JPS61222510A - Hollow yarn membrane module and its preparation - Google Patents
Hollow yarn membrane module and its preparationInfo
- Publication number
- JPS61222510A JPS61222510A JP60065518A JP6551885A JPS61222510A JP S61222510 A JPS61222510 A JP S61222510A JP 60065518 A JP60065518 A JP 60065518A JP 6551885 A JP6551885 A JP 6551885A JP S61222510 A JPS61222510 A JP S61222510A
- Authority
- JP
- Japan
- Prior art keywords
- outer cylinder
- resin
- hollow fiber
- cap
- membrane bundle
- 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
- 239000012528 membrane Substances 0.000 title claims abstract description 52
- 229920005989 resin Polymers 0.000 claims abstract description 47
- 239000011347 resin Substances 0.000 claims abstract description 47
- 238000000034 method Methods 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 5
- 239000012510 hollow fiber Substances 0.000 claims description 36
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000012466 permeate Substances 0.000 claims description 3
- 238000001816 cooling Methods 0.000 abstract description 3
- 230000001954 sterilising effect Effects 0.000 abstract description 3
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 abstract description 2
- 238000001746 injection moulding Methods 0.000 abstract 1
- 238000005266 casting Methods 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 229920003002 synthetic resin Polymers 0.000 description 5
- 239000000057 synthetic resin Substances 0.000 description 5
- 239000000853 adhesive Substances 0.000 description 4
- 230000001070 adhesive effect Effects 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- 239000003822 epoxy resin Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 229920000647 polyepoxide Polymers 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 241001122767 Theaceae Species 0.000 description 1
- 238000004026 adhesive bonding Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000010125 resin casting Methods 0.000 description 1
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
- B01D63/021—Manufacturing thereof
- B01D63/022—Encapsulating hollow fibres
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
この発明は中空糸膜モジュール及びその製造方法に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a hollow fiber membrane module and a manufacturing method thereof.
〈従来の技術〉
従来の中空糸膜モジュールは、中空糸膜束を外向内に挿
入し、この外筒の両端部において、注型用合成樹脂によ
り、該中空糸膜束を接着固定して製造している。<Conventional technology> Conventional hollow fiber membrane modules are manufactured by inserting a hollow fiber membrane bundle outward and fixing the hollow fiber membrane bundle at both ends of the outer cylinder using synthetic resin for casting. are doing.
上記の注型用合成樹脂にはエポキシ樹脂系あるいはウレ
タン系等が用いられ、樹脂と外筒との接着結合は、外筒
内面に溝や凹凸を設け、樹脂との接着面積を大きくする
方法が一般的である。Epoxy resins or urethane resins are used as the above synthetic resins for casting, and adhesive bonding between the resin and the outer cylinder can be achieved by providing grooves or unevenness on the inner surface of the outer cylinder to increase the bonding area with the resin. Common.
〈発明が解決しようとする問題点〉
上記のような従来の方法では、樹脂の硬化時の収縮率が
大きいと、樹脂が外筒から剥離する場合があり、又収縮
率が小さいものでも90℃以上の高温で中空糸膜モジュ
ールを煮沸殺菌したり、120℃以上で蒸気滅菌した場
合、冷却過程において、外筒と樹脂の収縮率の違いによ
り外筒と樹脂の剥離が生じることが多いという問題があ
った。<Problems to be Solved by the Invention> In the conventional method as described above, if the shrinkage rate of the resin during curing is large, the resin may peel off from the outer cylinder, and even if the shrinkage rate is small, the temperature may exceed 90°C. When hollow fiber membrane modules are sterilized by boiling at higher temperatures or steam sterilized at temperatures higher than 120°C, the problem is that the outer cylinder and resin often separate from each other during the cooling process due to the difference in shrinkage rate between the outer cylinder and the resin. was there.
〈問題点を解決するための手段〉
この発明は上記のような従来の中空糸膜モジュールの問
題点を解決するためになされたもので、両端を開放し、
透過液出口を設けた外筒の両端付近に複数の貫通孔を設
け、外筒内に挿入した中空糸膜束を該貫通孔を介して外
筒内に注入硬化させた樹脂により、外筒に固定するとと
もに、この樹脂により外筒の両端部外側も被覆した中空
糸膜モジュール及びその製造方法を提供する。<Means for solving the problems> This invention was made to solve the problems of the conventional hollow fiber membrane module as described above.
