JPH07313851A - Suppressor for Membrane Surface Adhesion in Membrane Separator - Google Patents
Suppressor for Membrane Surface Adhesion in Membrane SeparatorInfo
- Publication number
- JPH07313851A JPH07313851A JP10883394A JP10883394A JPH07313851A JP H07313851 A JPH07313851 A JP H07313851A JP 10883394 A JP10883394 A JP 10883394A JP 10883394 A JP10883394 A JP 10883394A JP H07313851 A JPH07313851 A JP H07313851A
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- separation device
- flow
- ribbon
- suppressor
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
(57)【要約】
【目的】 膜分離装置の膜面に対する洗浄効果を高め
る。
【構成】 隣接するセラミック膜エレメント7a間の各
流路20を上下方向に挿通して可撓性を有するリボン2
1を配置し、各リボン21を上端および下端において固
定部材22に固定した。
(57) [Summary] [Purpose] To enhance the cleaning effect on the membrane surface of the membrane separation device. [Structure] A ribbon 2 having flexibility by inserting each flow path 20 between adjacent ceramic membrane elements 7a in the vertical direction.
1 was arranged and each ribbon 21 was fixed to the fixing member 22 at the upper end and the lower end.
Description
【0001】[0001]
【産業上の利用分野】本発明は、膜面に濾過物等が付着
してケーキ層を形成することを抑制するもので、膜分離
装置における膜面付着物の抑制装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for suppressing the adhered substance on the membrane surface in a membrane separation device, which suppresses the formation of a cake layer due to the adhered substance on the membrane surface.
【0002】[0002]
【従来の技術】従来、膜を使った固液分離装置として
は、例えば図3〜図5に示すような浄水処理に関するも
のがある。図3〜図5において、水槽1内に原水供給管
2から原水3を供給する一方で、攪拌ブロワ4から供給
する空気を散気装置5を通して曝気する。散気装置5の
上方に配置した膜分離装置6は、管状をなす複数のセラ
ミック膜エレメント7aを適当間隔を開けて配置し、各
セラミック膜エレメント7の端部をヘッダ8で結合して
膜モジュール7を形成したものである。2. Description of the Related Art Conventionally, as a solid-liquid separation device using a membrane, there is one related to water purification treatment as shown in FIGS. In FIG. 3 to FIG. 5, while raw water 3 is supplied from the raw water supply pipe 2 into the water tank 1, air supplied from the stirring blower 4 is aerated through the air diffuser 5. The membrane separation device 6 arranged above the air diffuser 5 has a plurality of tubular ceramic membrane elements 7a arranged at appropriate intervals, and the end portions of each ceramic membrane element 7 are joined by a header 8 to form a membrane module. 7 is formed.
【0003】濾過時には、膜分離装置6に吸引管9を通
して吸引ポンプ10による負圧を作用させ、セラミック
膜エレメント7aによって原水3に含まれた濁質を固液
分離し、吸引濾過した膜透過水LFを吸引ポンプ10を
介して系外に取り出す。散気装置5から曝気する空気
は、そのエアリフト作用によって原水と空気の気液混合
流の上向流UFを生起し、この上向流が膜分離装置6の
膜面間を通って水槽1内を循環するとともに、膜面に対
して掃流として作用することにより膜面におけるケーキ
層の成長を抑制する。At the time of filtration, a negative pressure by a suction pump 10 is applied to the membrane separation device 6 through a suction pipe 9, and the ceramic membrane element 7a solid-liquid separates the suspended matter contained in the raw water 3 and suction-filters the permeated water. The LF is taken out of the system via the suction pump 10. The air aerated from the air diffuser 5 causes an upward flow UF of a gas-liquid mixed flow of raw water and air due to its air lift action, and this upward flow passes between the membrane surfaces of the membrane separation device 6 and the inside of the water tank 1 And also acts as a sweep flow on the film surface to suppress the growth of the cake layer on the film surface.
