JPH043623Y2 - - Google Patents
Info
- Publication number
- JPH043623Y2 JPH043623Y2 JP1985047558U JP4755885U JPH043623Y2 JP H043623 Y2 JPH043623 Y2 JP H043623Y2 JP 1985047558 U JP1985047558 U JP 1985047558U JP 4755885 U JP4755885 U JP 4755885U JP H043623 Y2 JPH043623 Y2 JP H043623Y2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- membrane
- permeate
- fibers
- flow path
- 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
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Description
【考案の詳細な説明】
<技術分野>
本考案は液体分離装置に関し、特に超純水や無
菌水の製造などに適した液体分離装置に関する。[Detailed Description of the Invention] <Technical Field> The present invention relates to a liquid separation device, and particularly to a liquid separation device suitable for producing ultrapure water or sterile water.
<従来技術>
液体分離装置は、例えば、多孔質膜を2枚合せ
て内部を透過液流路に形成した膜封筒と原液スペ
ーサとを重ねて透過液集液管の回りに巻回してな
る膜分離エレメントを用い、膜封筒間を流れる原
液から多孔質膜を透過して膜封筒内の透過液流路
に入つた透過液を集液管に集めて外部に取出すよ
うに構成されている。<Prior art> A liquid separation device is, for example, a membrane formed by combining two porous membranes and forming a permeate flow path inside a membrane envelope and a stock solution spacer, which are overlapped and wound around a permeate collection tube. It is configured to use a separation element to collect permeated liquid that has passed through the porous membrane from the stock solution flowing between the membrane envelopes and entered the permeated liquid flow path in the membrane envelopes into a liquid collection tube and taken out to the outside.
従来の装置では、前記透過液の集液管として、
硬質塩ビ、変成ポリフエニレンオキサイド、エポ
キシ系FRP、ステンレス製パイプが使用されて
きた。しかし、近年、超純水や無菌水製造用とし
て用いられる場合に、熱水や蒸気等による熱殺菌
にもそれら装置が耐え得る必要が生じてきた。 In conventional devices, as a collection pipe for the permeate,
Hard PVC, modified polyphenylene oxide, epoxy FRP, and stainless steel pipes have been used. However, in recent years, when used for producing ultrapure water or sterile water, it has become necessary for these devices to withstand heat sterilization using hot water, steam, or the like.
ところが先に示した材質の集液管を用いる従来
の液体分離装置では、繰返し加熱等による集液管
の熱伸縮の繰返しにより、該集液管と前記膜封筒
との接着部がはがれてしまい、原液の透過液への
混入等を起こして実用上問題があつた。また集液
管にエポキシ系FRPやステンレス製パイプを用
いた場合は、熱膨張による接着部のはがれは妨げ
るが、未硬化物や金属イオンの透過液への溶出が
多くなり、得られる透過水の純度が悪くなる欠点
があつた。またステンレス製パイプの場合、価格
が高く、重量も重く実用的でない。 However, in a conventional liquid separation device using a liquid collection tube made of the material mentioned above, the adhesive portion between the liquid collection tube and the membrane envelope peels off due to repeated thermal expansion and contraction of the liquid collection tube due to repeated heating, etc. This caused problems in practical use due to contamination of the stock solution with the permeate. In addition, when epoxy FRP or stainless steel pipes are used as liquid collecting pipes, peeling of the adhesive part due to thermal expansion is prevented, but uncured substances and metal ions are more likely to be eluted into the permeated liquid, and the resulting permeated water is It had the disadvantage of poor purity. In addition, stainless steel pipes are expensive, heavy, and impractical.
<目的>
本考案は上記従来技術の欠点を解消し、超純水
や無菌水製造の熱殺菌時のような高温や冷熱の繰
返し下においても、集液管が熱膨張を起こさず、
膜封筒との接着部のはがれのない液体分離装置の
提供を目的とする。<Purpose> The present invention solves the above-mentioned drawbacks of the conventional technology, and the liquid collecting pipe does not undergo thermal expansion even under repeated high temperature and cold heat such as during heat sterilization in the production of ultrapure water and sterile water.
