitrifying water in the inner tank is pumped back to the denitrification tank by the air lift pump and returned, the amount of water fed by the air lift pump is constant. Becomes

【0010】[0010]

【発明の実施の形態】図1は、実施の形態に係る浄化槽
の断面図である。原水は流入口1から夾雑物除去槽2に
導入され、スクリーン3を通り、原水貯留槽7へ流入す
る。なお、夾雑物の一部は汚泥貯留槽4へ落下する。ス
クリーン3の近傍にブロワ5によって気泡が散気管6か
ら散気される。
1 is a cross-sectional view of a septic tank according to an embodiment. Raw water is introduced from the inflow port 1 into the contaminant removal tank 2, passes through the screen 3, and flows into the raw water storage tank 7. It should be noted that some of the impurities fall into the sludge storage tank 4. Air bubbles are diffused from the diffuser pipe 6 in the vicinity of the screen 3 by the blower 5.

【0011】原水貯留槽7内の水は、移流筒8を経て脱
窒槽9へ流入し、脱窒処理される。この水は、次いで、
移流筒10を経て、硝化槽11に流入し、ブロワ13か
ら空気が供給される散気管12によって曝気される。硝
化処理された水は、エアリフトポンプ14によって硝化
槽11内の内槽15へ揚水される。なお、エアリフトポ
ンプ14へはブロワ13から空気が供給される。
The water in the raw water storage tank 7 flows into the denitrification tank 9 through the advection tube 8 and is denitrified. This water is then
It flows into the nitrification tank 11 through the advection cylinder 10 and is aerated by the air diffuser 12 to which air is supplied from the blower 13. The nitrification-treated water is pumped to the inner tank 15 in the nitrification tank 11 by the air lift pump 14. Air is supplied from the blower 13 to the air lift pump 14.

【0012】内槽15内には分離膜モジュール16が設
けられており、該分離膜モジュール16内がポンプ17
で吸引されることにより、水が膜を透過し、透過水が取
り出される。内槽15内の硝化処理水は、ブロワ18か
ら空気が供給された散気管19によって曝気されてい
る。内槽15内の水の一部は、エアリフトポンプ20に
よって脱窒槽9へ返送されている。このエアリフトポン
プ20へはブロワ18から空気が供給されている。
A separation membrane module 16 is provided in the inner tank 15, and the inside of the separation membrane module 16 is a pump 17.
The water permeates the membrane by being sucked in and the permeated water is taken out. The nitrification-treated water in the inner tank 15 is aerated by an air diffuser 19 to which air is supplied from a blower 18. Part of the water in the inner tank 15 is returned to the denitrification tank 9 by the air lift pump 20. Air is supplied to the air lift pump 20 from the blower 18.

【0013】なお、このエアリフトポンプ20の返送水
量とポンプ17を経て取り出される透過水量との合量よ
りも十分に多い硝化処理水がエアリフトポンプ14によ
って内槽15内へ供給されており、内槽15からは常に
水が硝化槽11へオーバーフローし、内槽15内の水位
は常に一定となっている。
The nitrification-treated water, which is sufficiently larger than the total amount of the returned water of the air lift pump 20 and the amount of permeated water taken out through the pump 17, is supplied into the inner tank 15 by the air lift pump 14. Water always overflows from 15 to the nitrification tank 11, and the water level in the inner tank 15 is always constant.

【0014】なお、硝化槽11内の汚泥はポンプ21を
有する配管22によって汚泥貯留槽4へ定期的に引き抜
かれる。
The sludge in the nitrification tank 11 is regularly withdrawn to the sludge storage tank 4 by a pipe 22 having a pump 21.

【0015】このように構成された浄化槽においては、
内槽15内の水位がオーバーフローにより一定となって
おり、分離膜モジュール16を該内槽15内の上部にま
で広げることができ、膜面積を大きくとることができ
る。
In the septic tank constructed as described above,
Since the water level in the inner tank 15 is constant due to the overflow, the separation membrane module 16 can be spread to the upper part in the inner tank 15, and the membrane area can be increased.

