JP2982842B2 - Membrane module - Google Patents
Membrane moduleInfo
- Publication number
- JP2982842B2 JP2982842B2 JP5015779A JP1577993A JP2982842B2 JP 2982842 B2 JP2982842 B2 JP 2982842B2 JP 5015779 A JP5015779 A JP 5015779A JP 1577993 A JP1577993 A JP 1577993A JP 2982842 B2 JP2982842 B2 JP 2982842B2
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- spacer
- membrane module
- support
- filtration
- 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.)
- Expired - Lifetime
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、水処理装置などにおい
て使用される膜分離ユニットの膜モジュールに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane module of a membrane separation unit used in a water treatment device or the like.
【0002】[0002]
【従来の技術】従来、この種の膜分離ユニットは、図2
に全体構成を示したように、処理槽の内部に設けられた
ケーシング1内に複数の膜モジュール2を適当な間隔で
平行に配置することによって構成している。2. Description of the Related Art Conventionally, a membrane separation unit of this type is shown in FIG.
As shown in FIG. 1, a plurality of membrane modules 2 are arranged in parallel at appropriate intervals in a casing 1 provided inside a processing tank.
【0003】そして、膜モジュール2の下方に、槽内の
被処理液に酸素または空気を供給する曝気装置7を設
け、この曝気装置7によって矢印Bのように槽外から酸
素または空気を取り込み、矢印Cで示される気泡流を膜
モジュール2どうしの間隙に供給することにより、槽内
に矢印C,Dで示される気液混合攪拌流を生起するとと
もに、濾過膜表面に付着するケーキ層を剥離洗浄してい
る。[0003] An aerator 7 for supplying oxygen or air to the liquid to be treated in the tank is provided below the membrane module 2, and oxygen or air is taken in from the outside of the tank as shown by an arrow B by the aerator 7. By supplying the bubble flow indicated by arrow C to the gap between the membrane modules 2, a gas-liquid mixed stirring flow indicated by arrows C and D is generated in the tank, and the cake layer adhering to the surface of the filtration membrane is separated. Has been washed.
【0004】膜モジュール2においては、図3に示した
ように、矩形平板状の膜支持体3の表面に有機濾過膜4
を配置している。また、有機濾過膜4と膜支持体3との
間に膜4と同寸法のフェルト状スペーサ5を介装し、濾
過膜4と膜支持体3との密着を防止して、濾過膜4の内
側に膜透過液流路を形成している。[0004] In the membrane module 2, as shown in FIG. 3, an organic filtration membrane 4 is provided on the surface of a rectangular plate-shaped membrane support 3.
Has been arranged. In addition, a felt-like spacer 5 having the same size as the membrane 4 is interposed between the organic filtration membrane 4 and the membrane support 3 to prevent the filtration membrane 4 and the membrane support 3 from sticking to each other. A membrane permeate flow path is formed inside.
【0005】このとき、膜4の周縁部に対応したフェル
ト状スペーサ5の周縁の両面に接着剤を塗布して、スペ
ーサ5を膜支持体3に接着固定するとともに、スペーサ
5に接着剤を保持させて、濾過膜4を充分溶かすことに
より、スペーサ5上に濾過膜4を周縁部で溶着させてい
る。At this time, an adhesive is applied to both sides of the peripheral edge of the felt-like spacer 5 corresponding to the peripheral portion of the film 4 to fix the spacer 5 to the film support 3 and hold the adhesive on the spacer 5. Then, by sufficiently dissolving the filtration membrane 4, the filtration membrane 4 is welded to the spacer 5 at the periphery.
【0006】そして、濾過膜4よりも内側に通じた透過
液吸引管を設け、この透過液吸引管を通して膜モジュー
ル2内に負圧を与えることにより、槽内の被処理液を濾
過膜4を通して吸引濾過している。[0006] A permeated liquid suction pipe is provided inside the filtration membrane 4, and a negative pressure is applied to the membrane module 2 through the permeated liquid suction pipe so that the liquid to be treated in the tank passes through the filtration membrane 4. Suction filtration.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、上記し
た従来の膜モジュール2は、図示したように通常、濾過
膜4とフェルト状スペーサ5とが同じ大きさに形成され
ており、接着剤がフェルト状スペーサ5の厚み方向に満
遍なく浸透していない場合は、スペーサ5の側面6から
汚泥などを含んだ被処理液が侵入するという問題点があ
る。However, in the conventional membrane module 2 described above, the filter membrane 4 and the felt-like spacer 5 are usually formed in the same size as shown in the drawing, and the adhesive is made of felt-like. If the liquid does not permeate uniformly in the thickness direction of the spacer 5, there is a problem that the liquid to be treated including sludge enters from the side surface 6 of the spacer 5.