A plurality of through holes are provided near both ends of the outer cylinder provided with a permeate outlet, and the hollow fiber membrane bundle inserted into the outer cylinder is injected into the outer cylinder through the through holes and hardened resin is applied to the outer cylinder. The present invention provides a hollow fiber membrane module in which both ends of the outer cylinder are fixed and the outside of both ends of the outer cylinder are also covered with the resin, and a method for manufacturing the same.
〈実施例〉
第2図の1は円筒状の外筒でその両端は開放されており
、又両端には複数の貫通孔2が設けてあり、かつ透過液
出口3が設けである。<Embodiment> Reference numeral 1 in FIG. 2 is a cylindrical outer tube, both ends of which are open, and both ends are provided with a plurality of through holes 2 and a permeated liquid outlet 3.
4は中空糸膜束で、公知の中空糸膜の両端をヒートシー
ル等により閉鎖して注型用樹脂が入らぬようにしたもの
の複数を束にしたものである。Reference numeral 4 denotes a hollow fiber membrane bundle, which is a bundle of a plurality of known hollow fiber membranes, both ends of which are closed by heat sealing or the like to prevent the casting resin from entering.
この糸膜束4を外筒1内に挿入するが、糸膜束4と外筒
1間には適当な隙間を設け、糸膜束4の両端を外筒1の
両端より突出させる。This thread membrane bundle 4 is inserted into the outer tube 1, with an appropriate gap provided between the thread membrane bundle 4 and the outer tube 1, so that both ends of the yarn membrane bundle 4 protrude from both ends of the outer tube 1.
次に第3図のように、外筒1を垂直にして、その下端部
に上向きのキャップ5を被せる。Next, as shown in FIG. 3, the outer cylinder 1 is made vertical, and the cap 5 facing upward is placed on the lower end thereof.
このキャップ5の内周には段部6が設けであるから、外
筒1の端部は段部6上に載り、外筒1がら突出した中空
糸膜束4の端部はキャップ5の底面に達する。又キャッ
プ5の周壁は外筒1の貫通孔2を形成した部分を完全に
被うようにする。Since a step 6 is provided on the inner periphery of the cap 5, the end of the outer tube 1 rests on the step 6, and the end of the hollow fiber membrane bundle 4 protruding from the outer tube 1 is placed on the bottom surface of the cap 5. reach. Further, the peripheral wall of the cap 5 is made to completely cover the portion of the outer cylinder 1 in which the through hole 2 is formed.
上記のようにキャップ5を外筒1の下端部に被せたのち
、ポリエチレン容器7に入れた液状の注型用合成樹脂8
をポリエチレンチューブ9を介してキャップ5内に注入
すると、該樹脂8はキャップ5内にある外筒1の各貫通
孔2から外筒1内に流入して外筒1と中空糸膜束4間の
隙間や、中空糸膜束4を構成する各糸膜間に充填され、
かっ外筒1の外側とキャップ5の内面間も充填される。After the cap 5 is placed on the lower end of the outer cylinder 1 as described above, the liquid synthetic resin for casting 8 is placed in the polyethylene container 7.
When the resin 8 is injected into the cap 5 through the polyethylene tube 9, the resin 8 flows into the outer cylinder 1 from each through hole 2 of the outer cylinder 1 in the cap 5 and flows between the outer cylinder 1 and the hollow fiber membrane bundle 4. It is filled in the gaps between the hollow fiber membrane bundles 4 and between the fiber membranes constituting the hollow fiber membrane bundle 4.
The space between the outside of the barrel 1 and the inside of the cap 5 is also filled.
その後一定時間静置して樹脂8を完全に硬化させたのち
、キャップ5を取外し、第3図の鎖線へ−A線に沿って
外筒1から突出している中空糸膜束4の端部を樹脂8と
ともに切断すると、各中空糸膜4を構成する各糸膜の閉
鎖された端部も開放される。After that, the resin 8 is left to stand for a certain period of time to completely harden, and then the cap 5 is removed and the end of the hollow fiber membrane bundle 4 protruding from the outer cylinder 1 is inserted along the chain line-A line in FIG. When the resin 8 is cut together, the closed ends of each fiber membrane constituting each hollow fiber membrane 4 are also opened.