【0004】[0004]
【発明が解決しようとする課題】しかし、上記した従来
の構成において、上向流が膜分離装置6のセラミック膜
エレメント7aの膜面に対して掃流として作用する一方
で、セラミック膜エレメント7aが上向流に対して抵抗
として作用し、上向流が膜分離装置6内において乱流と
なり、上向流が掃流として効果的に作用する上で問題が
あった。したがって、膜面に対するある程度の洗浄効果
を確保するためには攪拌ブロワ4の動力費が高くなる問
題があった。However, in the above-described conventional structure, while the upward flow acts as a sweep flow on the membrane surface of the ceramic membrane element 7a of the membrane separation device 6, the ceramic membrane element 7a There is a problem in that the upward flow acts as a resistance against the upward flow, the upward flow becomes a turbulent flow in the membrane separation device 6, and the upward flow effectively acts as a sweep flow. Therefore, there is a problem that the power cost of the stirring blower 4 becomes high in order to secure a certain cleaning effect on the film surface.
【0005】本発明は上記した課題を解決するもので、
上向流による洗浄効果を高めることができる膜分離装置
における膜面付着物の抑制装置を提供することを目的と
する。The present invention solves the above-mentioned problems.
An object of the present invention is to provide a device for suppressing deposits on the membrane surface in a membrane separation device, which can enhance the cleaning effect due to upward flow.
【0006】[0006]
【課題を解決するための手段】上記した課題を解決する
ために、本発明の膜分離装置における膜面付着物の抑制
装置は、複数の膜エレメントを適当間隙をあけて配置
し、隣接する膜面間に形成した上下方向の流路に気液混
合流からなる掃流を流通させて膜面の洗浄を行う膜分離
装置において、隣接する膜面間の前記各流路を上下方向
に挿通して可撓性を有するリボンを配置し、各リボンを
上端および下端において固定部材に固定した構成とする
ものである。In order to solve the above-mentioned problems, the device for suppressing the deposits on the membrane surface in the membrane separation device of the present invention has a plurality of membrane elements arranged with appropriate gaps and adjacent membranes. In a membrane separation device that cleans the membrane surface by passing a sweep stream consisting of a gas-liquid mixed flow through the vertical channels formed between the surfaces, vertically inserting each of the channels between adjacent membrane surfaces. Flexible ribbons are arranged and each ribbon is fixed to a fixing member at the upper and lower ends.
【0007】[0007]
【作用】上記した構成により、上向流は膜分離装置の各
膜エレメント間に形成した流路を掃流として流れ、膜面
に付着する濾過物を洗い流し、膜面上におけるケーキ層
の成長を抑制する。このとき、膜エレメント間に配置し
たリボンが上向流の流れを受けて揺れ動き、リボンがそ
の揺動によって膜面上の付着物を叩くように作用し、膜
面上の付着物を絶えず除去する。With the above-described structure, the upward flow flows as a sweep flow through the flow path formed between the membrane elements of the membrane separation device to wash away the filtered material adhering to the membrane surface and to grow the cake layer on the membrane surface. Suppress. At this time, the ribbon arranged between the membrane elements is swayed by the flow of the upward flow, and the action of the ribbon acts to hit the deposit on the membrane surface by the swing, and continuously removes the deposit on the membrane surface. .
【0008】このため、掃流によって膜面に濾過物が付
着することを抑制するとともに、リボンによって膜面に
付着した付着物を除去するので、従来に比べて、洗浄効
果を高めることができ、洗浄に要する駆動力の低減を図
ることができる。For this reason, it is possible to suppress the adherence of the filtered material to the membrane surface due to the sweeping flow, and to remove the adhered material attached to the membrane surface by the ribbon, so that the cleaning effect can be enhanced as compared with the conventional case. The driving force required for cleaning can be reduced.
【0009】[0009]
【実施例】以下、本発明の一実施例を図面に基づいて説
明する。先に図3〜図5において説明したものと同様の
作用を行う部材については同一番号を付して説明を省略
する。図1〜図2において、膜分離装置6は複数の膜モ
ジュール7を上下に積層したものであり、各膜モジュー
ル7は複数のセラミック膜エレメント7aの端部をヘッ
ダ8で結合したものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. Members having the same functions as those described above with reference to FIGS. 3 to 5 are designated by the same reference numerals and the description thereof will be omitted. 1 to 2, the membrane separation device 6 is formed by stacking a plurality of membrane modules 7 on top of each other, and each membrane module 7 is formed by connecting end portions of a plurality of ceramic membrane elements 7a with a header 8.