【0008】本発明は上記問題を解決するもので、被処
理液の侵入を防止し、好適に固液分離できる膜モジュー
ルを提供することを目的とするものである。An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to provide a membrane module capable of preventing intrusion of a liquid to be treated and capable of suitably performing solid-liquid separation.
【0009】[0009]
【課題を解決するための手段】上記問題を解決するため
に、本発明の膜モジュールは、処理槽の内部に設けるケ
ーシング内に適当な間隔で平行に配置し、下方に配置し
た曝気装置から供給する空気によって生起する気液混合
攪拌流で膜面を洗浄する膜モジュールであって、膜支持
体と濾過膜との間に介装するフェルト状スペーサを周縁
部で膜支持体に接着し、スペーサの周縁部を覆って配置
する濾過膜をスペーサより大きく形成した周縁部におい
て膜支持体に接着固定したものである。In order to solve the above problems, a membrane module according to the present invention is provided with a casing provided inside a processing tank.
In parallel at appropriate intervals and below.
-Liquid mixing caused by air supplied from aerated aerators
A membrane module that cleans the membrane surface with agitated flow, supporting the membrane
Around the felt spacer interposed between the body and the filtration membrane
Adhere to the membrane support at the part and cover the periphery of the spacer
At the periphery where the filter membrane to be formed is larger than the spacer
The adhesive was fixed to the membrane support .
【0010】[0010]
【作用】上記構成により、濾過膜をスペーサより大きく
形成し、スペーサを覆って配置して、濾過膜の周縁部に
おいてスペーサを介さずに膜支持体に直接接着固定した
ことによって、スペーサ全体が濾過膜で覆われるので、
スペーサの側面からの被処理液の侵入を防止できる。According to the above construction, the filtration membrane is formed larger than the spacer, is disposed so as to cover the spacer, and is directly adhered and fixed to the membrane support without the spacer at the peripheral portion of the filtration membrane. Because it is covered with a membrane
Intrusion of the liquid to be treated from the side surface of the spacer can be prevented.
【0011】[0011]
【実施例】以下、図面に基づき本発明の膜モジュールを
説明する。図1は、本発明の一実施例の膜モジュールの
要部断面図である。膜モジュール8において、9は矩形
平板状の膜支持体であり、膜支持体9の表面に膜透過液
流路を形成するフェルト状スペーサ10が周縁部12で接着
固定されるとともに、このスペーサ10を覆って濾過膜11
が配置されている。濾過膜11は、スペーサ10より大きく
形成されていて、膜11の周縁部13においてスペーサ10を
介することなく膜支持体9に接着固定されている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a membrane module according to the present invention will be described with reference to the drawings. FIG. 1 is a sectional view of a main part of a membrane module according to one embodiment of the present invention. In the membrane module 8, reference numeral 9 denotes a rectangular plate-like membrane support, and a felt-like spacer 10 forming a membrane permeate flow path is adhered and fixed to the surface of the membrane support 9 at a peripheral portion 12. Filter membrane 11
Is arranged. The filtration membrane 11 is formed larger than the spacer 10, and is fixed to the membrane support 9 at the periphery 13 of the membrane 11 without the spacer 10 interposed therebetween.
【0012】上記の構成により、スペーサ10は全体が濾
過膜11で覆われて被処理液に直接接触しなくなるため、
スペーサ10の側面からの被処理液の侵入が防止され、膜
モジュールによって好適に固液分離できる。With the above configuration, the spacer 10 is entirely covered with the filtration membrane 11 and does not directly contact the liquid to be treated.
Intrusion of the liquid to be treated from the side surface of the spacer 10 is prevented, and solid-liquid separation can be suitably performed by the membrane module.
