JPH1085565A - Membrane separator - Google Patents
Membrane separatorInfo
- Publication number
- JPH1085565A JPH1085565A JP24796196A JP24796196A JPH1085565A JP H1085565 A JPH1085565 A JP H1085565A JP 24796196 A JP24796196 A JP 24796196A JP 24796196 A JP24796196 A JP 24796196A JP H1085565 A JPH1085565 A JP H1085565A
- Authority
- JP
- Japan
- Prior art keywords
- diffuser
- water
- treated
- upward
- air
- 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 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000000926 separation method Methods 0.000 claims description 9
- 238000009792 diffusion process Methods 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 4
- 239000006260 foam Substances 0.000 abstract 2
- 239000002893 slag Substances 0.000 abstract 2
- 230000005494 condensation Effects 0.000 abstract 1
- 238000009833 condensation Methods 0.000 abstract 1
- 238000007664 blowing Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 125000006850 spacer group Chemical group 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 1
- 238000009295 crossflow filtration Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、汚水の浄化処理
などに使用せられるクロスフロー濾過式膜分離装置に関
する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cross-flow filtration type membrane separation apparatus used for purification of waste water.
【0002】[0002]
【従来の技術】従来より処理槽の被処理水中に並列状に
浸漬せられた垂直平膜モジュールの下方に、上向き噴気
孔を有する散気管が配置せられた膜分離装置は知られて
いる。2. Description of the Related Art Conventionally, there is known a membrane separation apparatus in which an air diffuser having an upward blowing port is disposed below a vertical flat membrane module immersed in parallel in water to be treated in a treatment tank.
【0003】[0003]
【発明が解決しようとする課題】上記従来装置は、散気
管により気泡を各垂直平膜モジュールの両面にそって上
昇させ、膜表面に濾滓が付着堆積するのを防止しようと
するものであるが、汚水を高濃度に濃縮しようとする場
合、上記気泡は比較的大きくしかも上昇速度が遅いた
め、濾滓が膜表面に成長するのを防ぐことができなかっ
た。その結果、処理槽の運転を停止し、膜洗浄作業を行
なわざるを得なかった。この発明の目的は、膜洗浄作業
なしに処理槽の長時間安定運転を継続して行ないうるよ
うにし、汚水の高濃度濃縮を可能とする膜分離装置を提
供することにある。The above-mentioned conventional apparatus aims to prevent bubbles from adhering and depositing on the membrane surface by raising bubbles along both sides of each vertical flat membrane module by means of an air diffuser. However, when trying to concentrate sewage to a high concentration, the above-mentioned bubbles were relatively large and the rising speed was slow, so that it was not possible to prevent the cake from growing on the membrane surface. As a result, the operation of the processing tank was stopped, and the membrane cleaning operation had to be performed. SUMMARY OF THE INVENTION An object of the present invention is to provide a membrane separation apparatus that enables a long-term stable operation of a treatment tank to be continuously performed without performing a membrane cleaning operation, and enables high-concentration concentration of wastewater.
【0004】[0004]
【課題を解決するための手段】この発明による膜分離装
置は、処理槽の被処理水中に並列状に浸漬せられた垂直
平膜モジュールの下方に、上向き噴気孔を有する散気管
と、空気吸込管を備えかつ被処理水を作動水とするエジ
ェクターの上向き吐出口を有するディフューザとが、前
者を上に、後者を下にして配置せられるとともに、散気
管よりの比較的大きな気泡と、ディフューザよりの超微
細気泡とが、ともに各垂直平膜モジュールの両面にそっ
て上昇するようになされているものである。SUMMARY OF THE INVENTION A membrane separation apparatus according to the present invention comprises a diffuser tube having an upward blowing port below a vertical flat membrane module immersed in parallel in the water to be treated in a treatment tank; A diffuser having a pipe and having an upward discharge port of an ejector using the water to be treated as working water is arranged with the former up and the latter down, and a relatively large bubble from the diffuser and a diffuser. Are raised along both sides of each vertical flat membrane module.
