JPH04317793A - Water treatment apparatus - Google Patents

Water treatment apparatus

Info

Publication number
JPH04317793A
JPH04317793A JP8429991A JP8429991A JPH04317793A JP H04317793 A JPH04317793 A JP H04317793A JP 8429991 A JP8429991 A JP 8429991A JP 8429991 A JP8429991 A JP 8429991A JP H04317793 A JPH04317793 A JP H04317793A
Authority
JP
Japan
Prior art keywords
membrane module
liquid
treated
membrane
water treatment
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
JP8429991A
Other languages
Japanese (ja)
Inventor
Masatsugu Yamagata
山縣 昌継
Yoshihisa Narukami
善久 鳴上
Kanji Tokushima
幹治 徳島
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP8429991A priority Critical patent/JPH04317793A/en
Publication of JPH04317793A publication Critical patent/JPH04317793A/en
Pending legal-status Critical Current

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  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PURPOSE:To prolong the time until a membrane module which is immersed in a liquid to be treated in a water treatment apparatus should be back-washed. CONSTITUTION:A membrane module 4 has membrane elements 3 which are able to filter a liquid to be treated 2. The membrane module 4 is supported by rotary shafts 11, 12 and the rotary shaft 11 is driven by a motor 14. Due to this, rotating force is given to the membrane module 4 immersed in the liquid to be treated 2 and flow speed is applied to the surfaces of the membrane elements 3 and thus scales are removed. Scale formation can be reduced even if the water treatment apparatus is operated for a long duration and the time until back washing becomes necessary is greatly prolonged.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は水処理装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to water treatment equipment.

【0002】0002

【従来の技術】下水などの汚水を処理するための水処理
装置として、従来、被処理液を濾過可能な膜エレメント
を有してこの被処理液中に浸漬される膜モジュールを備
えたものが提案されている。
[Prior Art] Conventionally, water treatment equipment for treating wastewater such as sewage has been equipped with a membrane module that has a membrane element capable of filtering the liquid to be treated and is immersed in the liquid to be treated. Proposed.

【0003】図4は従来のこの種の水処理装置を示すも
のである。ここで1は処理槽で、その内部には被処理液
2が貯留されている。処理槽1の内部には、多数のチュ
ーブ状の膜エレメント3を備えた膜モジュール4が、被
処理液2の中に没するようにして設けられている。膜モ
ジュール4は膜エレメント3の両端に位置する一対のヘ
ッダ5A,5Bを有し、これらヘッダ5A,5Bによっ
て多数の膜エレメント3をユニット化している。ヘッダ
5Bは、各膜エレメント3で濾過された濾過水を集めて
管路6へ送るための濾過水通路としても機能する。この
管路6は濾過水を槽外へ導くためのもので、その途中に
は吸引ポンプ7が設けられている。膜モジュール4より
も下方における処理槽1の内部には散気管8が設けられ
、この散気管8には槽外のブロワ9が接続されている。
FIG. 4 shows a conventional water treatment device of this type. Here, 1 is a processing tank in which a liquid to be processed 2 is stored. Inside the treatment tank 1, a membrane module 4 including a large number of tube-shaped membrane elements 3 is provided so as to be submerged in the liquid to be treated 2. The membrane module 4 has a pair of headers 5A and 5B located at both ends of the membrane element 3, and a large number of membrane elements 3 are made into a unit by these headers 5A and 5B. The header 5B also functions as a filtrate passage for collecting filtrate water filtered by each membrane element 3 and sending it to the pipe line 6. This pipe line 6 is for guiding the filtered water out of the tank, and a suction pump 7 is provided in the middle thereof. An aeration pipe 8 is provided inside the processing tank 1 below the membrane module 4, and a blower 9 outside the tank is connected to the aeration pipe 8.

【0004】このような構成においてブロワ9から散気
管8を経て処理槽1の内部に空気を供給すると、エアリ
フト効果により被処理液2が膜モジュール4に向け上昇
されて処理槽1の内部を循環するとともに、被処理液2
に対するエアレーションが行われる。かつ吸引ポンプ7
を運転することによって膜エレメント3の内部に吸引負
圧が作用され、被処理液2の濾過が行われる。濾過水は
管路6を経て処理槽1の外へ取り出される。
In such a configuration, when air is supplied from the blower 9 to the inside of the processing tank 1 through the aeration pipe 8, the liquid to be processed 2 is lifted toward the membrane module 4 due to the air lift effect and circulated inside the processing tank 1. At the same time, the liquid to be treated 2
Aeration is performed. And suction pump 7
By operating the membrane element 3, suction negative pressure is applied to the inside of the membrane element 3, and the liquid to be treated 2 is filtered. The filtered water is taken out of the treatment tank 1 through a pipe 6.