The purpose of the present invention is to provide a liquid separation device that does not peel off at the adhesive portion with a membrane envelope.
<構成>
本考案は、多孔質膜を2枚合せて内部を透過液
流路に形成した膜封筒と、原液スペーサとを重ね
て透過液集液管の回りに巻回してなる膜分離エレ
メントを有し、膜封筒間を流れる原液から多孔質
膜を透過して膜封筒内の透過液流路に入つた透過
液を集液管に集めて外部に取出すようにした液体
分離装置において、上記の集液管は、硬質塩化ビ
ニル、ポリプロピレン、ポリカーボネート、ポリ
スルホンもしくはポリ四フツ化エチレンのいずれ
かのプラスチツクと、熱収縮の小さい繊維との複
合材料によつて製作され、その繊維によつて軸方
向の強度が強化されていることによつて特徴づけ
られる。<Structure> The present invention uses a membrane separation element consisting of a membrane envelope in which two porous membranes are combined to form a permeate flow path inside, and a stock solution spacer that is overlapped and wound around a permeate collection tube. In a liquid separation device, the permeated liquid that has passed through the porous membrane from the stock liquid flowing between the membrane envelopes and entered the permeated liquid channel in the membrane envelope is collected in a liquid collecting pipe and taken out to the outside. The liquid collecting pipe is made of a composite material of hard vinyl chloride, polypropylene, polycarbonate, polysulfone, or polytetrafluoroethylene plastic and fibers with low heat shrinkage. Characterized by enhanced strength.
<実施例>
第1図は本考案の実施装置に用いる膜分離エレ
メントの斜視図、第2図は膜分離エレメントの構
造を示す一部断面斜視図、第3図は集液管の一部
破断斜視図、第4図は集液管の他の例を示す一部
破断斜視図である。<Example> Fig. 1 is a perspective view of a membrane separation element used in the implementation device of the present invention, Fig. 2 is a partially sectional perspective view showing the structure of the membrane separation element, and Fig. 3 is a partially cutaway view of a liquid collecting pipe. A perspective view, FIG. 4 is a partially cutaway perspective view showing another example of a liquid collecting pipe.
液体分離装置の主要構成部である膜分離エレメ
ント1は中心部の透過液集液管10と、該集液管
10の回りに巻回された膜封筒20と原液スペー
サ30とからなる。前記膜封筒20は2板の多孔
質膜21,21を合せて周縁部を接着し、内部を
透過液流路22に形成している。なお前記膜封筒
20の接着は原液が流入してくる端部20aには
施こされていない。また膜封筒20に集液管10
への接着部は膜21,21同士の接着はなされ
ず、透過液が集液管10の透過液流入孔11から
管10内に入るようにされている。 The membrane separation element 1, which is the main component of the liquid separation device, consists of a permeated liquid collecting pipe 10 in the center, a membrane envelope 20 wound around the liquid collecting pipe 10, and a raw liquid spacer 30. The membrane envelope 20 has two porous membranes 21, 21 bonded together at their peripheral edges to form a permeate flow path 22 inside. Note that the adhesive of the membrane envelope 20 is not applied to the end 20a into which the stock solution flows. In addition, the liquid collection tube 10 is attached to the membrane envelope 20.
The membranes 21 and 21 are not bonded to each other, and the permeate flows into the pipe 10 from the permeate inflow hole 11 of the liquid collecting pipe 10.
一方前記膜封筒20と重ね合されて原液スペー
サ30が設けられ、この原液スペーサ30と前記
膜封筒20とを一緒に集液管10に巻回すること
により膜分離エレメント1が構成される。前記原
液スペーサ30が介在する膜封筒20間が原液路
31になる。なお透過液流路22に透過液スペー
サ23を入れてもよい。 On the other hand, a stock solution spacer 30 is provided overlapping the membrane envelope 20, and the membrane separation element 1 is constructed by winding the stock solution spacer 30 and the membrane envelope 20 together around the liquid collection tube 10. The space between the membrane envelopes 20 with the stock solution spacer 30 interposed therebetween becomes a stock solution path 31. Note that a permeate spacer 23 may be inserted into the permeate flow path 22.
