JPS6248526B2 - - Google Patents
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- Publication number
- JPS6248526B2 JPS6248526B2 JP57168043A JP16804382A JPS6248526B2 JP S6248526 B2 JPS6248526 B2 JP S6248526B2 JP 57168043 A JP57168043 A JP 57168043A JP 16804382 A JP16804382 A JP 16804382A JP S6248526 B2 JPS6248526 B2 JP S6248526B2
- Authority
- JP
- Japan
- Prior art keywords
- membrane
- membranes
- tubular
- fluid
- adhesive seal
- 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
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- Separation Using Semi-Permeable Membranes (AREA)
Description
【発明の詳細な説明】
本発明は機能性高分子膜よりなる管状分離膜の
構造に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the structure of a tubular separation membrane made of a functional polymer membrane.
近年省資源、省エネルギー型で環境問題や医用
分野にまで多くの効果の期待出来る高分子機能性
分離膜が活発に研究・開発・実用化されている。
例えば高性能イオン交換膜による海水淡水化や、
非汚染性膜による省エネルギー型都市排水二次処
理システム、さらに医用分野では人工腎臓や人口
肺、化学工業では水素分離膜や酸素富化膜、酸素
利用化学反応膜など多方面ですでに実用化されつ
つある。そして従来の機能性高分子膜は膜の形そ
のまま利用するか、あるいは中空繊維の形に紡糸
されたものが利用された。しかし膜の形のままで
利用するのは、分離効率の向上をめざしていく
と、どうしても膜の厚みを極限まで薄くしていか
ねばならず、その場合の欠点として膜の耐圧など
の機械的強度が保持できず別に支持層として織布
や不織布、スポンジなど複合せねばならず、支持
体構造が複雑で、かつ高価になる。さらに膜の形
のまま利用する場合の欠点は分離を目的とする流
体に対して膜充填密度を大きくとれない事であ
り、効率の良い分離を困難にしている点にもあ
る。膜法にも長所はあり、平面なので多孔膜の孔
径や膜厚さらに膜の機能など種々の品質を検査し
た膜が使用出来る点や、いろいろな機能を持つた
膜の複合化を作りやすい点などである。次に中空
繊維膜は、膜厚が薄くても耐圧があり分離を目的
とする流体に対して膜充填密度を高く出来る長所
がある。欠点として複合膜にする事が困難であ
り、中空繊維膜の膜厚等の品質管理も難かしく、
さらに中空繊維1本1本に内部流体を導入してい
くシール構造に、煩雑な作業が必要である。 In recent years, research, development, and practical use have been actively conducted on polymeric functional separation membranes that are resource-saving, energy-saving, and expected to have many effects on environmental issues and medical fields.
For example, seawater desalination using high performance ion exchange membranes,
Energy-saving urban wastewater secondary treatment systems using non-polluting membranes, artificial kidneys and artificial lungs in the medical field, and hydrogen separation membranes, oxygen enrichment membranes, and oxygen-utilizing chemical reaction membranes in the chemical industry have already been put into practical use in many fields. It's coming. Conventional functional polymer membranes have either been used as they are, or spun into hollow fibers. However, if the membrane is used in its original form, the thickness of the membrane must be made as thin as possible in order to improve separation efficiency. cannot be retained, and a composite support layer such as woven fabric, non-woven fabric, or sponge must be used, making the support structure complicated and expensive. Furthermore, the disadvantage of using the membrane in its original form is that the membrane cannot be packed at a high packing density for the fluid to be separated, making efficient separation difficult. The membrane method also has advantages, such as the fact that it is flat, so membranes that have been tested for various qualities such as porous membrane pore size, membrane thickness, and membrane function can be used, and it is easy to create composite membranes with various functions. It is. Next, hollow fiber membranes have the advantage that even if the membrane is thin, it can withstand pressure and can have a high membrane packing density for the fluid to be separated. The disadvantage is that it is difficult to make a composite membrane, and quality control such as the thickness of the hollow fiber membrane is also difficult.