【0005】ところで被処理液2は一般に多量のMLS
Sを含むため、上記構成の水処理装置を運転すると膜エ
レメント3の表面に徐々にスケールが発生する。このス
ケールは、散気管8から上向きに吹き込まれる空気と、
この空気のエアリフト効果により上向きに流動される被
処理液との気液混相流によってある程度取り除かれる。
By the way, the liquid to be treated 2 generally contains a large amount of MLS.
Since it contains S, scale gradually forms on the surface of the membrane element 3 when the water treatment apparatus having the above configuration is operated. This scale corresponds to the air blown upward from the air diffuser 8,
This air is removed to some extent by a gas-liquid multiphase flow with the liquid to be treated that flows upward due to the air lift effect of the air.

【0006】しかし水処理装置の運転時間が長時間に及
ぶと、膜エレメント3の表面に発生するスケールの量が
多くなり、膜エレメント3の濾過性能が大幅に低下して
装置の運転に支障をきたすおそれがある。
[0006] However, when the water treatment equipment is operated for a long time, the amount of scale generated on the surface of the membrane element 3 increases, and the filtration performance of the membrane element 3 decreases significantly, which hinders the operation of the equipment. There is a risk that this may occur.

【0007】そこで従来、このような場合には、管路6
から各膜エレメント3の内部へ加圧流体を供給し、この
加圧流体を膜エレメント3の表面から処理槽1の内部へ
噴出させることによってスケールの除去を行う、いわゆ
る逆洗が行われている。
Conventionally, in such a case, the pipe line 6
So-called backwashing is performed in which scale is removed by supplying pressurized fluid to the inside of each membrane element 3 and ejecting this pressurized fluid from the surface of the membrane element 3 into the inside of the processing tank 1. .

【0008】[0008]

【発明が解決しようとする課題】しかし、このような逆
流をしばしば行うと、そのための作業工数が多大なもの
となって好ましくなく、また逆洗を行っている間は水処
理装置自体を稼働させることができず、運転休止状態に
なってしまうという問題点がある。
[Problem to be solved by the invention] However, if such backwashing is performed frequently, it requires a large amount of work, which is undesirable, and the water treatment equipment itself must be operated while backwashing is being performed. However, there is a problem in that the system is unable to do so and ends up in a suspended state.

【0009】そこで本発明はこのような問題点を解決し
、逆洗を行うまでの時間をできるだけ延ばすことができ
るようにすることを目的とする。
SUMMARY OF THE INVENTION It is an object of the present invention to solve these problems and to extend the time required for backwashing as much as possible.

【0010】0010

【課題を解決するための手段】上記目的を達成するため
本発明は、被処理液を濾過可能な膜エレメントを有して
前記被処理液中に浸漬される膜モジュールと、この膜モ
ジュールに回転を付与する手段とを備えた構成としたも
のである。
[Means for Solving the Problems] In order to achieve the above object, the present invention provides a membrane module that has a membrane element capable of filtering a liquid to be treated and is immersed in the liquid to be treated, and a membrane module that rotates around the membrane module. The present invention is configured to include means for imparting.

【0011】[0011]

【作用】このような構成によれば、被処理液中に浸漬さ
れた膜モジュールを回転させることで膜エレメントの表
面に流速が与えられ、これにより膜エレメントの表面に
生じるスケールが取り除かれる。このため水処理装置を
長時間運転してもスケールの発生が少なく、逆洗が必要
になるまでの時間が大幅に延長される。
[Operation] According to this structure, by rotating the membrane module immersed in the liquid to be treated, a flow velocity is applied to the surface of the membrane element, thereby removing scale formed on the surface of the membrane element. Therefore, even if the water treatment equipment is operated for a long time, there is little scale formation, and the time until backwashing is required is significantly extended.