【0016】なお、内槽15内の硝化水はエアリフトポ
ンプ20によって脱窒槽9へ送られて脱窒処理されるの
であるが、内槽15内の水位が常に一定となっているた
め、このエアリフトポンプ20による送水量も一定のも
のとなる。
The nitrifying water in the inner tank 15 is sent to the denitrification tank 9 by the air lift pump 20 for denitrification treatment. However, since the water level in the inner tank 15 is always constant, this air lift is required. The amount of water sent by the pump 20 is also constant.

【0017】前記ポンプ17は、浄化槽内の水位が下限
水位LWL以下になった場合に停止される。また、浄化
槽内の水位が下限水位LWLと上限水位HWLとの間に
あるときに定常運転され、上限水位HWL以上になった
場合には定常運転時の2倍速で運転される。このように
ポンプ17を制御することにより、一時的に多量の原水
が浄化槽に流入してきても十分に対処できる。
The pump 17 is stopped when the water level in the septic tank falls below the lower limit water level LWL. Further, the steady operation is performed when the water level in the septic tank is between the lower limit water level LWL and the upper limit water level HWL, and when the water level is equal to or higher than the upper limit water level HWL, the operation is performed at double speed as in the steady operation. By controlling the pump 17 in this way, even if a large amount of raw water temporarily flows into the septic tank, it can be sufficiently dealt with.

【0018】ポンプ17の運転時には原水貯留槽7から
脱窒槽9へ常に原水が流入するようになり、脱窒性能が
安定する。
During the operation of the pump 17, the raw water always flows from the raw water storage tank 7 into the denitrification tank 9, and the denitrification performance is stabilized.

【0019】この浄化槽においては、分離膜モジュール
16を予め内槽15に組み付けておき、この内槽15を
硝化槽11に挿入することにより併せて分離膜モジュー
ル16の設置を行える。
In this septic tank, the separation membrane module 16 is assembled in advance to the inner tank 15, and the inner tank 15 is inserted into the nitrification tank 11, so that the separation membrane module 16 can be installed together.

【0020】[0020]

【発明の効果】以上の通り、本発明の膜分離装置及び浄
化槽は、水位が一定の内槽に分離膜モジュールを設置し
たものであり、内槽内の上部にまで分離膜モジュールを
広げることにより膜面積を大きくとることができる。
As described above, the membrane separation device and the septic tank of the present invention have the separation membrane module installed in the inner tank having a constant water level. The film area can be increased.

【0021】本発明の浄化槽においては、内槽から脱窒
槽への返送水量をエアリフトポンプを使用しても一定の
ものとすることも可能である。
In the septic tank of the present invention, the amount of water returned from the inner tank to the denitrification tank can be made constant even if an air lift pump is used.

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

【図1】実施の形態に係る浄化槽の断面図である。FIG. 1 is a cross-sectional view of a septic tank according to an embodiment.

【符号の説明】[Explanation of symbols]

2 夾雑物除去槽 6 汚泥貯留槽 7 原水貯留槽 8,10 移流筒 9 脱窒槽 11 硝化槽 14,20 エアリフトポンプ 15 内槽 16 分離膜モジュール 2 Contaminant removal tank 6 Sludge storage tank 7 Raw water storage tank 8, 10 Advection cylinder 9 Denitrification tank 11 Nitrification tank 14, 20 Air lift pump 15 Inner tank 16 Separation membrane module

