JPH04290590A - Membrane separator in septic tank - Google Patents
Membrane separator in septic tankInfo
- Publication number
- JPH04290590A JPH04290590A JP3081746A JP8174691A JPH04290590A JP H04290590 A JPH04290590 A JP H04290590A JP 3081746 A JP3081746 A JP 3081746A JP 8174691 A JP8174691 A JP 8174691A JP H04290590 A JPH04290590 A JP H04290590A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- septic tank
- water
- supply pipe
- 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
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 34
- 238000000926 separation method Methods 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 17
- 230000002093 peripheral effect Effects 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 14
- 239000010802 sludge Substances 0.000 description 8
- 239000010865 sewage Substances 0.000 description 4
- 239000000706 filtrate Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000005273 aeration Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Biological Wastes In General (AREA)
- Activated Sludge Processes (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は、浄化槽における膜分
離装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a membrane separation device for a septic tank.
【0002】0002
【従来の技術】従来、汚水浄化槽として、嫌気性微生物
、及び好気性微生物による生物学的処理により汚水を浄
化していく方式の汚水浄化槽が広く知られ、さらにこれ
ら汚水浄化槽として、好気性処理槽に好気性活性汚泥を
使用した処理槽を有するものが知られている。[Prior Art] Conventionally, as a sewage septic tank, a sewage septic tank that purifies sewage through biological treatment using anaerobic microorganisms and aerobic microorganisms has been widely known. It is known to have a treatment tank using aerobic activated sludge.
【0003】この好気性活性汚泥処理槽は、処理水と活
性汚泥との接触率が非常に高く効率の良い汚水浄化が行
える利点を有するが、処理水排出の際活性汚泥の流出を
防止する必要があり、このため活性汚泥処理槽には処理
水のみを濾過排出する分離膜モジュールを配置すること
がある。[0003] This aerobic activated sludge treatment tank has the advantage that the contact rate between the treated water and the activated sludge is very high and that it can purify the sewage efficiently, but it is necessary to prevent the activated sludge from flowing out when discharging the treated water. Therefore, activated sludge treatment tanks are sometimes equipped with a separation membrane module that filters and discharges only the treated water.
【0004】0004
【従来技術の問題点】しかし、活性汚泥の分散した処理
水中で濾過を行えば分離膜モジュールに目詰まりを起こ
し易く、保守管理が非常に面倒となる問題があった。も
っともこのような目詰まり防止手段として、横型配置と
された分離膜モジュールの下部にせん断力の大きい、気
泡混入の上昇流を散気装置で起こさせることなどが行わ
れているが、このような上昇流を生じさせるには非常に
大きな動力の給気装置を要し、装置のコストアップ、あ
るいは小型化の弊害となっていた。[Problems with the Prior Art] However, if filtration is performed in treated water in which activated sludge is dispersed, the separation membrane module is likely to become clogged, making maintenance management extremely troublesome. However, as a means to prevent such clogging, an air diffuser is used to generate an upward flow containing air bubbles with a large shear force at the bottom of a horizontally arranged separation membrane module. In order to generate an upward flow, an air supply device with extremely large power is required, which increases the cost of the device or hinders its miniaturization.
【0005】[0005]
【発明が解決しようとする課題】この発明は上記の問題
点に鑑み、小さい馬力で十分に目詰まりが防止でき、ま
た保守点検等も容易に行える浄化槽における膜分離装置
を提供することを目的としてなされたものである。[Problems to be Solved by the Invention] In view of the above-mentioned problems, the present invention aims to provide a membrane separation device for a septic tank that can sufficiently prevent clogging with a small horsepower and that can be easily maintained and inspected. It has been done.
【0006】即ち、この発明の浄化槽における膜分離装
置は、管状外圧式微細多孔質分離膜を縦方向に平行に多
数一定間隔で集めてなる分離膜モジュールが浄化槽内底
に立設され、該分離膜モジュールの中央縦方向空間内に
周壁に多数の通水口を有する槽内液供給管が配置され、
該槽内液供給管には空気混入用エジェクタを介して前記
浄化槽内の液を供給するポンプが接続されてなることを
特徴とするものである。That is, in the membrane separation device for a septic tank of the present invention, a separation membrane module consisting of a large number of tubular external pressure type microporous separation membranes collected at regular intervals in parallel in the vertical direction is installed upright at the bottom of the septic tank, and the separation A tank liquid supply pipe having a large number of water holes on the peripheral wall is arranged in the central vertical space of the membrane module,
The present invention is characterized in that a pump for supplying the liquid in the septic tank is connected to the tank liquid supply pipe via an ejector for mixing air.