上記の工程ののち、今度は第3図で上になっている側を
下にして同一の工作を施す。After the above steps, the same process is performed this time with the side facing up in Figure 3 facing down.
尚注型硬化後A−A線に沿って切断する作業は両端に対
する注型樹脂の硬化が終ったのち行ってもよい。Note that the operation of cutting along the line A-A after the casting mold is cured may be performed after the casting resin has finished curing at both ends.
上記のような製造方法により得られた中空糸膜モジュー
ルが第1図に示しであるが、この図で明らかなように、
注型した樹脂8は貫通孔2を介して外筒1の内外に固く
結合し、外筒1と糸膜束4も固く結合している。The hollow fiber membrane module obtained by the above manufacturing method is shown in FIG. 1, and as is clear from this figure,
The cast resin 8 is firmly connected to the inside and outside of the outer cylinder 1 through the through hole 2, and the outer cylinder 1 and the thread membrane bundle 4 are also firmly connected.
上記の実施例に用いた外筒1は外形114m、肉厚4.
5rII!nのポリカーボネート製であり、貫通孔2は
直径4711111で、貫通孔2の数は、貫通孔2の総
面積が注型合成樹脂8の接着面積に対して約40%にな
るようにした。The outer cylinder 1 used in the above example has an outer diameter of 114 m and a wall thickness of 4.0 m.
5rII! The through holes 2 have a diameter of 4711111, and the number of through holes 2 is such that the total area of the through holes 2 is about 40% of the adhesive area of the cast synthetic resin 8.
キャップ5は段部6より上部の内径が125am、下部
の内径が105altであり、注型用合成樹脂8として
エポキシ系樹脂を用いた。 又、両端をA−A線から切
断除去したのち、完成した中空糸膜モジュールを100
℃で4時間アフターキュアを行なった。The cap 5 had an inner diameter of 125 am above the stepped portion 6 and an inner diameter of 105 alt below the stepped portion 6, and an epoxy resin was used as the synthetic resin 8 for casting. Also, after cutting and removing both ends from the A-A line, the completed hollow fiber membrane module was
After-cure was performed at ℃ for 4 hours.
上記実施例を中空糸膜モジユール内に約120℃の水蒸
気を1時間通したのち、直ちに25℃の水に切替え、1
時間通水した。その後、透過水出口の片方を盲にし、も
う一つの透過水出口3から2Kfl/CIiの空気圧を
かけた状態で水中に浸漬して外筒1と注型樹脂8間から
の空気洩れを観察したが空気洩れは全く認められなかっ
た。In the above example, water vapor at about 120°C was passed through the hollow fiber membrane module for 1 hour, and then immediately switched to water at 25°C.
The water ran for an hour. Thereafter, one of the permeated water outlets was blinded, and the other permeated water outlet 3 was immersed in water with an air pressure of 2 Kfl/CIi applied to observe air leakage from between the outer cylinder 1 and the casting resin 8. However, no air leakage was observed.
従って外筒1と注型樹脂8の剥離は生じていないことが
確認できる。Therefore, it can be confirmed that no peeling occurs between the outer cylinder 1 and the casting resin 8.
又、比較例として前記実施例と同じ寸法材料の外筒で、
両端に貫通孔のないものを用い、実施例と同様の中空糸
膜束を外筒内に挿入し、外筒の端部にキャップを被せた
後、外筒の外周に注型用樹脂がまわり込まないように透
過液出口からポリエチレンチューブを挿入してエポキシ
樹脂系注型樹脂を注入して硬化させた後、反対側も同様
に注形し、硬化後に、前記実施例と同様の工程を経て中
空茶膜モジュールを得た。In addition, as a comparative example, an outer cylinder made of the same material with the same dimensions as the above example,
Using a hollow fiber membrane bundle with no through holes at both ends, insert the same hollow fiber membrane bundle as in the example into the outer cylinder, cover the end of the outer cylinder with a cap, and then pour the casting resin around the outer periphery of the outer cylinder. After inserting a polyethylene tube from the permeated liquid outlet and injecting epoxy resin casting resin and hardening it, the other side was cast in the same way, and after hardening, the same process as in the previous example was carried out. A hollow tea membrane module was obtained.