【0010】各セラミック膜エレメント7aは適当間隙
をあけて配置しており、隣接するセラミック膜エレメン
ト7aの膜面間には上下方向の流路20を形成してい
る。この各流路20を上下方向に挿通して複数のリボン
21を配置しており、リボン21は樹脂材や金属箔等か
らなるもので可撓性を有している。各リボン21は上端
および下端においてバンド状の固定部材22に固定して
いる。Each ceramic membrane element 7a is arranged with an appropriate gap, and a vertical passage 20 is formed between the membrane surfaces of adjacent ceramic membrane elements 7a. A plurality of ribbons 21 are arranged by vertically penetrating each of the flow paths 20, and the ribbons 21 are made of a resin material, a metal foil, or the like and have flexibility. Each ribbon 21 is fixed to a band-shaped fixing member 22 at the upper and lower ends.
【0011】この構成によれば、濾過時にはセラミック
膜エレメント7aによって原水3に含まれた濁質を固液
分離し、吸引濾過した膜透過水LFを吸引ポンプ10を
介して系外に取り出す。一方、散気装置5から曝気する
空気によって生起した上向流UFがセラミック膜エレメ
ント7aの膜面間の流路20を通って水槽1内を循環す
るとともに、膜面に対して掃流として作用することによ
り膜面におけるケーキ層の成長を抑制する。According to this structure, during filtration, the suspended matter contained in the raw water 3 is solid-liquid separated by the ceramic membrane element 7a, and the membrane-permeated water LF suction-filtered is taken out of the system via the suction pump 10. On the other hand, the upward flow UF generated by the air aerated from the air diffuser 5 circulates in the water tank 1 through the flow path 20 between the membrane surfaces of the ceramic membrane element 7a, and acts as a sweep flow on the membrane surface. This suppresses the growth of the cake layer on the film surface.
【0012】このとき、隣接するセラミック膜エレメン
ト7a間に配置したリボン21が上向流の流れを受けて
揺れ動き、リボン21がその揺動によって膜面上の付着
物を叩くように作用し、膜面上の付着物を絶えず除去す
る。At this time, the ribbon 21 arranged between the adjacent ceramic membrane elements 7a is swayed by the upward flow, and the oscillating movement causes the ribbon 21 to strike the deposit on the membrane surface. The deposits on the surface are constantly removed.
【0013】本実施例においては、管状膜モジュールに
ついて説明したが、平膜状膜モジュールにも適用するこ
とは可能である。In this embodiment, the tubular membrane module has been described, but it can be applied to a flat membrane module.
【0014】[0014]
【発明の効果】以上述べたように本発明によれば、掃流
によって膜面に濾過物が付着することを抑制するととも
に、リボンによって膜面に付着した付着物を除去するの
で、従来に比べて、洗浄効果を高めることができ、洗浄
に要する駆動力の低減を図ることができる。As described above, according to the present invention, it is possible to suppress the adherence of the filtered material to the film surface by the sweep flow and to remove the adhered material adhered to the film surface by the ribbon. As a result, the cleaning effect can be enhanced and the driving force required for cleaning can be reduced.
【図1】本発明の一実施例を示す膜分離装置の縦断面図
である。FIG. 1 is a vertical cross-sectional view of a membrane separation device showing an embodiment of the present invention.
【図2】同実施例における膜分離装置の横断面図であ
る。FIG. 2 is a cross-sectional view of the membrane separation device in the same example.
【図3】従来の膜分離装置の構成を示す模式図である。FIG. 3 is a schematic diagram showing a configuration of a conventional membrane separation device.
【図4】従来の膜分離装置の斜視図である。FIG. 4 is a perspective view of a conventional membrane separation device.
【図5】従来のセラミック膜エレメントにおける濾過作
用を示す模式図である。FIG. 5 is a schematic view showing a filtering action in a conventional ceramic membrane element.