【0005】この発明の膜分離装置によれば、各垂直平
膜モジュールの両面にそって上昇する散気管よりの比較
的大きな気泡に加えて、ディフューザより超微細気泡が
作動水である被処理水とともに勢よく上向きに吐出せら
れるので、膜表面付近の被処理水に強い乱流が生じ、膜
表面に付着しようとする濾滓を除去してその成長を防
ぐ。また、ディフューザよりの上記上向きの吐出によ
り、垂直平膜モジュール群の外側では下向きの流れが生
じ、被処理水が循環するので、全体の濃度が均一化され
る。[0005] According to the membrane separation apparatus of the present invention, in addition to the relatively large bubbles rising from the air diffuser rising along both sides of each vertical flat membrane module, the diffused water is treated with ultra-fine bubbles from the diffuser. As a result, strong turbulence is generated in the water to be treated near the surface of the membrane, and the filter cake that tends to adhere to the membrane surface is removed to prevent its growth. In addition, the upward discharge from the diffuser causes a downward flow outside the vertical flat membrane module group, and the water to be treated circulates, so that the overall concentration is made uniform.
【0006】[0006]
【発明の実施の形態】この発明の実施の形態を、以下図
面を参照して説明する。図示の膜分離装置は、処理槽
(1) の被処理水(W) 中に並列状に浸漬せられた垂直平膜
モジュール(2) の下方に、上向き噴気孔(3) を有する散
気管(4) と、空気吸込管(5) を備えかつ被処理水(W) を
作動水とするエジェクター(6) の上向き吐出口(7) を有
するディフューザ(8) とが、前者を上に、後者を下にし
て配置せられている。Embodiments of the present invention will be described below with reference to the drawings. The membrane separator shown is a processing tank
Below the vertical flat membrane module (2) immersed in parallel in the water (W) to be treated (1), a diffuser (4) having an upward blowing port (3) and an air suction pipe (5) ) And a diffuser (8) having an upward discharge port (7) of an ejector (6) that uses the water to be treated (W) as working water, and the diffuser (8) is disposed with the former facing upward and the latter facing downward. .
【0007】平膜モジュール(2) は、上端排出口部(9)
およびスリット状の内向き開口部を有しかつ所定間隔を
おいて平行に配置せられた一対の垂直集水管(10)と、両
集水管(10)の上下にわたし止められた補強バー(11)と、
両集水管(10)の開口部に両縁が固定せられた濾過水通過
空間形成用網状スペーサ(12)と、網状スペーサ(12)の両
面に張られた平膜(13)とよりなるもので、図面では、分
かり易くするため枚数を少なくして示したが、通常13
〜30mm間隔おきに数10枚が固定脚(14)を有する横
断面方形の囲い(15)内に垂直に配列保持されている。各
平膜モジュール(2) の集水管(10)の排出口部(9) は、処
理槽(1) の上方に配されかつ吸引ポンプ(16)が関与せら
れた濾過水吸引管(17)の、平面からみてU形の分岐管(1
8)の連通口部(27)にホース(19)で接続せられている。[0007] The flat membrane module (2) has an upper end outlet (9).
And a pair of vertical water collecting pipes (10) having slit-shaped inward openings and arranged in parallel at a predetermined interval, and reinforcing bars (11) fixed to the upper and lower sides of both water collecting pipes (10). )When,
It consists of a mesh spacer (12) for forming filtered water passage space with both edges fixed to the openings of both water collection pipes (10), and a flat membrane (13) stretched on both sides of the mesh spacer (12) In the drawings, the number is reduced for the sake of clarity.
Several tens of sheets are vertically arranged in a rectangular enclosure (15) having fixed legs (14) at intervals of 〜30 mm. The outlet (9) of the water collecting pipe (10) of each flat membrane module (2) is located above the treatment tank (1) and has a filtered water suction pipe (17) that is associated with a suction pump (16). U-shaped branch pipe (1
The hose (19) is connected to the communication port (27) of (8).