前記集液管10は、前述したように、膜封筒2
0と接着され、透過液流路22と連通する透過液
流入孔11を表面に有する中空管で、内孔部12
を流入孔1から流入した透過液が通る。そして本
考案ではこの集液管10を熱伸縮の少ない繊維4
0で軸方向に繊維強化しており、加熱冷却による
熱伸縮を防止している。強化用繊維40としては
熱伸縮の少ないものとして、ガラス繊維やカーボ
ン繊維の長繊維(一端から他端まで連続したも
の)や短繊維を用いることができ、これを集液管
10の肉厚内或いは表面層に軸方向に施して複合
材料としている。繊維40は、第3図に示すよう
に軸に平行に施してもよく、また第4図に示すよ
うに、軸に適当な角度、例えば5〜30度、で網目
状に施してもよい。前記集液管10自体の材質
は、硬質塩化ビニル、ポリプロピレン、ポリカー
ボネート、ポリスルホンもしくはポリ四フツ化エ
チレンの低溶出性のプラスチツクが用いられる。 As mentioned above, the liquid collection tube 10 is connected to the membrane envelope 2.
0 and has a permeate inflow hole 11 on its surface that communicates with the permeate flow path 22.
The permeate flowing in from the inflow hole 1 passes through. In the present invention, this liquid collecting pipe 10 is made of fibers 4 with little heat expansion and contraction.
0, fiber reinforced in the axial direction to prevent thermal expansion and contraction due to heating and cooling. As the reinforcing fibers 40, long fibers (continuous from one end to the other end) or short fibers of glass fibers or carbon fibers can be used as materials with little heat expansion and contraction, and these can be used within the wall thickness of the liquid collecting pipe 10. Alternatively, it is applied to the surface layer in the axial direction to form a composite material. The fibers 40 may be applied parallel to the axis, as shown in FIG. 3, or in a mesh pattern, as shown in FIG. 4, at a suitable angle to the axis, such as from 5 to 30 degrees. As the material of the liquid collecting pipe 10 itself, a low elution plastic such as hard vinyl chloride, polypropylene, polycarbonate, polysulfone, or polytetrafluoroethylene is used.
G矢符のように導入された原液は膜封筒20,
20間から膜21を透過して透過液として透過液
通路22内に入り、中心部の集液管10に集めら
れ、矢符Tで示すように外部へ排出される。膜2
1を透過しなかつた液は濃縮液として原液流路3
1から矢符Nで示すように外部へ排出される。 The stock solution introduced like the G arrow is membrane envelope 20,
The liquid passes through the membrane 21 from between 20 and enters the permeate passage 22 as a permeate, is collected in the liquid collection tube 10 in the center, and is discharged to the outside as shown by arrow T. membrane 2
The liquid that did not pass through 1 is passed through the concentrate flow path 3 as a concentrated liquid.
1 to the outside as shown by the arrow N.
<効果>
以上説明したように、本考案によれば、集液管
を、硬質塩化ビニル、ポリプロピレン、ポリカー
ボネート、ポリスルホンもしくはポリ四フツ化エ
チレンのいずれかのプラスチツクと、熱収縮の小
さい繊維との複合材料によつて製作して、その繊
維によつて軸方向の強度を強化したので、超純水
や無菌水製造の熱殺菌時などにおいて、高温や冷
熱が繰り返して行われる場合であつても、集液管
の熱膨張・収縮がなく、これによつて原水の透過
水側への漏れ等が生じことがない。しかも、ポリ
四フツ化エチレンなどのプラスチツクは未硬化物
や金属イオンの溶出率が低いことから、純度の高
い透過水を得るころができる。<Effects> As explained above, according to the present invention, the liquid collection pipe is made of a composite of hard vinyl chloride, polypropylene, polycarbonate, polysulfone, or polytetrafluoroethylene plastic and fibers with low heat shrinkage. It is made of a material with reinforced axial strength due to its fibers, so even when high temperature and cold heat are repeatedly applied during heat sterilization in the production of ultrapure water and sterile water, etc. There is no thermal expansion or contraction of the liquid collecting pipe, which prevents leakage of raw water to the permeate side. Furthermore, since plastics such as polytetrafluoroethylene have a low elution rate of uncured substances and metal ions, it is possible to obtain permeated water with high purity.