Furthermore, the seal structure for introducing internal fluid into each hollow fiber requires complicated work.
本発明人等は、膜の形のまま利用する場合の欠
点を少なくし、長所を活かし、中空繊維の形の長
所をも併せ持つ構造にする事を目的に鋭意研究の
結果、次に述べるような構造を持つ機能性高分子
分離膜を発明する事に成功した。 The inventors of the present invention have conducted extensive research with the aim of reducing the disadvantages and utilizing the advantages of using membranes in their original form, and created a structure that also has the advantages of hollow fibers, as described below. We succeeded in inventing a functional polymer separation membrane with a structure.
本発明は少なくとも2枚以上重ねた機能性高分
子分離膜が、その左右両耳端部でシールされてお
り、このシールは最初より管状膜での形で作られ
ていても良く、また2枚以上の膜を左右両耳端部
で、接るシールされたものでも良いが、そのよう
な左右両端部でシールされる2枚以上の膜の両端
部の内側に多数本の線状・点状又はループ状の接
着シール部を設ける事により、機能性膜を出発原
料として之を2枚以上重ね、その左右両端部でシ
ールされたものの端部の内側に多数の流体の通路
を持つた機能性高分子膜に関するものである。 In the present invention, at least two stacked functional polymer separation membranes are sealed at both left and right end ends, and these seals may be made in the form of tubular membranes from the beginning, or two or more layers may be sealed. The above membranes may be sealed at both the left and right ends, but if the two or more membranes are sealed at both left and right ends, a large number of lines or dots may be formed on the inside of both ends. Or, by providing a loop-shaped adhesive seal part, two or more sheets of functional membranes are stacked as a starting material, and both left and right ends are sealed, but functionality is achieved by having multiple fluid passages inside the ends. It relates to polymer membranes.
本発明の構造の例を図によつて説明すると第1
図は2枚の高分子機能性分離膜1と2の左右両端
部3,3′でシールされて管状になつている。そ
の内側部はさらに線状の4,4′,4″,…で接着
シールされて、多群の細管状部を形成した構造に
なる。左右両端部のシール3,3′や内側部の接
着シール部4,4′,4″、の接着方法は高分子機
能性膜1と2がアセテートや多孔性ポリエチレン
等のヒートシール可能な場合はヒートシールが簡
便で都合が良いが、また別な方法として重ねる前
の膜の少なくとも片方の内側に接着剤を線状に塗
布して後重ね合せ、熱接着(ホツトメルト接着剤
の場合)や、接着剤に含まれている水や溶剤の除
去(エマルジヨン接着剤や溶剤型接着剤)などで
も接着出来るし、あるいは、膜1,2の間に接着
剤の付いた糸やテープをサンドイツチする事によ
つても可能である。その結果、2枚の機能性高分
子膜の間に多数の細管状部が形成され、その細か
い管状群の1本1本が中空繊維の1本1本と同等
の効果を生みだす。 An example of the structure of the present invention will be explained with reference to the drawings.
The figure shows two polymeric functional separation membranes 1 and 2 sealed at both left and right ends 3 and 3' to form a tubular shape. The inner part is further adhesively sealed with linear lines 4, 4', 4'', etc., forming a structure that forms multiple groups of thin tube-shaped parts.Seals 3, 3' at both left and right ends and adhesive sealing at the inner part Heat sealing is simple and convenient when the polymeric functional membranes 1 and 2 are made of acetate, porous polyethylene, etc. and can be heat-sealed, but there are other methods for bonding the sealing parts 4, 4', and 4''. Adhesive is applied in a line on the inside of at least one side of the membranes before they are stacked, and then they are stacked together, followed by thermal bonding (in the case of hot melt adhesives) or removal of water or solvent contained in the adhesive (emulsion bonding). Adhesion can be achieved by using adhesive or solvent type adhesive, or by sandwiching a thread or tape coated with adhesive between the membranes 1 and 2. As a result, a large number of thin tube-like parts are formed between the two functional polymer membranes, and each of the fine tube-like parts produces the same effect as each hollow fiber.