【0008】散気管(4) は平膜モジュール(2) と直交さ
せられるとともに、平膜(13)の幅全体にわたるように所
要本数、ブロア(20)が関与せられた空気供給管(21)の下
部水平部(22)にこれと連通するように並列状に設けられ
ており、各散気管(4) の噴気孔(3) は、隣り合う平膜モ
ジュール(2) のすべての間および両端に存在する平膜モ
ジュール(2) の各外方に存在しうる数だけ設けられてお
り、散気管(4) よりの比較的大きな気泡が各垂直平膜モ
ジュール(2) の両面にそって上昇するようになされてい
る。[0008] The air supply pipe (21) which is perpendicular to the flat membrane module (2) and which has a required number of blowers (20) so as to cover the entire width of the flat membrane (13). The air outlets (3) of each diffuser (4) are located between and at both ends of the adjacent flat membrane module (2). As many as possible outside each of the flat membrane modules (2) that exist in the vertical air membrane module (2), and relatively large bubbles from the air diffuser (4) rise along both sides of each vertical flat membrane module (2). It has been made to be.
【0009】図4に詳しく示されているように、エジェ
クター(6) の羽根車(23)の真下に下向きの被処理水吸引
口(24)があけられており、同ノズル(25)の先に空気吸込
管(5) が接続せられ、さらにその先にそれぞれディフュ
ーザ(8) を有する両側に2つずつ直角にのびた分岐部(2
6)が設けられている。合わせて4つのディフューザ(8)
の形状と配置は、これらより作動水である被処理水とと
もに噴出せられる超微細気泡全体が、各垂直平膜モジュ
ール(2) の両面にそって上昇するようになされている。
なお、ディフューザ(8) の数および配置は、垂直平膜モ
ジュール(2) の大きさに合わせて適宜変更される。As shown in detail in FIG. 4, a downwardly-treated water suction port (24) is opened immediately below an impeller (23) of the ejector (6), and a tip of the nozzle (25) is provided. Is connected to an air suction pipe (5), and further has two diffusers (2) on each side having a diffuser (8).
6) is provided. Four diffusers in total (8)
The shape and arrangement are such that the entire ultrafine bubbles ejected together with the water to be treated as working water rises along both surfaces of each vertical flat membrane module (2).
The number and arrangement of the diffusers (8) are appropriately changed according to the size of the vertical flat membrane module (2).
【0010】上記膜分離装置によれば、処理槽(1) 内の
汚水である被処理水(W) は、クロスフローにより平膜(1
3)を通過するさいに濾過され、濾過水となってスペーサ
(12)によって保持された流路空間を通り、集水管(10)、
ホース(19)を経て濾過水吸引管(17)により所定の場所に
送られる。According to the above-mentioned membrane separation apparatus, the water to be treated (W), which is the sewage in the treatment tank (1), is converted into a flat membrane (1) by cross flow.
3) Filtered when passing through, becomes filtered water and spacer
Through the channel space held by (12), water collecting pipe (10),
It is sent to a predetermined place by a filtered water suction pipe (17) via a hose (19).
【0011】一方、各散気管(4) の上向き噴気孔(3) よ
り噴出せられた比較的大きな気泡は、各垂直平膜モジュ
ール(2) の両面にそって上昇する。また、散気管(4) の
下方において、ディフューザ(8) より超微細気泡が作動
水である被処理水とともに勢よく上向きに吐出せられ
る。そのために、散気管(4) よりの比較的大きな気泡と
あわさることにより、膜表面付近の被処理水に強い乱流
が生じ、膜表面に付着しようとする濾滓を除去してその
成長を防ぐ。また、ディフューザ(8) よりの上向きの吐
出により、垂直平膜モジュール(2) 群の外側では下向き
の流れが生じ、被処理水(W) が循環するので、全体の濃
度が均一化し、低濃度から50,000ppmの高濃度
までの広範囲にわたり安定した濾過が行なわれる。On the other hand, relatively large bubbles ejected from the upward blowing holes (3) of each diffuser (4) rise along both surfaces of each vertical flat membrane module (2). Further, below the diffuser pipe (4), the ultrafine bubbles are discharged from the diffuser (8) together with the water to be treated, which is working water, in a vigorous upward direction. As a result, the turbulent air flows from the air diffuser (4), causing strong turbulence in the water to be treated near the membrane surface. prevent. In addition, the upward discharge from the diffuser (8) causes a downward flow outside the vertical flat membrane module (2) group, and the water to be treated (W) circulates. Stable filtration is performed over a wide range from 1 to 50,000 ppm.
