JPH0644978B2 - Method for producing hollow fiber semipermeable membrane - Google Patents
Method for producing hollow fiber semipermeable membraneInfo
- Publication number
- JPH0644978B2 JPH0644978B2 JP60270752A JP27075285A JPH0644978B2 JP H0644978 B2 JPH0644978 B2 JP H0644978B2 JP 60270752 A JP60270752 A JP 60270752A JP 27075285 A JP27075285 A JP 27075285A JP H0644978 B2 JPH0644978 B2 JP H0644978B2
- Authority
- JP
- Japan
- Prior art keywords
- hollow fiber
- semipermeable membrane
- fiber semipermeable
- producing
- drying
- 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)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、中空糸状半透膜の製造方法に関するものであ
る。TECHNICAL FIELD The present invention relates to a method for producing a hollow fiber-shaped semipermeable membrane.
中空糸状半透膜は従来、ポリマー、溶媒及び各種添加剤
を含む原液をギヤポンプで環状ノズルに送り、その中心
から純水が外部に原液を伴つて吐出され、次いで凝固浴
においてゲル化したポリマーは更に水洗され、中空糸内
部に純水を封入した状態の中空糸状半透膜が製造され
る。該中空糸状半透膜は、グリセリン等の乾燥防止剤を
内、外面に塗布した後、乾燥、接着工程を経てモジュー
ル化される。しかし、水圧により乾燥防止剤水溶液を中
空糸状半透膜内面に注入、塗布するという従来法では、
中空糸状半透膜の内径が小さくなるにつれ、グリセリン
水溶液等の高粘度溶液の注入は困難となる。従来法で内
部へ注入するならば、その乾燥防止剤の粘度に応じて水
圧を高め、加熱し、更に数時間の処理時間を要する。In the hollow fiber semipermeable membrane, conventionally, a stock solution containing a polymer, a solvent and various additives is sent to an annular nozzle by a gear pump, pure water is discharged from the center with the stock solution to the outside, and then a gelled polymer in a coagulation bath is discharged. Further, the hollow fiber is washed with water to produce a hollow fiber semipermeable membrane in which pure water is enclosed in the hollow fiber. The hollow fiber semipermeable membrane is made into a module by applying a drying inhibitor such as glycerin on the inner and outer surfaces, and then drying and adhering. However, in the conventional method of injecting and coating the aqueous solution of the anti-drying agent on the inner surface of the hollow fiber-shaped semipermeable membrane by water pressure,
As the inner diameter of the hollow fiber semipermeable membrane becomes smaller, it becomes more difficult to inject a highly viscous solution such as an aqueous glycerin solution. If it is injected into the interior by the conventional method, the water pressure is increased according to the viscosity of the anti-drying agent, heating is carried out, and a treatment time of several hours is required.
本発明は、乾燥防止処理を伴なう中空糸状半透膜の製造
方法を提供するものである。The present invention provides a method for producing a hollow fiber-like semipermeable membrane accompanied by a drying prevention treatment.
本発明者らは、中空糸状半透膜が内部に液体が封入され
た状態で製造されることに着目し、鋭意検討を重ねた結
果、中空糸状半透膜内部に紡糸工程において乾燥防止剤
を封入する製造方法を見い出し、本発明を完成させた。The present inventors have paid attention to the fact that the hollow fiber-shaped semipermeable membrane is manufactured in a state in which a liquid is sealed inside, and as a result of intensive studies, as a result, an anti-drying agent was added inside the hollow fiber-shaped semipermeable membrane in the spinning step. The manufacturing method of encapsulation was found, and the present invention was completed.
即ち、本発明は、中空糸状半透膜を、紡糸工程において
乾燥防止剤を含む水溶液を内部に注入し、次に乾燥防止
剤を含む水溶液に接触させることを特徴とする中空糸状
半透膜の製造方法である。That is, the present invention is a hollow fiber semipermeable membrane characterized by comprising injecting an aqueous solution containing a drying inhibitor into a hollow fiber semipermeable membrane in a spinning step and then contacting the solution with an antidrying agent. It is a manufacturing method.
以下本発明の構成について詳述する。The configuration of the present invention will be described in detail below.