第2図は、管内流体5の導入部および排出部で
は、所定の距離を残して、その内側に接着シール
した部分を設ける事により、内部の多群管状体そ
れぞれへの管内流体5の導入又は排出の際の導入
管又は排出管との接続を容易にし、かかる部分に
特別のシールを必要とせず、これは従来の中空繊
維には持合せていない本発明の構造で始めて可能
になつた事である。 FIG. 2 shows that in the introduction and discharge parts of the pipe fluid 5, a predetermined distance is left and an adhesive-sealed portion is provided inside the pipe fluid 5, thereby introducing or discharging the pipe fluid 5 into each of the internal multiple group tubular bodies. The structure of the present invention makes it easy to connect to the inlet pipe or the discharge pipe during discharge, and does not require special seals in such parts, which is not possible with conventional hollow fibers. It is.
第3図は、第2図の内側部の接着シール部4,
4′,4″,…を膜のシール部をループ状として残
してそのループ内に切れ目を持つ構造にした事
で、この事で膜の外部の流体が表裏に自由に通じ
うるようになり、中空繊維と同等の役割をし、中
空繊維のモジユールとして有名なデユポン社の
“permasep”タイプに組込めるようになつた。 FIG. 3 shows the adhesive seal portion 4 on the inner side of FIG.
4', 4'', ... are structured so that the seal part of the membrane is left as a loop and there is a cut in the loop, this allows the fluid outside the membrane to freely communicate between the front and back sides. It plays the same role as hollow fibers, and can now be incorporated into DuPont's "permasep" type, which is famous for its hollow fiber modules.
第4図はその“permasep”タイプのモジユー
ルの例で、5が導入流体、6が排出流体で、8が
この分離膜によつて透過した透過流体である。内
部には本発明の第3図の多群の管状部よりなる分
離膜を詰めた例で、中空繊維同等に膜充填密度も
上げられる。また導入流体や排出流体のシールも
第3図の構造の膜を使用すれば非常に容易な事が
判る。 FIG. 4 shows an example of the "permasep" type module, where 5 is an inlet fluid, 6 is an outlet fluid, and 8 is a permeate fluid that has permeated through this separation membrane. This is an example in which a separation membrane consisting of multiple groups of tubular parts as shown in FIG. 3 of the present invention is packed inside, and the packing density of the membrane can be increased to the same level as that of hollow fibers. Furthermore, it can be seen that sealing of the introduced fluid and the discharged fluid is very easy if the membrane having the structure shown in FIG. 3 is used.
第5図は、内側部の接着シール部を千鳥状の直
線にし、そのシール部をループ状としてシールを
保つたままの形でそのループ内に切れ目を入れた
場合である。第5図のように多群管状部が千鳥状
に配列されている場合は内部流体が流れる際、
転々流動して撹拌効果を生じやすく、管状部が短
かくても効率の良い分離膜にする事が出来る。 FIG. 5 shows a case where the adhesive seal portion on the inner side is made into a staggered straight line, and the seal portion is formed into a loop, and cuts are made in the loop while maintaining the seal. When the multi-group tubular parts are arranged in a staggered manner as shown in Fig. 5, when the internal fluid flows,
It easily flows and produces a stirring effect, and even if the tubular part is short, it can be made into an efficient separation membrane.