1 水槽 3 原水 5 散気装置 6 膜分離装置 7 膜モジュール 7a セラミック膜エレメント 10 吸引ポンプ 20 流路 21 リボン 1 Water Tank 3 Raw Water 5 Diffuser 6 Membrane Separation Device 7 Membrane Module 7a Ceramic Membrane Element 10 Suction Pump 20 Flow Path 21 Ribbon
Claims (1)
配置し、隣接する膜面間に形成した上下方向の流路に気
液混合流からなる掃流を流通させて膜面の洗浄を行う膜
分離装置において、隣接する膜面間の前記各流路を上下
方向に挿通して可撓性を有するリボンを配置し、各リボ
ンを上端および下端において固定部材に固定したことを
特徴とする膜分離装置における膜面付着物の抑制装置。1. A membrane surface is cleaned by arranging a plurality of membrane elements with appropriate gaps, and passing a scavenging flow consisting of a gas-liquid mixed flow through a vertical flow path formed between adjacent membrane surfaces. In the membrane separation device, a flexible ribbon is arranged by vertically inserting the respective flow paths between adjacent membrane surfaces, and each ribbon is fixed to a fixing member at an upper end and a lower end. A device for suppressing film surface deposits in a separation device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10883394A JPH07313851A (en) | 1994-05-24 | 1994-05-24 | Suppressor for Membrane Surface Adhesion in Membrane Separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10883394A JPH07313851A (en) | 1994-05-24 | 1994-05-24 | Suppressor for Membrane Surface Adhesion in Membrane Separator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07313851A true JPH07313851A (en) | 1995-12-05 |
Family
ID=14494713
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10883394A Pending JPH07313851A (en) | 1994-05-24 | 1994-05-24 | Suppressor for Membrane Surface Adhesion in Membrane Separator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07313851A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002030550A1 (en) * | 2000-10-09 | 2002-04-18 | U.S. Filter Wastewater Group, Inc. | Improved membrane filtration system |
US7220358B2 (en) | 2004-02-23 | 2007-05-22 | Ecolab Inc. | Methods for treating membranes and separation facilities and membrane treatment composition |
US7392811B2 (en) | 2004-02-23 | 2008-07-01 | Ecolab Inc. | Delivery head for multiple phase treatment composition, vessel including a delivery head, and method for treating a vessel interior surface |
CN105884016A (en) * | 2014-12-23 | 2016-08-24 | 江南大学 | Method for manufacturing immersed square staggered arrangement tubular membrane bioreactor |
CN105884014A (en) * | 2014-12-23 | 2016-08-24 | 江南大学 | Method for manufacturing immersed regularly triangular staggered arrangement tubular membrane bioreactor |
CN105884015A (en) * | 2014-12-23 | 2016-08-24 | 江南大学 | Method for manufacturing immersed type square in-line arrangement tubular membrane bioreactor |
-
1994
- 1994-05-24 JP JP10883394A patent/JPH07313851A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002030550A1 (en) * | 2000-10-09 | 2002-04-18 | U.S. Filter Wastewater Group, Inc. | Improved membrane filtration system |
AU2001291514B2 (en) * | 2000-10-09 | 2006-11-09 | Evoqua Water Technologies Llc | Improved membrane filtration system |
US7220358B2 (en) | 2004-02-23 | 2007-05-22 | Ecolab Inc. | Methods for treating membranes and separation facilities and membrane treatment composition |
US7392811B2 (en) | 2004-02-23 | 2008-07-01 | Ecolab Inc. | Delivery head for multiple phase treatment composition, vessel including a delivery head, and method for treating a vessel interior surface |
CN105884016A (en) * | 2014-12-23 | 2016-08-24 | 江南大学 | Method for manufacturing immersed square staggered arrangement tubular membrane bioreactor |
CN105884014A (en) * | 2014-12-23 | 2016-08-24 | 江南大学 | Method for manufacturing immersed regularly triangular staggered arrangement tubular membrane bioreactor |
CN105884015A (en) * | 2014-12-23 | 2016-08-24 | 江南大学 | Method for manufacturing immersed type square in-line arrangement tubular membrane bioreactor |
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