JPS621409A - Filter module made of hollow fiber - Google Patents

Filter module made of hollow fiber

Info

Publication number
JPS621409A
JPS621409A JP13803385A JP13803385A JPS621409A JP S621409 A JPS621409 A JP S621409A JP 13803385 A JP13803385 A JP 13803385A JP 13803385 A JP13803385 A JP 13803385A JP S621409 A JPS621409 A JP S621409A
Authority
JP
Japan
Prior art keywords
hollow fiber
cylindrical frame
filtration
frame
hollow fibers
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
JP13803385A
Other languages
Japanese (ja)
Inventor
Hiroshi Saito
浩 斉藤
Hiroshi Fukuhara
福原 博
Masahiro Furukawa
征弘 古川
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP13803385A priority Critical patent/JPS621409A/en
Publication of JPS621409A publication Critical patent/JPS621409A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a single module having a filter area increased by integer- fold compared with the existing filter element, which saves lots of time and labor for installation, replacement and maintenance by means of connecting and adjoining integrally plural unit filter elements. CONSTITUTION:The ends of hollow fiber 2 are connected with the packed bed 3 made of epoxy resin-originated adhesive inside the cylindrical frame 1 made of unit filter element formed with Noryl resin. For instance, plural fan-shaped 1b's having almost equivalent area of the frame 1a are adhered around the cylindrical frame 1a, encircling 1a to form an integral round shape altogether.

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は透過裏かうなる中空糸を集束した外圧式或は
内圧弐F通用の中空糸による濾過モジュールに関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a filtration module using hollow fibers that can be used for external pressure or internal pressure, in which permeable hollow fibers are bundled together.

(従来の技術) Pv人、ポリサルホン、ポリエーテルサルホン、ポリオ
レフィン、ポリプロピレノ、ポリエチレン等からなる中
空糸の一本は外径が約1.6鴎、内径が約1園であり、
長さが1rsの場合でp過面積はo.oos yと非常
に小さい。従って、大型濾過装置を構成する場合は、そ
の多数本を集束し、その各端部をノリル樹脂などで成形
した筒形枠中で相互に間隔を保ち、上記筒形枠中に充填
したエポキシ樹脂系の接7f剤の固化によ9上記箇形枠
と一体に結合したP過エレメントとし、装置の規模に応
じ所定数のP−Aエレメントを使用していろ。
(Prior art) One hollow fiber made of polysulfone, polyethersulfone, polyolefin, polypropylene, polyethylene, etc. has an outer diameter of about 1.6 mm and an inner diameter of about 1 mm,
When the length is 1rs, the p overarea is o. oos y and very small. Therefore, when configuring a large filtration device, a large number of them are bundled, each end of which is kept spaced apart from each other in a cylindrical frame made of noryl resin, etc., and the epoxy resin is filled into the cylindrical frame. By solidifying the contact 7f agent in the system, a P-passing element is integrally connected to the above-mentioned bullet frame, and a predetermined number of P-A elements are used depending on the scale of the device.

(発明が解決しよ5とする問題点) 従来の濾過エレメントはエポキシ樹脂系接着剤の硬化時
の発熱、中窒糸接N部の強度等の関係で内径80瓢の筒
形枠中(′C約aOO本の中空糸を結合してP−A面積
を42にするのが限度で、それ以上に内径が大きい筒形
枠中に同程度の冨度となる様によ9多数の中空糸を結合
すると接漕部の3度が弱くなると共に、長期間の運転に
よ・9経年疲労し、接漕面に破絣が庄じろ。
(Problems to be solved by the invention) Conventional filtration elements have a cylindrical frame with an inner diameter of 80 mm (' The limit is to combine approximately aOO hollow fibers to make the P-A area 42, and beyond that, 9 hollow fibers can be combined to have the same degree of richness in a cylindrical frame with a larger inner diameter. When combined, the 3 degrees of the row contacting part becomes weaker, and due to long-term operation, it becomes fatigued and cracks appear on the row contact surface.

従って、750r&/h程度の大型装置の場合には濾過
エレメントを500〜600本使用することになり、部
品点数が多く、メンテナンスにも時間を要する。
Therefore, in the case of a large-scale device of about 750 r&/h, 500 to 600 filtration elements are used, which requires a large number of parts and requires time for maintenance.

(問題点を解決するだめの手段) そこで本発明は複数の単位濾過エレメントを@接させて
一体に結合したことを特徴とする。
(Means for Solving the Problems) Therefore, the present invention is characterized in that a plurality of unit filtration elements are brought into contact with each other and are integrally combined.