【0012】[0012]
【発明の効果】この発明の膜分離装置によれば、散水管
とエジェクターとの相乗効果により、膜洗浄作業なしに
処理槽の長時間安定運転を継続して行なうことができ、
汚水の高濃度濃縮が可能となる。According to the membrane separation device of the present invention, the synergistic effect of the sprinkler tube and the ejector allows the treatment tank to be continuously operated for a long time without performing the membrane cleaning operation.
High concentration of sewage becomes possible.
【図1】この発明による膜分離装置の垂直断面図であ
る。FIG. 1 is a vertical sectional view of a membrane separation device according to the present invention.
【図2】図1のII−II線にそう断面図である。FIG. 2 is a sectional view taken along line II-II of FIG.
【図3】図1のIII −III 線にそう断面図である。FIG. 3 is a sectional view taken along line III-III in FIG. 1;
【図4】空気吸込管と上向き吐出口を有するディフュー
ザを備えたエジェクターの部分拡大断面図である。FIG. 4 is a partially enlarged cross-sectional view of an ejector provided with a diffuser having an air suction pipe and an upward discharge port.
(1) :処理槽 (2) :垂直平膜モジュール (3) :上向き噴気孔 (4) :散気管 (5) :空気吸込管 (6) :エジェクター (7) :上向き吐出口 (8) :ディフューザ (W) :被処理水 (1): Treatment tank (2): Vertical flat membrane module (3): Upward fumarole (4): Air diffuser (5): Air suction pipe (6): Ejector (7): Upward discharge port (8): Diffuser (W): Water to be treated
Claims (1)
れた垂直平膜モジュールの下方に、上向き噴気孔を有す
る散気管と、空気吸込管を備えかつ被処理水を作動水と
するエジェクターの上向き吐出口を有するディフューザ
とが、前者を上に、後者を下にして配置せられるととも
に、散気管よりの比較的大きな気泡と、ディフューザよ
りの超微細気泡とが、ともに各垂直平膜モジュールの両
面にそって上昇するようになされている膜分離装置。1. An air diffusion pipe having an upward blast hole and an air suction pipe below a vertical flat membrane module immersed in parallel in water to be treated in a treatment tank, and the water to be treated is used as working water. A diffuser having an upward discharge port of the ejector is arranged with the former facing upward and the latter facing downward, and relatively large bubbles from the diffuser and ultrafine bubbles from the diffuser are both vertical flat membranes. A membrane separation device that rises along both sides of the module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24796196A JPH1085565A (en) | 1996-09-19 | 1996-09-19 | Membrane separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24796196A JPH1085565A (en) | 1996-09-19 | 1996-09-19 | Membrane separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH1085565A true JPH1085565A (en) | 1998-04-07 |
Family
ID=17171137
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24796196A Pending JPH1085565A (en) | 1996-09-19 | 1996-09-19 | Membrane separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH1085565A (en) |
Cited By (41)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000009245A3 (en) * | 1998-08-12 | 2000-08-03 | Mitsubishi Rayon Co | Membrane assembly for solid-liquid separation, method of cleaning the same, and detergent |
| WO2001000307A3 (en) * | 1999-06-25 | 2001-07-05 | Millenniumpore Ltd | Self cleaning filter |
| JP2002525197A (en) * | 1998-09-25 | 2002-08-13 | ユー・エス・フィルター・ウェイストウォーター・グループ・インコーポレイテッド | Cleaning device and cleaning method for filtration membrane module |
| EP1115474A4 (en) * | 1998-09-25 | 2005-03-30 | Us Filter Wastewater Group Inc | Apparatus and method for cleaning membrane filtration modules |
| DE102004009886A1 (en) * | 2004-02-26 | 2005-09-15 | Hans Huber Ag Maschinen- Und Anlagenbau | Process and assembly to treat sewage sludge in an assembly that separates sludge and filtrate |
| US6962258B2 (en) | 2000-04-10 | 2005-11-08 | U.S. Filter Wastewater Group, Inc. | Hollow fiber restraining system |
| EP1567249A4 (en) * | 2002-12-05 | 2006-01-11 | Us Filter Wastewater Group Inc | Mixing chamber |