第3図や第5図のような切れ目を入れる方法と
しては、カミソリ刃などで切れ目を入れても良い
が、ヒートシール可能な膜ではいわゆる溶断によ
つて、内部の接着シールと切れ目を入れるのが同
時に可能であり、そのようなカツターとして、膜
の溶融開始温度以上に加熱された熱刃がロールに
植えられた熱刃ロータリーカツターと、液体によ
り冷却された弾性体ロールとの間に膜を連続的に
通して熱刃に当つた所を溶断していく方法である
所の本願発明者等の先願発明特公昭61−11757
「熱可塑性皮膜に切れ目を入れる方法」が最も適
した方法の1つである。 To make the cuts as shown in Figures 3 and 5, you can use a razor blade or the like to make the cuts, but with heat-sealable films, it is best to make the cuts with the internal adhesive seal by so-called fusing. is possible at the same time, and as such a cutter, a film is cut between a hot blade rotary cutter, in which a hot blade heated above the melting temperature of the film is planted in the roll, and an elastic roll cooled by a liquid. Patent Publication No. 11,757/1986 of the inventors of the present application, which is a method of continuously passing through the hot blade and fusing the part that hits the hot blade.
One of the most suitable methods is the method of making cuts in the thermoplastic film.
第1,2,3,5図の構造は接着シール部が直
線の場合のみを記したが、かならずしも直線でな
くても良く種々の曲線にする事により内部流体の
加圧や減圧を繰返したり、内部流体の撹拌をもた
らす構造にする事も可能である。また接着シール
部を種々の点の配列とする事も出来る。第6図は
管状部の内側部の接着シール部が円状で、ループ
状となりその中心に穴があいている場合で、この
ような構造も本発明の効果を満足出来る。 The structures in Figures 1, 2, 3, and 5 are shown only when the adhesive seal part is a straight line, but it does not necessarily have to be a straight line and can be made into various curves to repeatedly pressurize and depressurize the internal fluid. It is also possible to create a structure that provides agitation of the internal fluid. Furthermore, the adhesive seal portion can be arranged at various points. FIG. 6 shows a case where the adhesive seal portion on the inner side of the tubular portion is circular and loop-shaped with a hole in the center, and such a structure can also satisfy the effects of the present invention.
本発明の特長として、膜を出発原料としている
ので、穴径、膜厚、膜の機能性(例えばイオン交
換膜の吸着基の分布など)を充分に品質管理した
状態で使用出来るので高品位の管状膜になる。さ
らに膜を多層複合化して高度の機能を持たせた管
にする事も出来る。また、内部流体の導入や排出
の際の流体シールが従来の中空繊維に比較になら
ない位容易で簡単に出来る点も本発明の大きな特
長である。 A feature of the present invention is that since a membrane is used as a starting material, it can be used with sufficient quality control in terms of pore diameter, membrane thickness, and membrane functionality (e.g., the distribution of adsorption groups in ion exchange membranes), resulting in high-quality products. It becomes a tubular membrane. Furthermore, it is also possible to create tubes with advanced functionality by combining multiple layers of membranes. Another great feature of the present invention is that fluid sealing when introducing and discharging internal fluid can be done more easily and simply than in conventional hollow fibers.
また、中空繊維の場合は、多数本の繊維がそれ
ぞれ独立しているので、モジユールに組込む際、
本数を数えたり、長さを揃えたり、ねじれや曲り
を直したりしなければならず、その本数も数千本
から数万本にも及ぶことがあり、その取扱いが非
常に面倒であるが、本発明の構造の場合は中空繊
維の数百本が1つのユニツトになつていると同等
の構造になつており、しかもそのユニツトの中で
は長さは一定であり、ねじれや曲りも問題になら
ず、非常に取り扱いが簡単である。 In addition, in the case of hollow fibers, many fibers are independent, so when incorporating them into a module,
You have to count the number of pieces, make the lengths the same, and fix twists and bends, and the number of pieces can range from several thousand to tens of thousands, making handling them extremely troublesome. In the case of the structure of the present invention, the structure is equivalent to that of several hundred hollow fibers forming one unit, and the length is constant within the unit, so twisting and bending are not a problem. It is extremely easy to handle.