(作 用) 隣接して結合した各単位濾過エレメントの面積が内径約
80鱈の円の面状に略々等しく、夫々約800木兄、長
さ1?PLの中空糸の端部を固定しであると、従来の濾
過エレメントの9部数倍の濾過面状を有する単一の濾過
モジュールが得られる。
(Function) The area of each unit filtration element connected adjacent to each other is approximately equal to the shape of a circle with an inner diameter of about 80 mm, and each unit has a diameter of about 800 mm and a length of 1 mm. If the ends of the PL hollow fibers are fixed, a single filtration module having a filtration surface shape nine times that of a conventional filtration element can be obtained.

(実施例) 図示の各実施例において、lはノリル樹脂で成形した各
電位濾過エレメントの筒形枠、コ・・・は上記枠内にエ
ポキシ樹脂系接着剤の充填層Jで端部を結合した中空糸
である。
(Example) In each of the illustrated examples, l is a cylindrical frame of each potential filtration element molded from Noryl resin, and c... is a cylindrical frame of each potential filtration element molded from Noryl resin, and the ends are joined within the frame with a filling layer J of epoxy resin adhesive. It is a hollow fiber.

第1図の第1冥施例は約800本の中空糸を固定した直
径約80mの円筒形の筒形枠/Lsの回りに、夫々直径
約80wxの円と面積がはy等しい同大の6つの扇形の
筒形枠/bを接層剤で結合して包囲し、全体として円形
にしたもので、各扇形筒形枠l&内にも充填ノー3で約
aOO固定の中空糸の端部が固定しである。この場合、
層形筒形枠/bの曲率半径は内周が約40m、外周が約
110閣である。この実施例では中空糸の長さが1隅で
あれば、濾過面積が従来の濾過エレメントの7倍の28
n?の濾過モジュールが得られる〇第4図の実施例は上
記第1図の実施例の層形筒形枠ihの回りに、夫々直径
約8C1a+の円と面状がはy等しい同大の6つの扇形
の筒形枠/Cを接層剤で結合して包囲し、全体として円
形にしたもので、この各筒形枠/c内にも充填層Jで約
800木兄の中空糸の4部が固定しである。
The first example in Fig. 1 is a cylindrical frame/Ls with a diameter of about 80 m to which about 800 hollow fibers are fixed, and a circle with a diameter of about 80 wx and a circle of the same size with an area equal to y. Six fan-shaped cylindrical frames /b are bonded and surrounded by a layering agent to form a circular shape as a whole, and each fan-shaped cylindrical frame l& has a filling no. 3 and the ends of hollow fibers are fixed at approximately aOO. is fixed. in this case,
The radius of curvature of the layered cylindrical frame/b is approximately 40 m on the inner circumference and approximately 110 m on the outer circumference. In this example, if the length of the hollow fiber is one corner, the filtration area is 28, which is 7 times that of the conventional filtration element.
n? In the embodiment shown in Fig. 4, six circles each having a diameter of about 8C1a+ and a surface shape of y are arranged around the layered cylindrical frame ih of the embodiment shown in Fig. 1. A fan-shaped cylindrical frame/C is bound and surrounded by a layering agent to form a circular shape as a whole, and within each cylindrical frame/c there are also 4 portions of hollow fibers of about 800 wood in the filling layer J. is fixed.

この場合、各筒形枠/Cの曲率半径は内周が約110 
mg 、外周が145mである。中空糸の長さが1風で
あれば、この実施例の濾過モジュールの濾過面積は従来
のFMエレメントの13倍の約52iKなる。
In this case, the radius of curvature of each cylindrical frame/C is approximately 110 mm on the inner circumference.
mg, and the outer circumference is 145 m. If the length of the hollow fiber is 1 wind, the filtration area of the filtration module of this embodiment is about 52 iK, which is 13 times that of the conventional FM element.

第5図の実施例は円’Y2i!射状に66分に分割した
扇形の筒形枠/dを6個、再び円形に接層剤で結合した
もので、各筒形、枠/dの面積は直・径約80mの円と
面積がはy等しく、夫々の内部には充填層3で約800
木兄の中空糸の端部が固定しである。各筒形枠の外周の
曲率半径は約100 ELである。中空糸の長さが1m
であれば、この実施例では従来の濾過エレメントの約6
倍−の2tr?の濾過面積を有する濾過モジュールとな
る。
The example in FIG. 5 is the circle 'Y2i! Six fan-shaped cylindrical frames/d divided into 66 segments in a radial pattern are joined together again into a circle with a layering agent, and the area of each cylinder and frame/d is a circle with a diameter of approximately 80 m. is equal to y, and there are about 800 filling layers 3 inside each
The end of the wooden hollow fiber is fixed. The radius of curvature of the outer periphery of each cylindrical frame is approximately 100 EL. The length of hollow fiber is 1m
If so, in this example, the conventional filtration element is about 6
Double 2tr? The filtration module has a filtration area of .