【0007】[0007]
【実施例】次に、この発明の実施例を説明する。図1は
この発明の実施例の断面図である。 この発明の浄化
槽における膜分離装置1は、管状外圧式微細多孔質分離
膜2A…2Aを縦方向に平行に多数一定間隔で集めてな
る分離膜モジュール2が浄化槽、例えば好気性活性汚泥
処理槽の内底3に立設され、分離膜モジュール2の中央
縦方向空間2B内に、周壁に多数の通水口4A…4Aを
有する槽内液供給管4が配置され、この槽内液供給管4
には空気混入用のエジェクタ5を介して前記浄化槽内の
液Wを供給するポンプ6が接続されて構成されている。
また、本法は接触ばっ気槽内で使用することも可能であ
る。[Example] Next, an example of the present invention will be described. FIG. 1 is a sectional view of an embodiment of the invention. A membrane separation device 1 for a septic tank according to the present invention has a separation membrane module 2 formed by collecting a large number of tubular external pressure type microporous separation membranes 2A...2A in parallel in the vertical direction at regular intervals for use in a septic tank, for example, an aerobic activated sludge treatment tank. A tank liquid supply pipe 4 is installed vertically on the inner bottom 3 and has a large number of water passage ports 4A...4A on the peripheral wall in the central vertical space 2B of the separation membrane module 2.
A pump 6 for supplying the liquid W in the septic tank via an ejector 5 for mixing air is connected to the septic tank. The method can also be used in contact aeration tanks.
【0008】なお、図中7は管状外圧式微細多孔質分離
膜2Aよりなる分離膜モジュール2より濾過水を吸引す
る吸引ポンプを示し、濾過水を外部へ排出する管7Aと
連接されている。また図中8はエジェクタ3への空気取
り入れ管を示す。Reference numeral 7 in the figure indicates a suction pump that sucks filtrate from the separation membrane module 2 made of a tubular external pressure type microporous separation membrane 2A, and is connected to a pipe 7A that discharges the filtrate to the outside. Further, reference numeral 8 in the figure indicates an air intake pipe to the ejector 3.
【0009】[0009]
【作用】上記において、吸引ポンプ7を駆動して処理水
を濾過排出する際は、ポンプ6を駆動して浄化槽内の液
Wを分離膜モジュール2の中央縦方向空間2B内に供給
する。このとき水流につれエジェクタ5より空気が混入
し、空気混じりの液Wが槽内液供給管4の通水口4A…
4Aより勢い良く噴出する。一方、吸引ポンプ6の駆動
により分離膜モジュール2の膜内部が負圧となり膜外部
から内部への濾過が生じ、膜表面には活性汚泥等の浮遊
物が付着するが、中央縦方向空間2B内に吹き出る空気
混じりの液Wの流勢により膜外面には矢印で示す方向に
水流が生じ、付着異物の剥離が生じやすくなる。また、
同時に酸素供給も行われる。[Operation] In the above, when the suction pump 7 is driven to filter and discharge treated water, the pump 6 is driven to supply the liquid W in the septic tank into the central vertical space 2B of the separation membrane module 2. At this time, air is mixed in from the ejector 5 as the water flows, and the air-mixed liquid W is transferred to the water inlet 4A of the tank liquid supply pipe 4...
It ejects more forcefully than 4A. On the other hand, the drive of the suction pump 6 creates a negative pressure inside the membrane of the separation membrane module 2, causing filtration from the outside of the membrane to the inside, and suspended matter such as activated sludge adheres to the membrane surface, but inside the central vertical space 2B. Due to the force of the air-mixed liquid W that is blown out, a water flow is generated on the outer surface of the membrane in the direction shown by the arrow, and the attached foreign matter is likely to be peeled off. Also,
Oxygen is also supplied at the same time.
【0010】0010
【発明の効果】以上説明したように、この発明は膜分離
装置を縦型配置とし、その中心より径方向外側へ向け水
流を生じさせ、同時にエジェクタより空気を取り入れて
気泡を多く混入させるので膜外面に付着した異物は効率
良く剥離され、長期にわたり目詰まりが防止されるので
ある。また膜分離装置は縦型配置であるので取出、挿入
も容易であり後の保守点検作業も容易となるなどの効果
を有する。Effects of the Invention As explained above, the present invention has a membrane separator arranged vertically, generates water flow from the center to the outside in the radial direction, and at the same time takes in air from the ejector to mix in many air bubbles. Foreign matter adhering to the outer surface is efficiently removed and clogging is prevented for a long period of time. Furthermore, since the membrane separator is vertically arranged, it is easy to take out and insert, and subsequent maintenance and inspection work is also facilitated.
【図1】この発明の実施例の断面図である。FIG. 1 is a sectional view of an embodiment of the invention.