この比較例としての中空糸膜モジュールに実施例と同じ
試験を行なったところ、外筒と注型樹脂の接着境界面か
ら空気洩れが認められ、剥離が生じていることが確認さ
れた。When this hollow fiber membrane module as a comparative example was subjected to the same test as in the example, air leakage was observed from the adhesive interface between the outer cylinder and the casting resin, and it was confirmed that peeling had occurred.
尚、発明に用いる外筒の貫通孔の形状及び大きさは特に
限定されず、種々の形状及び大きざが選ばれ、その数も
限定されない。Note that the shape and size of the through-hole of the outer cylinder used in the invention are not particularly limited, and various shapes and sizes may be selected, and the number thereof is also not limited.
しかし、注型用樹脂の接着部分に対する貫通孔の総面積
の割合は、外筒自身の強度、収縮率、樹脂と外筒の接着
力によって求められ、通常10〜90%である。However, the ratio of the total area of the through holes to the adhesive portion of the casting resin is determined by the strength of the outer cylinder itself, the shrinkage rate, and the adhesive force between the resin and the outer cylinder, and is usually 10 to 90%.
又、外筒外周部の樹脂層の厚みも特に限定されない。Further, the thickness of the resin layer on the outer circumference of the outer cylinder is not particularly limited.
〈効果〉
この発明の中空糸膜モジュールは外筒内部において、中
空糸膜束を外筒に結合する樹脂層と外筒の外側の樹脂層
とが外筒端部付近に設けた複数の貫通孔を介して一体化
しているから、樹脂層と外筒とが極めて強固に接着され
る。<Effects> In the hollow fiber membrane module of the present invention, inside the outer cylinder, the resin layer that connects the hollow fiber membrane bundle to the outer cylinder and the resin layer on the outside of the outer cylinder have a plurality of through holes provided near the end of the outer cylinder. Since the resin layer and the outer cylinder are integrated through the resin layer, the resin layer and the outer cylinder are bonded extremely firmly.
従って高温殺菌や蒸気滅菌後の急激な冷却過程において
も樹脂層が外筒から剥離するようなおそれはない。Therefore, there is no fear that the resin layer will peel off from the outer cylinder even during the rapid cooling process after high temperature sterilization or steam sterilization.
又この発明の中空モジュールの製造方法は両端を閉鎖し
た多数の中空糸膜からなる中空糸膜束を、両端に複数の
貫通孔を有する外筒内に挿入し、外筒に被ぜたキャップ
に外筒の外側から注型用樹脂を注入することにより外筒
の貫通孔を介して外筒内にも樹脂が注入されるものであ
るから樹脂の注入がきわめて容易であり、外筒内におけ
る樹脂注入量も外部から確認できるので、樹脂の注入量
の調整が正確に行える。In addition, the method for manufacturing a hollow module of the present invention involves inserting a hollow fiber membrane bundle consisting of a large number of hollow fiber membranes with both ends closed into an outer cylinder having a plurality of through holes at both ends, and inserting the hollow fiber membrane bundle into a cap that covers the outer cylinder. By injecting the resin for casting from the outside of the outer cylinder, the resin is also injected into the outer cylinder through the through hole of the outer cylinder, so it is extremely easy to inject the resin. Since the injection amount can also be checked from the outside, the resin injection amount can be adjusted accurately.
また、注型時は各中空糸膜の端部は閉鎖されているので
、注型樹脂が糸膜内に流入して目詰りを起すおそれがな
いなどの効果がある。Furthermore, since the ends of each hollow fiber membrane are closed during casting, there is an advantage that there is no possibility that the casting resin will flow into the fiber membrane and cause clogging.
第1図はこの発明の中空糸膜モジュールの一例を示す縦
断側面図、第2図は同上に用いる外筒の側面図、第3図
は製造状態の一部切欠縦断側面図である。FIG. 1 is a longitudinal sectional side view showing an example of the hollow fiber membrane module of the present invention, FIG. 2 is a side view of an outer cylinder used in the same, and FIG. 3 is a partially cutaway longitudinal sectional side view of a manufactured state.
