JPH0732866B2 - Filtration membrane module - Google Patents
Filtration membrane moduleInfo
- Publication number
- JPH0732866B2 JPH0732866B2 JP4071791A JP7179192A JPH0732866B2 JP H0732866 B2 JPH0732866 B2 JP H0732866B2 JP 4071791 A JP4071791 A JP 4071791A JP 7179192 A JP7179192 A JP 7179192A JP H0732866 B2 JPH0732866 B2 JP H0732866B2
- Authority
- JP
- Japan
- Prior art keywords
- filtration membrane
- plate
- resin layer
- membrane module
- filtered
- 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、濾過膜モジュールに関
し、一端が閉鎖され且つ他端が開口するチューブ状濾過
膜の開口を、板状体にて周壁の一部が構成された濾過液
収集室内へ臨ませるべく、前記チューブ状濾過膜の開口
側先端部を前記板状体に設けた貫通孔に貫通させると共
に、前記チューブ状濾過膜を前記板状体に対してシール
状態で接着固定する樹脂層を設けてある濾過膜モジュー
ルに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filtration membrane module, and a filtration liquid collection in which an opening of a tubular filtration membrane having one end closed and the other end opened is constituted by a plate-like member to constitute a part of a peripheral wall. In order to face the inside of the room, the distal end of the tubular filtration membrane on the opening side is penetrated into the through hole provided in the plate-shaped body, and the tube-shaped filtration membrane is sealed to the plate-shaped body.
The present invention relates to a filtration membrane module provided with a resin layer that is adhesively fixed in a state .
【0002】[0002]
【従来の技術】従来の濾過膜モジュールは、一般に、図
3に示すような構造となっている。即ち、濾過膜モジュ
ールの枠体1の中間の適宜部分には、隔壁状の板状体1
aが形成されており、その板状体1aの両側には濾過液
収集室5及び被濾過液通流空間6が形成されている。前
記被濾過液通流空間6は、そこを被濾過液が通過できる
ように双方向に(例えば、上下方向に)開いており、そ
の被濾過液通流空間6には、一端が閉鎖されたチューブ
状濾過膜3の複数本が並設されている。そして、前記チ
ューブ状濾過膜3の他端部は、前記板状体1aに設けた
貫通孔を貫通し、その他端に開いた開口3aが前記濾過
液収集室5に臨むように取り付けられている。更に、前
記チューブ状濾過膜3を前記板状体1aに対してシール
状態で接着固定する樹脂層4(例えば、シール用樹脂と
しても固定用樹脂としても機能するシリコーン等の軟質
樹脂層)が、前記板状体1aにおける前記濾過液収集室
5側とは反対側の面(即ち、前記被濾過液通流空間6側
の面)に設けられている。かかる濾過膜モジュールを用
いて被濾過液の濾過を行う場合は、前記被濾過液通流空
間6において、前記チューブ状濾過膜3の周囲に被濾過
液を透過圧力をかけつつ通流させ、その一部を濾過膜通
過させることによって被濾過液の濾過が行われる。かか
る濾過過程においては、前記チューブ状濾過膜3の前記
板状体1aに対する貫通部分に、前記被濾過液通流空間
6側から前記濾過液収集室5側へ前記透過圧力に基づく
圧力がかかるようになる。従って、前記樹脂層4が上述
の如く前記濾過液収集室5側とは反対側の面に設けられ
ていると、前記圧力は前記樹脂層4において圧縮応力と
して作用するようになるため、前記樹脂層4での亀裂の
発生が抑えられて前記樹脂層4を経由する被濾過液のリ
ーク(被濾過液の濾過液収集室5へのリーク)が抑えら
れるようになる、と従来は考えられていた。そこで、従
来の濾過膜モジュールにおいては、前記板状体1aにお
ける前記濾過液収集室5側とは反対側の面に前記樹脂層
4を設けることとしていた。2. Description of the Related Art A conventional filtration membrane module generally has a structure as shown in FIG. That is, the partition plate-shaped plate 1 is provided at an appropriate portion in the middle of the frame 1 of the filtration membrane module.
a is formed, and a filtrate collection chamber 5 and a filtered liquid flow space 6 are formed on both sides of the plate 1a. The filtered liquid flow-through space 6 is open bidirectionally (for example, in the vertical direction) so that the filtered liquid can pass therethrough, and the filtered liquid flow-through space 6 has one end closed. A plurality of tubular filtration membranes 3 are arranged in parallel. The other end of the tubular filtration membrane 3 penetrates a through hole provided in the plate-shaped body 1a, and an opening 3a opened at the other end is attached to the filtrate collection chamber 5. . Furthermore, the tubular filtration membrane 3 is sealed to the plate-shaped body 1a.