第1図は本考案の実施装置に用いる膜分離エレ
メントの斜視図、第2図は膜分離エレメントの構
造を示す一部断面斜視図、第3図は集液管の一部
破断斜視図、第4図は集液管の他の例を示す一部
破断斜視図である。
1……膜分離エレメント、10……集液管、1
1……透過液流入孔、20……膜封筒、21……
多孔質膜、22……透過液流路、30……原液ス
ペーサ、31……原液流路、40……繊維。
Fig. 1 is a perspective view of a membrane separation element used in the apparatus for implementing the present invention, Fig. 2 is a partially cutaway perspective view showing the structure of the membrane separation element, Fig. 3 is a partially cutaway perspective view of a liquid collecting pipe, FIG. 4 is a partially cutaway perspective view showing another example of the liquid collecting pipe. 1... Membrane separation element, 10... Liquid collection pipe, 1
1... Permeate inflow hole, 20... Membrane envelope, 21...
Porous membrane, 22... Permeated liquid channel, 30... Stock solution spacer, 31... Stock solution channel, 40... Fiber.
Claims (1)
した膜封筒と、原液スペーサとを重ねて透過液集
液管の回りに巻回してなる膜分離エレメントを有
し、上記膜封筒間を流れる原液から多孔質膜を透
過して膜封筒内の透過液流路に入つた透過液を上
記集液管に集めて外部に取出すようにした液体分
離装置において、上記集液管は、硬質塩化ビニ
ル、ポリプロピレン、ポリカーボネート、ポリス
ルホンもしくはポリ四フツ化エチレンのいずかの
プラスチツクと、熱収縮の小さい繊維との複合材
料によつて製作され、その繊維によつて軸方向の
強度が強化されていることを特徴とする液体分離
装置。 It has a membrane separation element formed by stacking two porous membranes to form a permeate flow path inside and a stock solution spacer and winding it around a permeate collection tube, and between the membrane envelopes. In the liquid separation device, the permeated liquid that has passed through the porous membrane and entered the permeated liquid flow path in the membrane envelope from the stock liquid flowing through the membrane envelope is collected in the liquid collecting pipe and taken out to the outside. Manufactured from a composite material of vinyl chloride, polypropylene, polycarbonate, polysulfone, or polytetrafluoroethylene plastic and fibers with low heat shrinkage, and the fibers strengthen the axial strength. A liquid separation device characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985047558U JPH043623Y2 (en) | 1985-03-29 | 1985-03-29 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1985047558U JPH043623Y2 (en) | 1985-03-29 | 1985-03-29 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61163004U JPS61163004U (en) | 1986-10-09 |
| JPH043623Y2 true JPH043623Y2 (en) | 1992-02-04 |
Family
ID=30562995
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1985047558U Expired JPH043623Y2 (en) | 1985-03-29 | 1985-03-29 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH043623Y2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5145682B2 (en) * | 2006-10-02 | 2013-02-20 | 東洋紡株式会社 | Permeated water nozzle for reverse osmosis membrane module and reverse osmosis membrane module |
| CA2736814C (en) | 2008-09-02 | 2017-02-28 | Natrix Separations Inc. | Chromatography membranes, devices containing them, and methods of use thereof |
| EP2709749B1 (en) | 2011-05-17 | 2018-08-15 | Natrix Separations Inc. | Method of use of wrapped membranes for chromatography |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES8608030A1 (en) * | 1983-12-01 | 1986-06-01 | Exxon Research Engineering Co | A METHOD FOR SEPARATING AUXILIARY DEPARAFFINATION AGENT FROM A PARAFFIN |
-
1985
- 1985-03-29 JP JP1985047558U patent/JPH043623Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61163004U (en) | 1986-10-09 |
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