Claims (2)
付近に貫通孔を設け、外筒内に挿入した中空糸膜束を、
該貫通孔を介して外筒内に注入硬化させた樹脂により外
筒に固定するとともに外筒の両端部外側も被覆したこと
を特徴とする中空糸膜モジュール。(1) Both ends are open and through holes are provided near both ends of the outer cylinder provided with a permeate outlet, and the hollow fiber membrane bundle inserted into the outer cylinder is
A hollow fiber membrane module characterized in that it is fixed to the outer cylinder with a resin injected into the outer cylinder through the through hole and hardened, and the outer sides of both ends of the outer cylinder are also covered.
通孔を設けた外筒を垂直に立て、下向きとなった該外筒
の端部に上向きにしたキャップを被せるとともに、両端
を閉鎖した多数の中空糸膜からなる中空糸膜束を外筒内
に挿入してその端部を外筒端部からキャップの底部に突
出させた状態で該キャップ内に液状の樹脂を注入して、
この樹脂を外筒の貫通孔から外筒内に流入させ、この樹
脂が硬化したのち、キャップを除去し、外筒から突出し
た中空糸膜束の端部を切除することを特徴とする中空糸
膜中空糸膜モジュールの製造方法。(2) Stand vertically an outer cylinder with both ends open, a permeate outlet provided, and a through hole provided near both ends, and cover the downward facing end of the outer cylinder with an upward facing cap. A hollow fiber membrane bundle consisting of a large number of closed hollow fiber membranes is inserted into an outer cylinder, and a liquid resin is injected into the cap with its end protruding from the end of the outer cylinder to the bottom of the cap. ,
A hollow fiber characterized in that the resin is allowed to flow into the outer cylinder through the through hole of the outer cylinder, and after the resin is cured, the cap is removed and the end of the hollow fiber membrane bundle protruding from the outer cylinder is cut off. A method for manufacturing a hollow fiber membrane module.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60065518A JPS61222510A (en) | 1985-03-28 | 1985-03-28 | Hollow yarn membrane module and its preparation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60065518A JPS61222510A (en) | 1985-03-28 | 1985-03-28 | Hollow yarn membrane module and its preparation |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61222510A true JPS61222510A (en) | 1986-10-03 |
Family
ID=13289329
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60065518A Pending JPS61222510A (en) | 1985-03-28 | 1985-03-28 | Hollow yarn membrane module and its preparation |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61222510A (en) |
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EP1415703A3 (en) * | 2002-10-16 | 2004-08-25 | Toray Industries, Inc. | Hollow-fiber membrane module |
JP2006314937A (en) * | 2005-05-13 | 2006-11-24 | Daicen Membrane Systems Ltd | Membrane module and its manufacturing method |
EP1807176A1 (en) * | 2004-08-23 | 2007-07-18 | Siemens Water Technologies Corp. | Potting process for membrane filtration modules |
WO2007128440A1 (en) | 2006-05-05 | 2007-11-15 | Fresenius Medical Care Deutschland Gmbh | Process and apparatus for introducing a potting composition into a filter apparatus |
US7931463B2 (en) | 2001-04-04 | 2011-04-26 | Siemens Water Technologies Corp. | Apparatus for potting membranes |
US8268176B2 (en) | 2003-08-29 | 2012-09-18 | Siemens Industry, Inc. | Backwash |
US8287743B2 (en) | 2007-05-29 | 2012-10-16 | Siemens Industry, Inc. | Membrane cleaning with pulsed airlift pump |
US8293098B2 (en) | 2006-10-24 | 2012-10-23 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US8318028B2 (en) | 2007-04-02 | 2012-11-27 | Siemens Industry, Inc. | Infiltration/inflow control for membrane bioreactor |
US8377305B2 (en) | 2004-09-15 | 2013-02-19 | Siemens Industry, Inc. | Continuously variable aeration |
US8382981B2 (en) | 2008-07-24 | 2013-02-26 | Siemens Industry, Inc. | Frame system for membrane filtration modules |
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 |
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 |
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-
1985
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