A resin layer 4 (for example, a soft resin layer such as silicone that functions both as a sealing resin and a fixing resin) adhered and fixed in this state is provided on the side opposite to the filtrate collection chamber 5 side of the plate 1a. It is provided on the surface (that is, the surface on the side of the filtered liquid flow-through space 6 side). When the liquid to be filtered is filtered using such a filtration membrane module, the liquid to be filtered is caused to flow around the tubular filtration membrane 3 in the liquid flow passage space 6 while applying a permeation pressure, The liquid to be filtered is filtered by passing a part through the filtration membrane. In the filtration process, a pressure based on the permeation pressure is applied to the filtered liquid flow-through space 6 side to the filtered liquid collection chamber 5 side at the portion of the tubular filtration membrane 3 that penetrates the plate-shaped body 1a. become. Therefore, when the resin layer 4 is provided on the surface opposite to the filtrate collection chamber 5 side as described above, the pressure acts on the resin layer 4 as a compressive stress, so that the resin It has been conventionally considered that the generation of cracks in the layer 4 is suppressed and the leakage of the liquid to be filtered (leakage of the liquid to be filtered into the filtrate liquid collecting chamber 5) via the resin layer 4 is suppressed. It was Therefore, in the conventional filtration membrane module, the resin layer 4 is provided on the surface of the plate-shaped body 1a opposite to the filtration liquid collection chamber 5 side.
【0003】[0003]
【発明が解決しようとする課題】然るに、上述した従来
の濾過膜モジュールを実際に使用した場合、前記樹脂層
4の亀裂Kは、図4に示す如く、前記濾過過程において
よりも次に述べる過程において発生し易い、ということ
を知見した。即ち、前記チューブ状濾過膜3の目詰まり
等をなくすために前記透過圧力とは反対方向に圧力をか
けて前記チューブ状濾過膜3の洗浄(以下、その洗浄を
逆洗(逆圧洗浄)といい、そのときにかける圧力を逆洗
圧力という)を行う過程において発生し易い、というこ
とを知見した。本発明は、かかる知見に基づいてなされ
たものであり、上述した如き樹脂層の亀裂の発生を抑え
て、被濾過液の濾過液収集室へのリークを抑える手段を
提供することを目的としている。However, when the above-mentioned conventional filtration membrane module is actually used, the crack K of the resin layer 4 is, as shown in FIG. 4, a process described below rather than in the filtration process. It was found that it is easy to occur in. That is, in order to eliminate clogging and the like of the tubular filtration membrane 3, pressure is applied in a direction opposite to the permeation pressure to wash the tubular filtration membrane 3 (hereinafter, the washing is called backwashing (backpressure washing)). It was found that the pressure applied at that time is easily generated in the process of performing the backwash pressure. The present invention has been made based on such findings, and an object of the present invention is to provide a means for suppressing the occurrence of cracks in the resin layer as described above and suppressing the leakage of the liquid to be filtered into the filtrate collection chamber. .
【0004】[0004]
【課題を解決するための手段】本発明に係る濾過膜モジ
ュールは、チューブ状濾過膜を板状体に対してシール状
態で接着固定する樹脂層を、前記板状体における濾過液
収集室側の面に設けてある点に特徴を有している。A filtration membrane module according to the present invention comprises a tubular filtration membrane sealed to a plate.
The present invention is characterized in that the resin layer that is adhesively fixed in the state is provided on the surface of the plate-shaped body on the side of the filtrate collection chamber.