【0012】0012

【実施例】以下、本発明の一実施例を、図1および図2
にもとづき、図4に示した部材と同一の部材には同一の
参照番号を付して、詳細に説明する。
[Embodiment] An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.
Based on this, the same members as those shown in FIG. 4 are given the same reference numerals and will be described in detail.

【0013】図1および図2に示すように、膜モジュー
ル4は、一対の円盤状のヘッダ5A,5Bと、これらヘ
ッダ5A,5Bどうしの間にわたされる多数のチューブ
状の膜エレメント3とを有して、概略円柱状に形成され
ている。膜エレメント3は、膜モジュール4の軸心方向
と平行に配置されている。ヘッダ5Aには回転軸11が
取り付けられ、またヘッダ5Bには管路として機能する
中空の回転軸12が取り付けられている。両回転軸11
,12は膜モジュール4が浸漬状態で水平方向となるよ
うに処理槽1の壁部を貫通し、水密シール機能を併せ持
った軸受装置13によって、それぞれ回転自在に支持さ
れている。 回転軸11は槽外においてモータ14に連結されている
。回転軸12はヘッダ5Bの内部に連通するようにこの
ヘッダ5Bに接続され、かつ槽外においてロータリジョ
イント15を介して管路16に連結されている。管路1
6には図4の場合と同様の吸引ポンプ7が設けられてい
る。
As shown in FIGS. 1 and 2, the membrane module 4 includes a pair of disk-shaped headers 5A, 5B and a large number of tube-shaped membrane elements 3 passed between these headers 5A, 5B. It is formed into a roughly cylindrical shape. The membrane element 3 is arranged parallel to the axial direction of the membrane module 4. A rotating shaft 11 is attached to the header 5A, and a hollow rotating shaft 12 that functions as a conduit is attached to the header 5B. Both rotating shafts 11
, 12 penetrate through the wall of the processing tank 1 so that the membrane module 4 is oriented horizontally in the immersed state, and are each rotatably supported by a bearing device 13 which also has a watertight sealing function. The rotating shaft 11 is connected to a motor 14 outside the tank. The rotating shaft 12 is connected to the header 5B so as to communicate with the inside of the header 5B, and is connected to a pipe line 16 via a rotary joint 15 outside the tank. Conduit 1
6 is provided with a suction pump 7 similar to that in FIG.

【0014】このような構成において、水処理を行う際
には、吸引ポンプ7およびブロワ9を運転するとともに
、モータ14を運転して膜モジュール4をその軸心まわ
りに回転させる。すると、吸引濾過により生じた濾過水
は、膜エレメント3、ヘッダ5B、中空の回転軸12、
ロータリジョイント15および管路16を経て、槽外へ
取り出される。
In such a configuration, when performing water treatment, the suction pump 7 and the blower 9 are operated, and the motor 14 is operated to rotate the membrane module 4 about its axis. Then, the filtered water generated by suction filtration is transferred to the membrane element 3, header 5B, hollow rotating shaft 12,
It is taken out of the tank via the rotary joint 15 and the pipe line 16.

【0015】このとき、図4の場合と同様に、散気管8
からの空気流にもとづく気液混相流によって、膜エレメ
ント3の表面に発生するスケールがある程度取り除かれ
る。かつ、膜モジュール4を回転させることで、膜エレ
メント3の表面に流速が生じ、これによってスケールの
除去が行われる。なお、この流速、すなわち膜エレメン
ト3と被処理液2との相対速度は、0.3 〜3m/s
程度が適当である。
At this time, as in the case of FIG.
The scale generated on the surface of the membrane element 3 is removed to some extent by the gas-liquid multiphase flow based on the air flow from the membrane element 3. Further, by rotating the membrane module 4, a flow velocity is generated on the surface of the membrane element 3, thereby removing scale. Note that this flow rate, that is, the relative velocity between the membrane element 3 and the liquid to be treated 2 is 0.3 to 3 m/s.
The degree is appropriate.

【0016】このように良好にスケールが取り除かれる
ことで、水処理装置を長時間運転してもスケールの発生
をわずかなものとすることができ、逆洗が必要になるま
での時間が大幅に延長される。このため、逆洗のための
作業工数を低減できるとともに、逆洗を行うことにより
装置の稼働率が低下することが効果的に防止される。
[0016] By effectively removing scale in this way, even if the water treatment equipment is operated for a long time, the generation of scale can be minimized, and the time until backwashing is required can be significantly shortened. It will be extended. Therefore, the number of work steps required for backwashing can be reduced, and a decrease in the operating rate of the apparatus due to backwashing can be effectively prevented.