第6図の実施例は第5図の実施例のび過モジュールの回
りに、夫々直径約80mの円と面状かはy等しい同大の
6つの扇形の筒形枠/aを接−漕剤で結合して包囲し、
全体として円形にしたもので、この各筒形砕/−内にも
充填層3で約800木兄の中空糸の端部が固定しである
。各筒形枠/#の曲率半径は内周が約100m、外周が
約140鴎である。
In the embodiment shown in FIG. 6, six fan-shaped cylindrical frames /a each having a diameter of about 80 m and a plane shape or having the same size are attached around the extension module of the embodiment shown in FIG. 5. combine and surround,
The overall shape is circular, and the ends of the hollow fibers of approximately 800 mm are fixed in each cylindrical shape with a filling layer 3. The radius of curvature of each cylindrical frame/# is approximately 100 m on the inner circumference and approximately 140 m on the outer circumference.

この実施例では中空糸の長さが1惧とすると、従来の濾
過エレメントの約12倍の約48rr?の濾過モジュー
ルが得られろ◎ 又、この実施例では便宜上、筒形枠内に中空糸を800
本宛固定することで説明したが、本数−はこれに限られ
るものではないと共に、一体に結合した際の形状も円筒
状に限られるものではない。
In this example, if the length of the hollow fiber is 1 mm, it is about 48 rr, which is about 12 times that of the conventional filtration element. A filtration module of
Although the description has been made by fixing the books to each other, the number of books is not limited to this, and the shape when combined together is not limited to a cylindrical shape either.

又、筒形枠を用いてこれ同志を@!接して結合せず、中
空糸を固定した接、f酌同志を隣接して結合してもよい
Also, use a cylindrical frame to create this comrade @! Instead of being bonded in contact with each other, the hollow fibers with fixed hollow fibers may be bonded adjacently.

尚、原水を中空糸の外周から管壁に透過させて中窒内部
に処理水を得る外圧式F通の場合は第2図に示す様に中
空糸の一端を充填層3の端面に開口させ、他端は充填層
中に埋めて閉基する。
In addition, in the case of the external pressure type F passage in which raw water is passed through the tube wall from the outer periphery of the hollow fiber to obtain treated water inside the inner nitrogen, one end of the hollow fiber is opened at the end face of the packed bed 3 as shown in Fig. 2. , the other end is buried in a packed bed and closed.

又、原水を中正系の甲窒部に通し、内周から管壁に透過
させて中9糸の外に処理水を得る内圧式濾過の場合は第
3図の碌に中空糸の両端を充填層Jの端面に開口させる
In addition, in the case of internal pressure filtration, in which the raw water is passed through the upper part of the hollow fiber system and passed through the tube wall from the inner periphery to obtain the treated water outside the inner 9 threads, fill both ends of the hollow fibers as shown in Figure 3. An opening is made in the end face of layer J.

(発明の効果) 本発明による濾過モジュールの濾過面状は従来のPmエ
レメントの数倍〜10fi倍もあるため、従来−過エレ
メントな1fi100本使用していた大型装置に男いろ
と使用本数は激減し、その取付け、取替え、メンテナン
ス等に要する手数を省力し、且つ時間を著しく短縮する
ことができろ。
(Effect of the invention) Since the filtration surface shape of the filtration module according to the present invention is several times to 10 times that of the conventional Pm element, the number of 1fi elements used in large equipment, which used to be 100 1fi elements, is drastically reduced. However, it is possible to save labor and time required for installation, replacement, maintenance, etc., and to significantly shorten the time.