中空糸状半透膜としてはどんな孔径、糸径、材質のもの
でも湿式紡糸可能なものならすべて適用出来、また、乾
燥防止剤としては、不揮発性であり、水に容易に溶解、
洗浄出来るものならばどんなものでも良く、粘度及び取
扱い性から見て、多価アルコール水溶液が好ましく、グ
リセリン、ジプロピレングリコール、トリプロピレング
リコール、ポリプロピレングリコール及びテトラエチレ
ングリコールが更に好ましい。As a hollow fiber semipermeable membrane, any pore size, yarn diameter and material can be applied as long as it can be wet-spun, and as a drying inhibitor, it is non-volatile and easily dissolved in water.
Any washable substance may be used, and from the viewpoint of viscosity and handleability, a polyhydric alcohol aqueous solution is preferable, and glycerin, dipropylene glycol, tripropylene glycol, polypropylene glycol and tetraethylene glycol are more preferable.
本発明の中空糸状半透膜を製造するには、まず、多価ア
ルコールを微粒子等をあらかじめフイルターで除去した
純水に溶解し、5〜50wt%好ましくは10〜30wt%
の濃度に調整する。濃度を5wt%以下にすると、中空糸
状半透膜の表面全体が被われない為、乾燥後の透水量の
回復率が20%以下に低下してしまう。また、50wt%
以上にすると、高粘度になる為に、紡糸時に糸切れが発
生し、また、膜の物性にも影響を与えてしまう。つぎ
に、該溶液を定量ポンプにより一定速度で環状ノズルか
ら吐出し、中空糸状半透膜内部に封入される。このよう
にして得られた中空糸状半透膜を、多価アルコール水溶
液に常温で短時間浸漬することで中空糸状半透膜は、乾
燥後も透水量は70%以上回復する。In order to produce the hollow fiber semipermeable membrane of the present invention, first, the polyhydric alcohol is dissolved in pure water from which fine particles and the like have been removed beforehand by a filter, and the amount is 5 to 50 wt%, preferably 10 to 30 wt%.
Adjust to the concentration of. If the concentration is 5 wt% or less, the entire surface of the hollow fiber semipermeable membrane is not covered, so that the recovery rate of the amount of water permeation after drying is reduced to 20% or less. Also, 50 wt%
In the above case, since the viscosity is high, yarn breakage occurs during spinning, and the physical properties of the film are also affected. Next, the solution is discharged from the annular nozzle at a constant rate by a metering pump and enclosed in the hollow fiber semipermeable membrane. By immersing the hollow fiber-shaped semipermeable membrane thus obtained in a polyhydric alcohol aqueous solution for a short period of time at room temperature, the hollow fiber-shaped semipermeable membrane recovers 70% or more in water permeability even after drying.
以下実施例を示す。 Examples will be shown below.
実施例1 乾燥防止剤として、2〜70wt%のグリセリン、ジエチ
レングリコール、テトラエチレングリコール水溶液を用
いて特開昭58−156018号の実施例1と同様に紡
糸し、乾燥防止剤と同じ溶液に常温で30分浸漬し、5
0℃で2時間乾燥した後、透水量の回復率を調べた。そ
の結果を第1図に示す。第1図に示されるように5wt%
以上で透水の回復率は最大となり各溶液固有の値を示し
ているので第1表に示す多価アルコールの30wt%水溶
液を用い、前記と同じ方法で中空糸状半透膜を製造し、
それぞれの透水回復性を評価した。その結果を第1表に
示す。Example 1 As a drying inhibitor, 2 to 70 wt% of glycerin, diethylene glycol and tetraethylene glycol aqueous solution was used and spun in the same manner as in Example 1 of JP-A-58-156018, and the same solution as the drying inhibitor was added at room temperature. Soak for 30 minutes, 5
After drying at 0 ° C. for 2 hours, the recovery rate of water permeability was examined. The results are shown in FIG. 5 wt% as shown in Fig. 1
Since the recovery rate of water permeability is maximum and shows the value peculiar to each solution, a hollow fiber semipermeable membrane is manufactured by the same method as above using a 30 wt% aqueous solution of polyhydric alcohol shown in Table 1.
The water permeability recovery property of each was evaluated. The results are shown in Table 1.
尚、用いた中空糸状半透膜はポリスルホンであり、糸径
は、内径が0.4mm、外径が0.8mmであつた。The hollow fiber semipermeable membrane used was polysulfone, and the thread diameter was 0.4 mm in inner diameter and 0.8 mm in outer diameter.