| US7361274B2 (en) | 2002-08-21 | 2008-04-22 | Siemens Water Technologies Corp. | Aeration method |
| EP1911510A3 (en) * | 1998-08-12 | 2008-06-11 | Mitsubishi Rayon Co. Ltd. | A membrane separator assembly |
| US7387723B2 (en) | 2004-04-22 | 2008-06-17 | Siemens Water Technologies Corp. | Filtration apparatus comprising a membrane bioreactor and a treatment vessel for digesting organic materials |
| US7455765B2 (en) | 2006-01-25 | 2008-11-25 | Siemens Water Technologies Corp. | Wastewater treatment system and method |
| US7563363B2 (en) | 2005-10-05 | 2009-07-21 | Siemens Water Technologies Corp. | System for treating wastewater |
| US7591950B2 (en) | 2004-11-02 | 2009-09-22 | Siemens Water Technologies Corp. | Submerged cross-flow filtration |
| US7632439B2 (en) | 2002-02-12 | 2009-12-15 | Siemens Water Technologies Corp. | Poly(ethylene chlorotrifluoroethylene) membranes |
| 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 | Sludge treatment method |
| JP2012106161A (en) * | 2010-11-16 | 2012-06-07 | Toshiba Corp | Membrane separation biological treatment apparatus |
| US8268176B2 (en) | 2003-08-29 | 2012-09-18 | Siemens Industry, Inc. | Backwash |
| US8287743B2 (en) | 2007-05-29 | 2012-10-16 | Siemens Industry, Inc. | Membrane cleaning with pulsed airlift pump |
| US8293098B2 (en) | 2006-10-24 | 2012-10-23 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
| US8318028B2 (en) | 2007-04-02 | 2012-11-27 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
| US8377305B2 (en) | 2004-09-15 | 2013-02-19 | Siemens Industry, Inc. | Continuously variable aeration |
| US8382981B2 (en) | 2008-07-24 | 2013-02-26 | Siemens Industry, Inc. | Frame system for membrane filtration modules |
| US8858796B2 (en) | 2005-08-22 | 2014-10-14 | Evoqua Water Technologies Llc | Assembly for water filtration using a tube manifold to minimise backwash |
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| CN105339312A (en) * | 2013-07-17 | 2016-02-17 | 三菱重工业株式会社 | Water treatment device |
| US9533261B2 (en) | 2012-06-28 | 2017-01-03 | Evoqua Water Technologies Llc | Potting method |
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| US9675938B2 (en) | 2005-04-29 | 2017-06-13 | Evoqua Water Technologies Llc | Chemical clean for membrane filter |
| US9764289B2 (en) | 2012-09-26 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane securement device |
| US9764288B2 (en) | 2007-04-04 | 2017-09-19 | Evoqua Water Technologies Llc | Membrane module protection |
| US9815027B2 (en) | 2012-09-27 | 2017-11-14 | Evoqua Water Technologies Llc | Gas scouring apparatus for immersed membranes |
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| US9925499B2 (en) | 2011-09-30 | 2018-03-27 | Evoqua Water Technologies Llc | Isolation valve with seal for end cap of a filtration system |
| US9962865B2 (en) | 2012-09-26 | 2018-05-08 | Evoqua Water Technologies Llc | Membrane potting methods |
| CN108114601A (en) * | 2016-11-30 | 2018-06-05 | 斗山重工业建设有限公司 | Membrane filtration system |
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| US10427102B2 (en) | 2013-10-02 | 2019-10-01 | Evoqua Water Technologies Llc | Method and device for repairing a membrane filtration module |
| CN112169600A (en) * | 2020-09-15 | 2021-01-05 | 兰德森膜技术南京有限公司 | Flat membrane full-plastic assembly and production method thereof |
-
1996
- 1996-09-19 JP JP24796196A patent/JPH1085565A/en active Pending
Cited By (63)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1911510A3 (en) * | 1998-08-12 | 2008-06-11 | Mitsubishi Rayon Co. Ltd. | A membrane separator assembly |
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