【0017】また、スケールの発生が少ないことから、
膜モジュール4のフラックス量を多くすることができ、
効率の良い運転が可能になる。図3は本発明の他の実施
例の水処理装置を示す。すなわち、図1および図2の実
施例では、膜エレメント3は膜モジュール4の軸心方向
と平行に配置されていたが、ここでは、膜モジュール4
の軸心と角度をなすようにねじった状態で配置されてい
る。このような構成によれば、膜エレメント3は、膜モ
ジュール4の回転方向と直角な方向に対し角度を有する
ことになるため、被処理液2が膜エレメント3の表面に
沿って複雑に流動する。このため、いっそう良好にスケ
ールの除去が行われる。
[0017] Also, since there is less scale generation,
The amount of flux in the membrane module 4 can be increased,
Enables efficient driving. FIG. 3 shows a water treatment device according to another embodiment of the present invention. That is, in the embodiments shown in FIGS. 1 and 2, the membrane element 3 was arranged parallel to the axial direction of the membrane module 4, but here, the membrane element 3 is arranged parallel to the axial direction of the membrane module 4.
It is arranged in a twisted state so as to form an angle with the axis of the According to such a configuration, the membrane element 3 has an angle with respect to the direction perpendicular to the rotational direction of the membrane module 4, so that the liquid to be treated 2 flows in a complicated manner along the surface of the membrane element 3. . For this reason, scale removal is performed even better.

【0018】[0018]

【発明の効果】以上述べたように本発明によると、被処
理液中に浸漬される膜モジュールを回転させるようにし
たため、膜モジュールを構成する膜エレメントの表面に
流速を与えることができ、これにより膜エレメントの表
面に生じるスケールを取り除くことができる。この結果
スケールの発生を低減でき、逆洗が必要になるまでの時
間を大幅に延長することができる。
As described above, according to the present invention, since the membrane module immersed in the liquid to be treated is rotated, a flow velocity can be applied to the surface of the membrane elements constituting the membrane module. The scale generated on the surface of the membrane element can be removed by this method. As a result, the occurrence of scale can be reduced and the time until backwashing becomes necessary can be significantly extended.

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

【図1】本発明の一実施例の水処理装置の概略構成を示
す正面図である。
FIG. 1 is a front view showing a schematic configuration of a water treatment apparatus according to an embodiment of the present invention.

【図2】図1における膜モジュールの斜視図である。FIG. 2 is a perspective view of the membrane module in FIG. 1;

【図3】本発明の他の実施例の水処理装置の概略構成を
示す正面図である。
FIG. 3 is a front view showing a schematic configuration of a water treatment device according to another embodiment of the present invention.

【図4】従来の水処理装置の概略構成を示す正面図であ
る。
FIG. 4 is a front view showing a schematic configuration of a conventional water treatment device.

【符号の説明】[Explanation of symbols]

2        被処理液 3        膜エレメント 4        膜モジュール 11,12    回転軸 14        モータ 2. Liquid to be treated 3. Membrane element 4 Membrane module 11, 12 Rotation axis 14 Motor

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  被処理液を濾過可能な膜エレメントを
有して前記被処理液中に浸漬される膜モジュールと、こ
の膜モジュールに回転を付与する手段とを備えたことを
特徴とする水処理装置。
1. A water filter comprising a membrane module having a membrane element capable of filtering a liquid to be treated and immersed in the liquid to be treated, and means for imparting rotation to the membrane module. Processing equipment.
JP8429991A 1991-04-17 1991-04-17 Water treatment apparatus Pending JPH04317793A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8429991A JPH04317793A (en) 1991-04-17 1991-04-17 Water treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8429991A JPH04317793A (en) 1991-04-17 1991-04-17 Water treatment apparatus

Publications (1)

Publication Number Publication Date
JPH04317793A true JPH04317793A (en) 1992-11-09

Family

ID=13826601

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8429991A Pending JPH04317793A (en) 1991-04-17 1991-04-17 Water treatment apparatus