【0005】[0005]
【作用】かかる濾過膜モジュールによれば、前記樹脂層
が、前記板状体における濾過液収集室側の面に設けられ
ているため、前記チューブ状濾過膜の目詰まり等を解消
すべく逆洗を実行したとしても、そのときにかかる逆洗
圧力は前記樹脂層において圧縮応力として作用するよう
になる。従って、逆洗過程における前記樹脂層での亀裂
の発生が抑えられるようになる。尚、前記濾過膜モジュ
ールを用いて、透過圧力をかけつつ被濾過液の濾過を実
行する濾過過程においては、透過圧力が前記樹脂層にお
いて引張応力として作用するようになって亀裂の発生す
る可能性があるが、その亀裂の発生を抑えるのは容易で
ある。なぜなら、一般に透過圧力は逆洗圧力に比して小
さい傾向にあり、逆洗圧力による引張応力に耐えるよう
に前記樹脂層を設計するのに比べ、透過圧力による引張
応力に耐えるように前記樹脂層を設計する方が容易であ
るからである。According to this filtration membrane module, since the resin layer is provided on the surface of the plate-shaped body on the side of the filtrate collection chamber, backwashing is performed to eliminate clogging of the tubular filtration membrane. Even if is performed, the backwash pressure applied at that time acts as a compressive stress in the resin layer. Therefore, the occurrence of cracks in the resin layer during the backwash process can be suppressed. In the filtration process of performing filtration of the liquid to be filtered while applying the permeation pressure using the filtration membrane module, the permeation pressure may act as a tensile stress in the resin layer, which may cause a crack. However, it is easy to suppress the occurrence of cracks. Because, in general, the permeation pressure tends to be smaller than the backwash pressure, and compared with designing the resin layer to withstand the tensile stress due to the backwash pressure, the resin layer so as to withstand the tensile stress due to the permeate pressure. Is easier to design.
【0006】[0006]
【発明の効果】本発明の濾過膜モジュールを用いる場合
は、実際には濾過過程においてよりも発生し易い、逆洗
過程において前記樹脂層に亀裂が発生するのを上述の如
く抑えることができる。従って、被濾過液の濾過液収集
室へのリークを実質的に抑えることができるようにな
り、もって、従来の問題が解消されるようになる。As described above, when the filtration membrane module of the present invention is used, it is possible to suppress the occurrence of cracks in the resin layer in the backwashing process, which is actually easier than in the filtration process, as described above. Therefore, it becomes possible to substantially suppress the leakage of the liquid to be filtered into the filtrate collection chamber, and thus the conventional problems can be solved.
【0007】[0007]
【実施例】以下、本発明の実施例を図面に基づいて説明
する。図1には、本発明の濾過膜モジュールの一実施例
が示されており、図2には、その濾過膜モジュールを備
えた濾過装置が示されている。尚、図面において従来例
と同一の符号で表示した部分は同一又は相当の部分を示
している。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 shows an embodiment of the filtration membrane module of the present invention, and FIG. 2 shows a filtration device equipped with the filtration membrane module. In the drawings, the portions denoted by the same reference numerals as the conventional example indicate the same or corresponding portions.
【0008】図1において、1は、前記濾過膜モジュー
ルの枠体であり、その枠体1は、硬質樹脂(例えば、ポ
リ塩化ビニリデン)を素材とし、大半部分が上下に開放
した方形枠状に成形されている。その枠体1の中間の適
宜部分には、隔壁状の板状体1aが形成されている。そ
の板状体1aの両側には濾過液収集室5及び被濾過液通
流空間6が形成されている。In FIG. 1, reference numeral 1 is a frame body of the filtration membrane module, and the frame body 1 is made of a hard resin (for example, polyvinylidene chloride), and has a rectangular frame shape in which most of the frame body is opened vertically. It is molded. A partition-shaped plate-shaped body 1a is formed at an appropriate portion in the middle of the frame body 1. A filtrate collection chamber 5 and a filtered liquid flow space 6 are formed on both sides of the plate 1a.
【0009】前記濾過液収集室5は、濾過液取出部7を
除いて外に閉ざされた密閉空間とされている。一方、前
記被濾過液通流空間6は、そこを被濾過液が通過できる
ように上下方向に開いており、その被濾過液通流空間6
には、チューブ状濾過膜3の複数本が前記枠体1の長手
方向に延在するように並設されている。前記複数本のチ
ューブ状濾過膜3の各一端は、それらを前記枠体1にお
ける前記濾過液取出部7とは反対側の壁体1b内に夫々
埋め込むことにより(或いは、図示しないが、前記壁体
1bに夫々接当させた上でその接当状態を固着すること
により)閉鎖されている。前記複数本のチューブ状濾過
膜3の各他端には、夫々、開口3aが形成されている
が、その各開口3aを、前記板状体1aにて周壁の一部
が構成された前記濾過液収集室5内へ臨ませるべく、各
チューブ状濾過膜3の開口側先端部は、前記板状体1a
に設けた貫通孔に貫通されている。その貫通状態は、前
記板状体1aにおける濾過液収集室5側の面に層状に設
けられることによって前記チューブ状濾過膜3にも前記
板状体1aにも界面が接着するようになる樹脂層4の存
在に基づいてシール状態で固定維持されるようになる。
尚、前記樹脂層4としては、例えば、シール用樹脂とし
ても固定用樹脂としても有効に機能するシリコーン等の
軟質樹脂層が用いられる。The filtrate collection chamber 5 is a closed space which is closed outside except for the filtrate extraction section 7. On the other hand, the filtered liquid flow-through space 6 is opened vertically so that the filtered liquid can pass therethrough.