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

図面は本発明の実施例を示すもので、第1図は第1実施
例の平面図、第2図は同上の外圧式とした場合の一部を
断面にした側面図、第6図は同じく内圧式とした場合の
一部を断面にした側面図、第4図、第5図、第6図は夫
々他の実施例の平面図で、図中、/、lα、/b、/c
、 −/d、/−は筒形枠、コは中空糸、Jは接N剤の
充填ノーを示す。 q!f許出願出願人田工業株式会社 第1図
The drawings show embodiments of the present invention. Fig. 1 is a plan view of the first embodiment, Fig. 2 is a partially sectional side view of the same external pressure type as above, and Fig. 6 is the same. 4, 5, and 6 are plan views of other embodiments, respectively. In the figures, /, lα, /b, /c
, -/d, /- indicate the cylindrical frame, C indicates the hollow fiber, and J indicates the filling number of the N-contact agent. q! Figure 1

Claims (1)

【特許請求の範囲】[Claims] 多数本の中空糸の端部を相互に間隔を保ち接着剤により
固定した単位ろ過エレメントの複数を隣接して一体に結
合したことを特徴とする中空糸によるろ過モジュール。
A filtration module using hollow fibers, characterized in that a plurality of unit filtration elements, in which the ends of a large number of hollow fibers are kept spaced from each other and fixed with an adhesive, are joined together and adjacent to each other.
JP13803385A 1985-06-26 1985-06-26 Filter module made of hollow fiber Pending JPS621409A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13803385A JPS621409A (en) 1985-06-26 1985-06-26 Filter module made of hollow fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13803385A JPS621409A (en) 1985-06-26 1985-06-26 Filter module made of hollow fiber

Publications (1)

Publication Number Publication Date
JPS621409A true JPS621409A (en) 1987-01-07

Family

ID=15212471

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13803385A Pending JPS621409A (en) 1985-06-26 1985-06-26 Filter module made of hollow fiber

Country Status (1)

Country Link
JP (1) JPS621409A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0331067A2 (en) * 1988-03-02 1989-09-06 Akzo N.V. Mass and/or heat exchange apparatus
FR2629361A1 (en) * 1988-03-29 1989-10-06 Lyonnaise Eaux METHOD OF MANUFACTURING A TUBULAR PLATE FOR A HOLLOW FIBER SEPARATION APPARATUS, AND DEVICES OBTAINED
FR2820652A1 (en) * 2001-02-14 2002-08-16 Hoffmann La Roche HOLLOW FIBER MEMBRANE MODULES AND METHOD OF MAKING SAME
NL1021913C2 (en) * 2002-11-13 2004-05-14 Jb Ventures B V Filter module.
JP2007090309A (en) * 2005-09-30 2007-04-12 Kureha Corp Hollow fiber bundle, method for producing the same, tubular hollow fiber membrane module, and immersion type hollow fiber membrane module
JP2011075242A (en) * 2009-10-01 2011-04-14 Honda Motor Co Ltd Humidifying module
EP2794075A4 (en) * 2011-12-22 2015-11-25 Refine Technology Llc Hollow fiber cartridges and components and methods of their construction

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0331067A2 (en) * 1988-03-02 1989-09-06 Akzo N.V. Mass and/or heat exchange apparatus
EP0331067A3 (en) * 1988-03-02 1990-01-24 Akzo N.V. Mass and/or heat exchange apparatus
FR2629361A1 (en) * 1988-03-29 1989-10-06 Lyonnaise Eaux METHOD OF MANUFACTURING A TUBULAR PLATE FOR A HOLLOW FIBER SEPARATION APPARATUS, AND DEVICES OBTAINED
FR2820652A1 (en) * 2001-02-14 2002-08-16 Hoffmann La Roche HOLLOW FIBER MEMBRANE MODULES AND METHOD OF MAKING SAME
NL1019960C2 (en) * 2001-02-14 2005-04-08 Hoffmann La Roche Special hollow fiber membrane module for use in processes strongly influenced by fouling and its manufacture.
US7128837B2 (en) 2001-02-14 2006-10-31 Hoffmann-La Roche Inc. Hollow fiber membrane module
NL1021913C2 (en) * 2002-11-13 2004-05-14 Jb Ventures B V Filter module.
WO2004043578A1 (en) * 2002-11-13 2004-05-27 Jb Ventures B.V. Filter module
JP2007090309A (en) * 2005-09-30 2007-04-12 Kureha Corp Hollow fiber bundle, method for producing the same, tubular hollow fiber membrane module, and immersion type hollow fiber membrane module
JP2011075242A (en) * 2009-10-01 2011-04-14 Honda Motor Co Ltd Humidifying module
EP2794075A4 (en) * 2011-12-22 2015-11-25 Refine Technology Llc Hollow fiber cartridges and components and methods of their construction
US10213745B2 (en) 2011-12-22 2019-02-26 Refine Technology, Llc Hollow fiber cartridges and components and methods of their construction

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