1 膜分離装置
2 分離膜モジュール
2A 管状外圧式微細多孔質分離膜2B
中央縦方向空間
3 浄化槽内底
4 槽内液供給管
4A 通水口
5 エジェクタ
6 ポンプ
W 槽内液1 Membrane separation device 2 Separation membrane module 2A Tubular external pressure type microporous separation membrane 2B
Central vertical space 3 Septic tank inner bottom 4 Tank liquid supply pipe 4A Water inlet 5 Ejector 6 Pump W Tank liquid
Claims (1)
に平行に多数一定間隔で集めてなる分離膜モジュールが
浄化槽内底に立設され、該分離膜モジュールの中央縦方
向空間内に周壁に多数の通水口を有する槽内液供給管が
配置され、該槽内液供給管には空気混入用エジェクタを
介して前記浄化槽内の液を供給するポンプが接続されて
なることを特徴とする浄化槽における膜分離装置。Claim 1: A separation membrane module comprising a large number of tubular external pressure type microporous separation membranes arranged vertically in parallel at regular intervals is installed at the bottom of the septic tank, and a peripheral wall is provided in the central vertical space of the separation membrane module. A tank liquid supply pipe having a large number of water holes is disposed in the tank, and a pump for supplying the liquid in the septic tank is connected to the tank liquid supply pipe via an air mixing ejector. Membrane separation equipment in septic tanks.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3081746A JPH04290590A (en) | 1991-03-19 | 1991-03-19 | Membrane separator in septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3081746A JPH04290590A (en) | 1991-03-19 | 1991-03-19 | Membrane separator in septic tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04290590A true JPH04290590A (en) | 1992-10-15 |
Family
ID=13755004
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3081746A Pending JPH04290590A (en) | 1991-03-19 | 1991-03-19 | Membrane separator in septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04290590A (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001062481A (en) * | 1999-08-26 | 2001-03-13 | Kubota Corp | Treatment of concentrated sewage |
JP2001062480A (en) * | 1999-08-26 | 2001-03-13 | Kubota Corp | Treatment of sewage |
FR2825934A1 (en) * | 2001-06-15 | 2002-12-20 | Saint Aigulinoise Des Eaux Et | Immersed filtration module in wastewater tank containing particle suspension, includes pump and porous ceramic membrane filter for clarified water extraction |
JP2010207799A (en) * | 2009-03-09 | 2010-09-24 | Shenzhen Jdl Environmental Protection Ltd | Jet aeration apparatus and method of using the same |
JP2010264436A (en) * | 2009-05-15 | 2010-11-25 | Shenzhen Jdl Environmental Protection Ltd | Method for sludge treatment |
JP2012061432A (en) * | 2010-09-16 | 2012-03-29 | Mitsubishi Rayon Co Ltd | Air diffuser and method of operating membrane separation device |
JP2012106161A (en) * | 2010-11-16 | 2012-06-07 | Toshiba Corp | Membrane separation biological treatment apparatus |
WO2015008346A1 (en) * | 2013-07-17 | 2015-01-22 | 三菱重工業株式会社 | Water treatment device |
RU180554U1 (en) * | 2018-04-03 | 2018-06-18 | Владимир Сергеевич Спасский | Sewer treatment device |
RU180556U1 (en) * | 2018-04-03 | 2018-06-18 | Владимир Сергеевич Спасский | Sewer treatment device |
RU180890U1 (en) * | 2018-04-03 | 2018-06-29 | Владимир Сергеевич Спасский | Sewer treatment device |
-
1991
- 1991-03-19 JP JP3081746A patent/JPH04290590A/en active Pending
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001062481A (en) * | 1999-08-26 | 2001-03-13 | Kubota Corp | Treatment of concentrated sewage |
JP2001062480A (en) * | 1999-08-26 | 2001-03-13 | Kubota Corp | Treatment of sewage |
FR2825934A1 (en) * | 2001-06-15 | 2002-12-20 | Saint Aigulinoise Des Eaux Et | Immersed filtration module in wastewater tank containing particle suspension, includes pump and porous ceramic membrane filter for clarified water extraction |
JP2010207799A (en) * | 2009-03-09 | 2010-09-24 | Shenzhen Jdl Environmental Protection Ltd | Jet aeration apparatus and method of using the same |
JP2010264436A (en) * | 2009-05-15 | 2010-11-25 | Shenzhen Jdl Environmental Protection Ltd | Method for sludge treatment |
JP2012061432A (en) * | 2010-09-16 | 2012-03-29 | Mitsubishi Rayon Co Ltd | Air diffuser and method of operating membrane separation device |
JP2012106161A (en) * | 2010-11-16 | 2012-06-07 | Toshiba Corp | Membrane separation biological treatment apparatus |
CN102557233A (en) * | 2010-11-16 | 2012-07-11 | 株式会社东芝 | Film Separation Bio-treatment Device |
WO2015008346A1 (en) * | 2013-07-17 | 2015-01-22 | 三菱重工業株式会社 | Water treatment device |
JP6072254B2 (en) * | 2013-07-17 | 2017-02-01 | 三菱重工業株式会社 | Water treatment equipment |
US10138147B2 (en) | 2013-07-17 | 2018-11-27 | Mitsubishi Heavy Industries Engineering, Ltd. | Water treatment device |
RU180554U1 (en) * | 2018-04-03 | 2018-06-18 | Владимир Сергеевич Спасский | Sewer treatment device |
RU180556U1 (en) * | 2018-04-03 | 2018-06-18 | Владимир Сергеевич Спасский | Sewer treatment device |
RU180890U1 (en) * | 2018-04-03 | 2018-06-29 | Владимир Сергеевич Спасский | Sewer treatment device |
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