A plurality of tubular filtration membranes 3 are arranged side by side so as to extend in the longitudinal direction of the frame 1. Each of the ends of the plurality of tubular filtration membranes 3 is embedded in the wall 1b of the frame 1 on the side opposite to the filtrate extraction portion 7 (or, although not shown, the wall They are closed by abutting each body 1b and then fixing their abutment. An opening 3a is formed at each of the other ends of the plurality of tubular filtration membranes 3, and each of the openings 3a is formed by the plate-shaped body 1a to form a part of a peripheral wall. In order to face the inside of the liquid collection chamber 5, the tip end on the opening side of each tubular filtration membrane 3 has the plate-shaped body 1a.
Is penetrated through a through hole provided in the. The penetration state is a resin layer in which the interface is adhered to both the tubular filtration membrane 3 and the plate 1a by being provided in layers on the surface of the plate 1a on the side of the filtrate collection chamber 5 side. Due to the presence of No. 4, it becomes fixed and maintained in a sealed state .
As the resin layer 4, for example, a soft resin layer such as silicone that effectively functions as a sealing resin and a fixing resin is used.
【0010】そして、前記濾過膜モジュールを、図2に
示す如く、被濾過液が貯留された処理槽8内の適宜位置
に浸漬すると共に、前記濾過膜モジュールの濾過液取出
部7を前記処理槽8の外部まで引き出し配管し、更にそ
の引き出し配管部分に、前記濾過液収集室5内の濾過液
を吸引するポンプ9、及び、空気を濾過液とは逆向きに
流して逆洗圧力をかける逆洗手段10を設けることによ
り、逆洗を適宜実行しながら被濾過液の濾過を行うこと
ができる濾過装置が構成されている。Then, as shown in FIG. 2, the filtration membrane module is immersed in an appropriate position in the treatment tank 8 in which the liquid to be filtered is stored, and the filtrate extraction portion 7 of the filtration membrane module is placed in the treatment tank. 8 to the outside of 8, and a pump 9 for sucking the filtered liquid in the filtered liquid collecting chamber 5 and an air flow in the direction opposite to the filtered liquid to apply a backwash pressure to the drawing pipe portion. By providing the washing means 10, a filtration device capable of filtering the liquid to be filtered while appropriately performing backwashing is configured.
【0011】かかる濾過装置に装備された濾過膜モジュ
ールによれば、前記樹脂層4が、前記板状体1aにおけ
る濾過液収集室5側の面に設けられているため、前記チ
ューブ状濾過膜3の目詰まり等を解消すべく逆洗を実行
するときに、逆洗圧力が前記樹脂層4において圧縮応力
として作用するようになる。従って、逆洗過程における
前記樹脂層4での亀裂の発生が抑えられるようになる。According to the filtration membrane module equipped in such a filtration device, since the resin layer 4 is provided on the surface of the plate-shaped body 1a on the filtrate collection chamber 5 side, the tubular filtration membrane 3 is provided. When backwashing is performed to eliminate the clogging of the resin layer 4, the backwashing pressure acts as a compressive stress in the resin layer 4. Therefore, the occurrence of cracks in the resin layer 4 during the backwash process can be suppressed.
【0012】次に、別実施例について説明する。前記複
数本のチューブ状濾過膜3の各一端をフリーな状態にし
つつも閉鎖し、各チューブ状濾過膜3の保持を、その各
他端側のみにて行うように構成した実施例も考えられ
る。Next, another embodiment will be described. An embodiment is also conceivable in which one end of each of the plurality of tubular filtration membranes 3 is closed while being freed, and each tubular filtration membrane 3 is held only on the other end side thereof. .
【0013】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.
【図1】本発明に係る濾過膜モジュールを示す水平断面
図FIG. 1 is a horizontal sectional view showing a filtration membrane module according to the present invention.
【図2】そのモジュールを備える濾過装置を示す縦断面
図FIG. 2 is a vertical cross-sectional view showing a filtration device including the module.