Country Status (1)

Country Link
JP (1) JPH04317793A (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1224965A1 (en) * 2000-05-21 2002-07-24 Berghof Filtrations- und Anlagentechnik GmbH & Co. KG. Device and method for separating a permeate
WO2006074519A1 (en) 2005-01-14 2006-07-20 Siemens Water Technologies Corp. Filtration system
CN100349645C (en) * 2005-09-23 2007-11-21 浙江大学 Revolve type film separator
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US9022224B2 (en) 2010-09-24 2015-05-05 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
US9533261B2 (en) 2012-06-28 2017-01-03 Evoqua Water Technologies Llc Potting method
US9604166B2 (en) 2011-09-30 2017-03-28 Evoqua Water Technologies Llc Manifold arrangement
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
US9914097B2 (en) 2010-04-30 2018-03-13 Evoqua Water Technologies Llc Fluid flow distribution device
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
US10322375B2 (en) 2015-07-14 2019-06-18 Evoqua Water Technologies Llc Aeration device for filtration system
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Cited By (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1224965A1 (en) * 2000-05-21 2002-07-24 Berghof Filtrations- und Anlagentechnik GmbH & Co. KG. Device and method for separating a permeate
WO2006074519A1 (en) 2005-01-14 2006-07-20 Siemens Water Technologies Corp. Filtration system
EP1850950A1 (en) * 2005-01-14 2007-11-07 Siemens Water Technologies Corp. Filtration system
EP1850950A4 (en) * 2005-01-14 2009-09-02 Siemens Water Tech Corp Filtration system
AU2006206046B2 (en) * 2005-01-14 2010-10-28 Evoqua Water Technologies Llc Filtration system
US9675938B2 (en) 2005-04-29 2017-06-13 Evoqua Water Technologies Llc Chemical clean for membrane filter
US8858796B2 (en) 2005-08-22 2014-10-14 Evoqua Water Technologies Llc Assembly for water filtration using a tube manifold to minimise backwash
US8894858B1 (en) 2005-08-22 2014-11-25 Evoqua Water Technologies Llc Method and assembly for water filtration using a tube manifold to minimize backwash
CN100349645C (en) * 2005-09-23 2007-11-21 浙江大学 Revolve type film separator
US9764288B2 (en) 2007-04-04 2017-09-19 Evoqua Water Technologies Llc Membrane module protection
US9573824B2 (en) 2007-05-29 2017-02-21 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US8840783B2 (en) 2007-05-29 2014-09-23 Evoqua Water Technologies Llc Water treatment membrane cleaning with pulsed airlift pump
US9206057B2 (en) 2007-05-29 2015-12-08 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US10507431B2 (en) 2007-05-29 2019-12-17 Evoqua Water Technologies Llc Membrane cleaning with pulsed airlift pump
US9023206B2 (en) 2008-07-24 2015-05-05 Evoqua Water Technologies Llc Frame system for membrane filtration modules
US8956464B2 (en) 2009-06-11 2015-02-17 Evoqua Water Technologies Llc Method of cleaning membranes
US10441920B2 (en) 2010-04-30 2019-10-15 Evoqua Water Technologies Llc Fluid flow distribution device
US9914097B2 (en) 2010-04-30 2018-03-13 Evoqua Water Technologies Llc Fluid flow distribution device
US9630147B2 (en) 2010-09-24 2017-04-25 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9022224B2 (en) 2010-09-24 2015-05-05 Evoqua Water Technologies Llc Fluid control manifold for membrane filtration system
US9604166B2 (en) 2011-09-30 2017-03-28 Evoqua Water Technologies Llc Manifold arrangement
US9925499B2 (en) 2011-09-30 2018-03-27 Evoqua Water Technologies Llc Isolation valve with seal for end cap of a filtration system
US10391432B2 (en) 2011-09-30 2019-08-27 Evoqua Water Technologies Llc Manifold arrangement
US11065569B2 (en) 2011-09-30 2021-07-20 Rohm And Haas Electronic Materials Singapore Pte. Ltd. Manifold arrangement
US9533261B2 (en) 2012-06-28 2017-01-03 Evoqua Water Technologies Llc Potting method
US9764289B2 (en) 2012-09-26 2017-09-19 Evoqua Water Technologies Llc Membrane securement device
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