【0013】この実施例においては濾過膜11とスペーサ
10の両方に接着剤を塗布して膜支持体9に接着固定した
が、膜11の周縁部13のみに接着剤を塗布して十分な接着
強度が得られる場合は、スペーサ10に接着剤を塗布しな
くてもよい。In this embodiment, a filter membrane 11 and a spacer
An adhesive is applied to both of the substrates 10 and fixed to the membrane support 9. However, when an adhesive is applied only to the peripheral portion 13 of the membrane 11 and sufficient adhesive strength can be obtained, the adhesive is applied to the spacer 10. It is not necessary to apply.
【0014】また、膜透過液流路の抵抗を減少させるた
めに、膜支持体9にシボをつけてもよい。The membrane support 9 may be textured to reduce the resistance of the membrane permeate flow path.
【0015】[0015]
【発明の効果】以上のように本発明によれば、スペーサ
より大きく形成した濾過膜でスペーサ全体を覆ったこと
によって、従来のようにスペーサの側面を閉塞させるほ
どの十分量の接着剤をスペーサに浸透させることなく、
スペーサの側面からの被処理液の侵入を回避でき、膜モ
ジュールによって好適に膜分離を行うことができる。As described above, according to the present invention, by covering the entire spacer with a filtration membrane formed larger than the spacer, a sufficient amount of adhesive enough to close the side surface of the spacer as in the prior art is provided. Without infiltrating
Intrusion of the liquid to be treated from the side surface of the spacer can be avoided, and membrane separation can be suitably performed by the membrane module.
【図1】本発明の一実施例の膜モジュールを説明する要
部断面図である。FIG. 1 is a cross-sectional view illustrating a main part of a membrane module according to an embodiment of the present invention.
【図2】本発明および従来例の膜モジュールが使用され
る膜分離ユニットの構成を示した説明図である。FIG. 2 is an explanatory diagram showing a configuration of a membrane separation unit using the present invention and a conventional membrane module.
【図3】従来例の膜モジュールを説明する要部断面図で
ある。FIG. 3 is a cross-sectional view illustrating a main part of a conventional membrane module.
8 膜モジュール 9 膜支持体 10 フェルト状スペーサ 11 濾過膜 13 周縁部 8 Membrane module 9 Membrane support 10 Felt-like spacer 11 Filtration membrane 13 Perimeter
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) B01D 63/08 B01D 63/00 510 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) B01D 63/08 B01D 63/00 510
Claims (1)
当な間隔で平行に配置し、下方に配置した曝気装置から
供給する空気によって生起する気液混合攪拌流で膜面を
洗浄する膜モジュールであって、膜支持体と濾過膜との
間に介装するフェルト状スペーサを周縁部で膜支持体に
接着し、スペーサの周縁部を覆って配置する濾過膜をス
ペーサより大きく形成した周縁部において膜支持体に接
着固定したことを特徴とする膜モジュール。(1) a casing provided inside a processing tank;
Arranged in parallel at appropriate intervals, from the aeration device located below
The membrane surface is stirred by a gas-liquid mixed stirring flow generated by the supplied air.
A membrane module for washing, comprising a membrane support and a filtration membrane.
Felt spacers interposed between the membrane support at the periphery
Glue and filter the filtration membrane placed over the periphery of the spacer.
Contact the membrane support at the periphery formed larger than the pacer
A membrane module that is fixedly attached.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5015779A JP2982842B2 (en) | 1993-02-03 | 1993-02-03 | Membrane module |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5015779A JP2982842B2 (en) | 1993-02-03 | 1993-02-03 | Membrane module |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH06226063A JPH06226063A (en) | 1994-08-16 |
JP2982842B2 true JP2982842B2 (en) | 1999-11-29 |
Family
ID=11898305
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5015779A Expired - Lifetime JP2982842B2 (en) | 1993-02-03 | 1993-02-03 | Membrane module |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2982842B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102011076238A1 (en) * | 2011-05-20 | 2012-11-22 | Siemens Ag | Arrangement and method for optical analysis and specific isolation of biological samples |
JP6215551B2 (en) * | 2013-03-27 | 2017-10-18 | 株式会社クボタ | Membrane cartridge |
-
1993
- 1993-02-03 JP JP5015779A patent/JP2982842B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH06226063A (en) | 1994-08-16 |
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