管状体内部に出来る多数の内部流体通路も円形
ばかりでなく楕円やその他さまざまな形状をとり
うるので、中空繊維の円に近い形のものよりは内
部流体量に対して接触膜面積を広くとる事も出来
る。その上この管状体内部の内部流体通路が千鳥
状など種々の通路を形成出来るので、内部流体を
加圧、減圧を繰返したり撹拌したりして膜の分離
効果を向上させる事が可能である。また、本発明
の構造は膜を出発原料としているにもかかわら
ず、中空繊維の場合のように内部流体の圧力を高
める事も可能であり、かつ内部流体に対して膜充
填密度を高くする事が出来る。さらに、従来の機
能性膜をそのままの形で使用出来るので製造も簡
単でコストの安い製品にする事が可能であり、ま
た膜の種類や管の径、内部流体のさまざまな形状
の通路など適応範囲の広い機能性高分子分離膜の
管状体にする事が出来る。 The numerous internal fluid passages formed inside the tubular body are not only circular, but can also take on various shapes such as ellipses, so it is better to have a larger contact membrane area for the amount of internal fluid than a hollow fiber with a shape close to a circle. You can also do it. Furthermore, since the internal fluid passages inside this tubular body can be formed in various ways, such as in a staggered pattern, it is possible to improve the separation effect of the membrane by repeatedly pressurizing and depressurizing the internal fluid, or by stirring it. Furthermore, although the structure of the present invention uses a membrane as a starting material, it is possible to increase the pressure of the internal fluid as in the case of hollow fibers, and it is also possible to increase the packing density of the membrane relative to the internal fluid. I can do it. Furthermore, since conventional functional membranes can be used as they are, they can be manufactured easily and at low cost, and can be adapted to various types of membranes, tube diameters, and various shapes of internal fluid passages. It can be made into a tubular body with a wide range of functional polymer separation membranes.
第1,2,3,5,6図は本発明の構造の例を
示す模式図、第4図はそれを分離膜として装置に
組込んだ場合の、装置の1例を示す斜視図であ
る。
Figures 1, 2, 3, 5, and 6 are schematic diagrams showing examples of the structure of the present invention, and Figure 4 is a perspective view showing an example of the device when it is incorporated into the device as a separation membrane. .
Claims (1)
でシールされて管状部が形成されている機能性高
分子機能膜で、その管状の内側部に多数本の線
状、点状、またはループ状の接着シール部を有す
る分離膜において、その管状部の流体入口部また
は入口部および出口部に所定の距離をおいてその
内側に接着シール部を設けることにより、膜内部
流体の導入および排出を容易にしたことを特徴と
する管状分離膜。 2 特許請求の範囲1の接着シール部の膜におい
て、そのシール部がループ状となつて、その中に
切れ目または穴を持つており、外部の流体が表裏
自由に通じるごとくなしたことを特徴とする管状
分離膜。[Scope of Claims] 1. A functional polymer functional membrane formed by stacking at least two layers and sealing the left and right ends of the membrane to form a tubular part, the inner part of the tubular part having a large number of linear, In a separation membrane having a dot-shaped or loop-shaped adhesive seal part, by providing an adhesive seal part inside the fluid inlet part or the inlet and outlet parts of the tubular part at a predetermined distance, the fluid inside the membrane can be sealed. A tubular separation membrane characterized in that it facilitates the introduction and discharge of. 2. The film of the adhesive seal part of claim 1 is characterized in that the seal part is loop-shaped and has a cut or a hole therein, so that external fluid can freely communicate between the front and back sides. Tubular separation membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16804382A JPS5959215A (en) | 1982-09-27 | 1982-09-27 | Tubular separation membrane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16804382A JPS5959215A (en) | 1982-09-27 | 1982-09-27 | Tubular separation membrane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5959215A JPS5959215A (en) | 1984-04-05 |
| JPS6248526B2 true JPS6248526B2 (en) | 1987-10-14 |
Family
ID=15860757
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16804382A Granted JPS5959215A (en) | 1982-09-27 | 1982-09-27 | Tubular separation membrane |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5959215A (en) |
-
1982
- 1982-09-27 JP JP16804382A patent/JPS5959215A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5959215A (en) | 1984-04-05 |
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