【図3】従来の濾過膜モジュールを示す水平断面図FIG. 3 is a horizontal sectional view showing a conventional filtration membrane module.
1a 板状体 3 チューブ状濾過膜 3a 開口 4 樹脂層 5 濾過液収集室 1a Plate-like body 3 Tubular filtration membrane 3a Opening 4 Resin layer 5 Filtrate collection chamber
Claims (1)
ブ状濾過膜(3)の開口(3a)を、板状体(1a)に
て周壁の一部が構成された濾過液収集室(5)内へ臨ま
せるべく、前記チューブ状濾過膜(3)の開口側先端部
を前記板状体(1a)に設けた貫通孔に貫通させると共
に、前記チューブ状濾過膜(3)を前記板状体(1a)
に対してシール状態で接着固定する樹脂層(4)を設け
てある濾過膜モジュールであって、前記樹脂層(4)を
前記板状体(1a)における前記濾過液収集室(5)側
の面に設けてある濾過膜モジュール。1. A filtrate collection chamber in which an opening (3a) of a tubular filtration membrane (3), one end of which is closed and the other end of which is open, has a peripheral wall partially formed by a plate-like body (1a). 5) in order to face into the plate with pass through, the tubular filtration membrane (3) the opening-side front end portion of the tubular filtration membrane (3) into a through hole provided in the plate-shaped body (1a) Shape (1a)
Provide a resin layer (4) that adheres and fixes in a sealed state to
A filtration membrane module with Te, filtration membrane module is provided wherein the resin layer (4) on the surface of the filtrate collection chamber (5) side of the plate-like body (1a).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4071791A JPH0732866B2 (en) | 1992-03-30 | 1992-03-30 | Filtration membrane module |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4071791A JPH0732866B2 (en) | 1992-03-30 | 1992-03-30 | Filtration membrane module |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05269356A JPH05269356A (en) | 1993-10-19 |
| JPH0732866B2 true JPH0732866B2 (en) | 1995-04-12 |
Family
ID=13470753
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4071791A Expired - Lifetime JPH0732866B2 (en) | 1992-03-30 | 1992-03-30 | Filtration membrane module |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0732866B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8523549D0 (en) * | 1985-09-24 | 1985-10-30 | Atomic Energy Authority Uk | Liquid treatment apparatus |
-
1992
- 1992-03-30 JP JP4071791A patent/JPH0732866B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05269356A (en) | 1993-10-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3341428B2 (en) | Operating method of immersion membrane device | |
| JP2763262B2 (en) | Backwashing method of ceramic membrane | |
| JP5441887B2 (en) | Membrane element and membrane module | |
| US20040238442A1 (en) | High solids module | |
| JP2003135935A (en) | Method for producing hollow fiber membrane module | |
| JP2000051669A (en) | Hollow fiber membrane module with lower cap | |
| JP3815645B2 (en) | Immersion type flat membrane separator and control method thereof | |
| JP5611032B2 (en) | Immersion membrane separator | |
| JPH0732866B2 (en) | Filtration membrane module | |
| JPH10230145A (en) | Spiral type membrane element | |
| JP3538902B2 (en) | Membrane element of immersion type membrane separation device | |
| JP2004041935A (en) | Cleaning method for membrane filtration equipment | |
| CN102292145B (en) | Membrane separation device | |
| JPH05269357A (en) | Filtration membrane module | |
| JP3929194B2 (en) | Hollow fiber membrane unit and membrane separator | |
| JPH07132214A (en) | Membrane element | |
| JPH10230140A (en) | Spiral type membrane element | |
| JPH05269358A (en) | Filtration membrane module | |
| JP3349649B2 (en) | Membrane filtration device | |
| JP3293215B2 (en) | Membrane separation device and operation method thereof | |
| JP4384740B2 (en) | Hollow fiber membrane module unit | |
| JPH08155278A (en) | Membrane element manufacturing method | |
| JP2000271461A (en) | Spiral type membrane element and operation method of spiral type membrane module | |
| JPH07100339A (en) | Submerged flat membrane element | |
| JPH0725212Y2 (en) | Immersion type membrane module |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080412 Year of fee payment: 13 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090412 Year of fee payment: 14 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100412 Year of fee payment: 15 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100412 Year of fee payment: 15 |
|
| FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110412 Year of fee payment: 16 |
|
| EXPY | Cancellation because of completion of term |