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 水を透過処理する分離膜モジュールを有
した膜分離装置において、 外槽と、該外槽の内部に設置された内槽と、該外槽の水
を該内槽に供給し、該内槽から水を該外槽にオーバーフ
ローさせて該内槽の水位を一定にするポンプとを備え、 前記分離膜モジュールが該内槽の内部に設置されている
ことを特徴とする膜分離装置。
1. A membrane separation apparatus having a separation membrane module for permeating water, wherein an outer tank, an inner tank installed inside the outer tank, and water in the outer tank are supplied to the inner tank. And a pump for overflowing water from the inner tank to the outer tank to keep the water level in the inner tank constant, wherein the separation membrane module is installed inside the inner tank. apparatus.
【請求項2】 脱窒槽と、硝化槽と、該硝化槽で硝化処
理された水を透過処理する分離膜モジュールとを備えた
浄化槽において、 該硝化槽内に内槽を設けると共に、硝化槽内の硝化処理
水を該内槽に供給し、該内槽からオーバーフローさせて
該内槽の水位を一定にするポンプを設け、 前記分離膜モジュールを該内槽に設置したことを特徴と
する浄化槽。
2. A decontamination tank comprising a denitrification tank, a nitrification tank, and a separation membrane module for permeation treatment of water nitrified in the nitrification tank, wherein an inner tank is provided in the nitrification tank and A nitrification-treated water of (1) is supplied to the inner tank, a pump for overflowing from the inner tank to keep the water level of the inner tank constant is provided, and the separation membrane module is installed in the inner tank.
【請求項3】 請求項2において、前記内槽の内部の硝
化処理水を前記脱窒槽に送る送水手段を備えたことを特
徴とする浄化槽。
3. The septic tank according to claim 2, further comprising a water feed means for sending the nitrification-treated water inside the inner tank to the denitrification tank.
【請求項4】 請求項3において、前記送水手段はエア
リフトポンプであることを特徴とする浄化槽。
4. The septic tank according to claim 3, wherein the water supply means is an air lift pump.
JP3647396A 1996-02-23 1996-02-23 Membrane separation device and water purifying tank Pending JPH09225484A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3647396A JPH09225484A (en) 1996-02-23 1996-02-23 Membrane separation device and water purifying tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3647396A JPH09225484A (en) 1996-02-23 1996-02-23 Membrane separation device and water purifying tank

Publications (1)

Publication Number Publication Date
JPH09225484A true JPH09225484A (en) 1997-09-02

Family

ID=12470792

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3647396A Pending JPH09225484A (en) 1996-02-23 1996-02-23 Membrane separation device and water purifying tank

Country Status (1)

Country Link
JP (1) JPH09225484A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001038178A (en) * 1999-07-30 2001-02-13 Daicel Chem Ind Ltd Separation membrane module
DE202008015792U1 (en) * 2008-11-28 2010-04-15 Rockbourne Environmental Ltd., Christchurch Filter system for dirty water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001038178A (en) * 1999-07-30 2001-02-13 Daicel Chem Ind Ltd Separation membrane module
DE202008015792U1 (en) * 2008-11-28 2010-04-15 Rockbourne Environmental Ltd., Christchurch Filter system for dirty water

Similar Documents

Publication Publication Date Title
WO2007019617A1 (en) Biological phosphorous removal
JP2008264772A (en) Membrane separation activated sludge apparatus and treatment method of organic substance-containing water
JPH09314177A (en) Method and apparatus for treating organic waste water
JP4059790B2 (en) Membrane separation activated sludge treatment apparatus and membrane separation activated sludge treatment method
JPH07155758A (en) Waste water treating device
US20070017867A1 (en) Submerged attached growth bioreactor
KR19980083279A (en) Treatment method of high concentration organic wastewater and nutrients using immersion type microfiltration membrane-activated sludge process
KR100948807B1 (en) High class treatment used flotation system having ultrasonic waves
CN106865889A (en) A kind of effluent purification method
JPH0813359B2 (en) Wastewater treatment equipment containing nitrogen
JP2584392B2 (en) Undiluted advanced treatment method for night soil and septic tank sludge
JP7015117B2 (en) Organic wastewater treatment method and organic wastewater treatment system
KR20130079834A (en) Operating method of advanced treatment process use of submerged membrane and advanced treatment apparatus thereof
JPH09225484A (en) Membrane separation device and water purifying tank
JP3263267B2 (en) Septic tank
CN212387932U (en) Domestic sewage treatment integrated device
JP2005246308A (en) Method for bio-treating wastewater
JP4709792B2 (en) Wastewater treatment system
JPH11104698A (en) Drainage treatment method
JP4307275B2 (en) Wastewater treatment method
CN111547955A (en) Domestic sewage treatment integrated device
JP2002192182A (en) Ultrahigh concentration membrane separation activated sludge method
JP3807945B2 (en) Method and apparatus for treating organic wastewater
JPH07256294A (en) Living waste water treatment apparatus
JP4104806B2 (en) Solid-liquid separation method and apparatus for organic wastewater treatment