比較例1 紡糸時に内部に純水を封入したポリスルホン中空糸状半
透膜を実施例1と同様に紡糸し、30wt%グリセリン水
溶液に常温で30分浸漬し、50℃で2時間乾燥した
後、透水量の回復率を調べた。その結果透水量の回復率
は約20%であつた。 Comparative Example 1 A polysulfone hollow fiber semipermeable membrane in which pure water was enclosed during spinning was spun in the same manner as in Example 1, immersed in a 30 wt% glycerin aqueous solution at room temperature for 30 minutes, dried at 50 ° C. for 2 hours, and then permeable to water. The recovery rate of quantity was investigated. As a result, the water permeability recovery rate was about 20%.
本発明の方法で得られた中空糸状半透膜は、乾燥防止剤
に常温で従来の1/10程度の時間浸漬するという極めて簡
便な方法で処理出来、更に形態及び材質を問わず、すべ
ての中空糸状半透膜の乾燥防止処理が出来るという利点
を有する。The hollow fiber-shaped semipermeable membrane obtained by the method of the present invention can be treated by a very simple method of immersing in a drying inhibitor at room temperature for about 1/10 of the time, and further, regardless of form and material, all It has an advantage that the hollow fiber semipermeable membrane can be dried.
第1図は、本発明実施例1におけるグリセリン、テトラ
エチレングリコール、ジエチレングリコール濃度と透水
回復率の関係を示すグラフである。FIG. 1 is a graph showing the relationship between the concentration of glycerin, tetraethylene glycol, diethylene glycol and the water permeation recovery rate in Example 1 of the present invention.
Claims (4)
防止剤を含む水溶液を内部に注入し、次に乾燥防止剤を
含む水溶液に接触させることを特徴とする中空糸状半透
膜の製造方法。1. A method for producing a hollow fiber semipermeable membrane, which comprises injecting an aqueous solution containing an anti-drying agent into a hollow fiber semipermeable membrane in a spinning step and then bringing the hollow fiber semipermeable membrane into contact with the aqueous solution containing the antidrying agent. Method.
リアクリロニトリル、ポリアミド、ポリイミド及びポリ
エーテルスルホン中空糸状半透膜を用いる特許請求の範
囲第1項記載の中空糸状半透膜の製造方法。2. The method for producing a hollow fiber semipermeable membrane according to claim 1, wherein a polysulfone, polyacrylonitrile, polyamide, polyimide and polyethersulfone hollow fiber semipermeable membrane is used as the hollow fiber semipermeable membrane.
特許請求の範囲第1項記載の中空糸状半透膜の製造方
法。3. The method for producing a hollow fiber semipermeable membrane according to claim 1, wherein a polyhydric alcohol is used as a drying inhibitor.
ロピレングリコール、トリプロピレングリコール、ポリ
プロピレングリコール及びテトラエチレングリコールを
用いる特許請求の範囲第3項記載の中空糸状半透膜の製
造方法。4. The method for producing a hollow fiber semipermeable membrane according to claim 3, wherein glycerin, dipropylene glycol, tripropylene glycol, polypropylene glycol and tetraethylene glycol are used as the polyhydric alcohol.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60270752A JPH0644978B2 (en) | 1985-12-03 | 1985-12-03 | Method for producing hollow fiber semipermeable membrane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60270752A JPH0644978B2 (en) | 1985-12-03 | 1985-12-03 | Method for producing hollow fiber semipermeable membrane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62132504A JPS62132504A (en) | 1987-06-15 |
| JPH0644978B2 true JPH0644978B2 (en) | 1994-06-15 |
Family
ID=17490483
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60270752A Expired - Lifetime JPH0644978B2 (en) | 1985-12-03 | 1985-12-03 | Method for producing hollow fiber semipermeable membrane |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0644978B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2512909B2 (en) * | 1986-09-30 | 1996-07-03 | エヌオーケー株式会社 | Method for producing hollow fiber porous membrane |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6022901A (en) * | 1983-07-05 | 1985-02-05 | Toray Ind Inc | Selective permeable hollow fiber |
-
1985
- 1985-12-03 JP JP60270752A patent/JPH0644978B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62132504A (en) | 1987-06-15 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |