JPS62162007A - Production of electric field-applied hollow fiber - Google Patents
Production of electric field-applied hollow fiberInfo
- Publication number
- JPS62162007A JPS62162007A JP144786A JP144786A JPS62162007A JP S62162007 A JPS62162007 A JP S62162007A JP 144786 A JP144786 A JP 144786A JP 144786 A JP144786 A JP 144786A JP S62162007 A JPS62162007 A JP S62162007A
- Authority
- JP
- Japan
- Prior art keywords
- electric field
- hollow fibers
- hollow fiber
- spinning
- nozzle
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/08—Hollow fibre membranes
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は溶液系における低分子化合物の分離、濃縮、あ
るいは気体系における気体分離、気体濃縮を効率よく行
うための中空糸あるいは中空管(以下単に中空糸という
)の新規な紡糸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 or hollow tube ( The present invention relates to a novel method for spinning hollow fibers (hereinafter simply referred to as hollow fibers).
(従来の技術)
中空糸の紡糸に用いる通常の紡糸口は、高分子原液と内
部凝固液(または気体)とを隔てるために内側ノズルと
外側ノズルを備えた2重管ノズルである。公知の紡糸口
では内側と外側のノズルはステンレス製で溶接あるいは
ねじこみ式になっているので、内外のノズルは絶縁され
ていない。(Prior Art) A typical spinneret used for spinning hollow fibers is a double tube nozzle equipped with an inner nozzle and an outer nozzle to separate the polymer stock solution and the internal coagulation liquid (or gas). In known spinnerets, the inner and outer nozzles are made of stainless steel and are welded or screwed together, so the inner and outer nozzles are not insulated.
従って高分子原液に電界をかけて防止することは不可能
であった。Therefore, it was impossible to prevent this by applying an electric field to the polymer stock solution.
本発明者等は、新規な紡糸法を鋭意開発研究した結果、
電界内において紡糸した中空糸では、その物性値、例え
ば、透水量、親水性の向上(接触角の低下)等が電界を
かけないで紡糸した中空糸に比べて格段に優れた成績を
示すことを見いだし本発明をなしたものである。As a result of intensive research and development of a new spinning method, the present inventors found that
Hollow fibers spun in an electric field exhibit significantly superior physical properties, such as water permeability and improved hydrophilicity (reduction in contact angle), compared to hollow fibers spun without an electric field. The present invention was created based on this discovery.
(発明が解決しようとする問題点)
本発明は、電界内で中空糸を紡糸することにより、表面
親水性の向上した中空糸あるいは透水量等の物性値の優
れた中空糸を得ることを目的とするものである。(Problems to be Solved by the Invention) The purpose of the present invention is to obtain hollow fibers with improved surface hydrophilicity or hollow fibers with excellent physical properties such as water permeability by spinning hollow fibers in an electric field. That is.
(問題点を解決するための手段)
本発明の中空糸の製法は紡糸口の内側ノズルと外側ノズ
ルを絶縁体で隔てた中空紡糸装置を用いて、電界強度I
V / m以上の電界内で紡糸することを特徴とする
。(Means for Solving the Problems) The hollow fiber manufacturing method of the present invention uses a hollow spinning device in which the inner nozzle and outer nozzle of the spinneret are separated by an insulator, and the electric field intensity I
It is characterized by spinning within an electric field of V/m or more.
本発明によって、物性値の改善された中空糸が得られる
理由は、今のところ明確ではないが、一応次のように考
えられる。即ち、電界をかけることにより、キャスト原
液(通常、ボリア−2溶媒、塩類、添加剤等を含む)中
のポリマーのもつ双極子モーメントあるいは荷電基が中
空糸表面に配向を起こし、表面付近の親木性を高め、或
は効率よく配向した双極子または荷電基が溶質あるいは
水の透過性を制御するものと思われる。電界としては、
電界を意図的にかけない場合、すなわち通常の紡糸を行
なう場の電界変化(ノイズ)より、少なくともI V
/ m以上(電界強度I V / m以上)であれば、
局所的に双極子モーメントあるいは荷電基を有する高分
子にモルフォロジー変化を引き起こすと考えられる。し
かしより効果を期待するためには3X10V/m以上が
望ましい。The reason why hollow fibers with improved physical properties can be obtained according to the present invention is not clear at present, but it is thought to be as follows. That is, by applying an electric field, the dipole moments or charged groups of the polymer in the casting stock solution (usually containing Boria-2 solvent, salts, additives, etc.) are oriented to the hollow fiber surface, and the parent particles near the surface are aligned. It is believed that the enhanced woodiness or efficiently oriented dipoles or charged groups control the permeability of solutes or water. As an electric field,
When an electric field is not applied intentionally, that is, at least I V
/ m or more (electric field strength IV / m or more),
It is thought that this locally causes a morphological change in a polymer having a dipole moment or a charged group. However, in order to expect better effects, it is desirable to use 3×10 V/m or more.
本発明の紡糸法に用いた紡糸口は、添付図面に示すよう
に、内側ノズル(1)と外側ノズル(2)がテフロンの
ような絶縁体(3)で隔てられた2重管ノズルで、各ノ
ズルには電極4.4′が設けられている。そのため内側
と外側のノズルは絶縁されており、紡糸原液(5)に電
界をかけて紡糸できるようになっている。(6)は内部
凝固液である。As shown in the accompanying drawing, the spinneret used in the spinning method of the present invention is a double tube nozzle in which an inner nozzle (1) and an outer nozzle (2) are separated by an insulator (3) such as Teflon. Each nozzle is provided with an electrode 4.4'. Therefore, the inner and outer nozzles are insulated so that an electric field can be applied to the spinning dope (5) to perform spinning. (6) is the internal coagulation liquid.
紡糸原液としては、特に限定されないが、局所的に双極
子モーメントを持つポリマー(例えば、ポリスルホン、
ポリエーテルスルホン、ポリエーテルイミドなど)を含
む原液、或は荷電基を有するポリマー(例えばスルホン
化ポリスルホン、スルホン化ポリエーテルスルホン、ス
ルホン化ポリエーテルイミド、カルボキシメチル化ポリ
フェニレンエーテルなど)を含む原液を用いて、本発明
によって紡糸された中空糸は電界による著しい物性値の
改善を示す。たとえば、図面の電極4にプラス電位を与
えてアニオン性荷電物を含む原液を用いて紡糸すると、
得られた中空糸の外表面は、内表面よりマイナス荷電基
をより多く有するようになる。逆に、電極4にマイナス
電位を与えた場合には、内表面がマイナス荷電基を多く
持つようになる。The spinning stock solution is not particularly limited, but polymers with a local dipole moment (e.g., polysulfone,
using a stock solution containing a polymer containing a charged group (e.g., sulfonated polysulfone, sulfonated polyether sulfone, sulfonated polyetherimide, carboxymethylated polyphenylene ether, etc.). Thus, the hollow fibers spun according to the present invention exhibit significant improvements in physical properties due to electric fields. For example, if a positive potential is applied to the electrode 4 in the drawing and a stock solution containing anionic charges is used for spinning,
The outer surface of the obtained hollow fiber has more negatively charged groups than the inner surface. Conversely, if a negative potential is applied to the electrode 4, the inner surface will have many negatively charged groups.
以下実施例によって本発明を更に説明する。The present invention will be further explained below with reference to Examples.
(実施例1)
溶媒としてジメチルアセトアミド、添加剤としてプロピ
レングリコール、さらに
で表わされる繰り返し単位を有するポリスルホンを重量
%で68:14:18の割合で混合し均一な溶液を得た
。このポリマー溶液を図面に示す紡糸口(φa=0.5
mm、φb= 1 、5mm 、 h=2cm)から押
し出し、内部及び外部凝固液として25℃の精製水を用
いて中空糸多孔膜を得た。この場合、原液温度は25℃
で、ノズルから外部凝固液までの距離(空中走行距離)
は3Cm、紡速15m/分の紡糸条件であった。また電
極4はプラス、電極4′はマイナスとして1.5■の電
位を与えた。従って、紡糸原液を1.5×10’V/m
の電界内で紡糸したことになる。(Example 1) Dimethylacetamide as a solvent, propylene glycol as an additive, and polysulfone having a repeating unit represented by are mixed in a weight ratio of 68:14:18 to obtain a uniform solution. This polymer solution was applied to the spinneret shown in the drawing (φa=0.5
mm, φb = 1, 5 mm, h = 2 cm) to obtain a hollow fiber porous membrane using purified water at 25°C as an internal and external coagulation liquid. In this case, the stock solution temperature is 25℃
and the distance from the nozzle to the external coagulating liquid (air travel distance)
The spinning conditions were 3 Cm and a spinning speed of 15 m/min. Further, the electrode 4 was set as positive, and the electrode 4' was set as negative, and a potential of 1.5 .mu. was applied. Therefore, the spinning dope was 1.5×10'V/m
This means that the spinning was carried out within the electric field of .
得られた中空糸の特性は、内径0.75mm、外径1.
35mm、膜厚0.3mm、透水率15rn”/ゴ*d
ay*atms水温25℃、破裂強度30 K g /
cゴ、デキストラン分子量4 X 104の5重量%
に対するカット率は85%であった。The characteristics of the obtained hollow fibers are that the inner diameter is 0.75 mm and the outer diameter is 1.75 mm.
35mm, film thickness 0.3mm, water permeability 15rn”/go*d
ay*atms water temperature 25℃, bursting strength 30Kg/
C, 5% by weight of dextran molecular weight 4 x 104
The cut rate was 85%.
(参考例1)
電界をかけない以外は実施例1と同様にして紡糸し多孔
性中空糸を得た。この中空糸の特性は、内径0.75m
m、外径1.35mm、膜厚0゜3mm、透水率11r
n”/rn’eday*atm*水温25℃、破裂強度
31Kg/crr?、デキストラン分子量4 X 10
4 の5重量%に対するカット率は79%であった。(Reference Example 1) Porous hollow fibers were obtained by spinning in the same manner as in Example 1 except that no electric field was applied. This hollow fiber has an inner diameter of 0.75m.
m, outer diameter 1.35mm, film thickness 0゜3mm, water permeability 11r
n"/rn'eday*atm*Water temperature 25℃, bursting strength 31Kg/crr?, dextran molecular weight 4 X 10
The cut rate for 5% by weight of No. 4 was 79%.
(実施例?)
0 、82 m e q / Hの交換容量を有するス
ルホン化ポリスルホン(米国特許第3709841号に
準じて作成)とポリスルホンの重量割合で1=13の混
合物をポリマーとして用いた以外は、実施例1と同様に
して多孔性中空糸を得た。この中空糸をカチオン染料(
CI Ba5ic Bluel)で染色した所、外
表面は濃厚に染色されたが、内表面はわずかじか染色さ
れなかった。このことより中空糸中のスルホン化ポリス
ルホンは外表面近傍に局在化していると推定された。(Example?) Except that a mixture of sulfonated polysulfone (prepared according to US Pat. No. 3,709,841) and polysulfone with an exchange capacity of 0.0, 82 m eq / H and polysulfone in a weight ratio of 1 = 13 was used as the polymer. A porous hollow fiber was obtained in the same manner as in Example 1. This hollow fiber was dyed with a cationic dye (
When stained with CI Ba5ic Blue), the outer surface was deeply stained, but the inner surface was only slightly stained. From this, it was estimated that the sulfonated polysulfone in the hollow fiber was localized near the outer surface.
得られた中空糸の特性は内径0.74mm、外径1.3
4mm、膜厚0.3mm、透水率19ゴ/m’eday
eatme水温25℃、破裂強度29 K g / C
rn’、デキストラン分子量4X10 (7)5重量
%に対するカット率は82%であった。The characteristics of the obtained hollow fibers are that the inner diameter is 0.74 mm and the outer diameter is 1.3 mm.
4mm, film thickness 0.3mm, water permeability 19g/m'eday
eatme water temperature 25℃, bursting strength 29K g/C
rn', dextran molecular weight 4X10 (7) The cut rate for 5% by weight was 82%.
(実施例3)
電極4はマイナス、電極4′はプラスとして1.5■の
電位を与えた以外は実施例2と同様にBa5ic B
luel)ffi染色した所、外表面はわずかしか染色
されなかったが、内表面は濃厚に染色された。この場合
、実施例2とは逆に内表面にスルホン化ポリスルホンが
局在化していると推定される。(Example 3) Ba5ic B was used in the same manner as in Example 2 except that the electrode 4 was negative and the electrode 4' was positive and a potential of 1.5 cm was applied.
When stained with luel)ffi, the outer surface was only slightly stained, but the inner surface was deeply stained. In this case, contrary to Example 2, it is presumed that sulfonated polysulfone is localized on the inner surface.
(発明の効果)
本発明で得られた中空糸は、電界をかけないで紡糸した
ものと比べて、表面の親木性を増し、かつ透水量等の物
性値を改善することができる。さらに荷電物を含む原液
から中空糸を紡糸した場合、電極の向きを変えることに
より、外表面あるいは内表面に、優先的に極性基を局在
化させることができる。(Effects of the Invention) Compared to those spun without applying an electric field, the hollow fibers obtained by the present invention can increase the wood-philicity of the surface and improve physical properties such as water permeability. Furthermore, when hollow fibers are spun from a stock solution containing charged substances, polar groups can be preferentially localized on the outer or inner surface by changing the orientation of the electrodes.
添付図面は、本発明で使用する紡糸口の1例を示す概略
断面図。The accompanying drawing is a schematic cross-sectional view showing one example of a spinneret used in the present invention.
Claims (1)
紡糸装置を用いて、電界強度1V/m以上の電界内で紡
糸することを特徴とする中空糸の製法。A method for producing hollow fibers, which comprises spinning in an electric field with an electric field strength of 1 V/m or more using a hollow spinning device in which an inner nozzle and an outer nozzle of a spinneret are separated by an insulator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61001447A JPH0753925B2 (en) | 1986-01-09 | 1986-01-09 | Manufacturing method of hollow fiber under electric field |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61001447A JPH0753925B2 (en) | 1986-01-09 | 1986-01-09 | Manufacturing method of hollow fiber under electric field |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62162007A true JPS62162007A (en) | 1987-07-17 |
JPH0753925B2 JPH0753925B2 (en) | 1995-06-07 |
Family
ID=11501692
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61001447A Expired - Lifetime JPH0753925B2 (en) | 1986-01-09 | 1986-01-09 | Manufacturing method of hollow fiber under electric field |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0753925B2 (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001087633A (en) * | 1999-09-21 | 2001-04-03 | Asahi Kasei Corp | Method for preparing hollow fibrous porous film by melt spinning |
JP2007197860A (en) * | 2006-01-25 | 2007-08-09 | Espinex:Kk | Spinneret, method for producing nanofiber using the same and nanofiber |
JP2007327148A (en) * | 2006-06-06 | 2007-12-20 | Tokyo Institute Of Technology | Polyelectrolyte fiber and method for producing the same |
JP2009174066A (en) * | 2008-01-21 | 2009-08-06 | Mecc Co Ltd | Spinneret for electrospinning device |
JP2010236133A (en) * | 2009-03-31 | 2010-10-21 | National Institute Of Advanced Industrial Science & Technology | Apparatus for producing nanofiber by electrospinning method using double-pipe nozzle and nanofiber production method |
JP2017031003A (en) * | 2015-07-31 | 2017-02-09 | 日本電気硝子株式会社 | Production method of glass fiber and production device of glass fiber |
JP2019077964A (en) * | 2017-10-25 | 2019-05-23 | 日本バイリーン株式会社 | Fiber sheet and method for producing fiber sheet |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5971409A (en) * | 1982-03-29 | 1984-04-23 | ロデイア・アクチエンゲゼルシヤフト | Method and apparatus for preparing electlet-filament yarn oranalogue |
-
1986
- 1986-01-09 JP JP61001447A patent/JPH0753925B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5971409A (en) * | 1982-03-29 | 1984-04-23 | ロデイア・アクチエンゲゼルシヤフト | Method and apparatus for preparing electlet-filament yarn oranalogue |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001087633A (en) * | 1999-09-21 | 2001-04-03 | Asahi Kasei Corp | Method for preparing hollow fibrous porous film by melt spinning |
JP2007197860A (en) * | 2006-01-25 | 2007-08-09 | Espinex:Kk | Spinneret, method for producing nanofiber using the same and nanofiber |
JP2007327148A (en) * | 2006-06-06 | 2007-12-20 | Tokyo Institute Of Technology | Polyelectrolyte fiber and method for producing the same |
JP2009174066A (en) * | 2008-01-21 | 2009-08-06 | Mecc Co Ltd | Spinneret for electrospinning device |
JP2010236133A (en) * | 2009-03-31 | 2010-10-21 | National Institute Of Advanced Industrial Science & Technology | Apparatus for producing nanofiber by electrospinning method using double-pipe nozzle and nanofiber production method |
JP2017031003A (en) * | 2015-07-31 | 2017-02-09 | 日本電気硝子株式会社 | Production method of glass fiber and production device of glass fiber |
JP2019077964A (en) * | 2017-10-25 | 2019-05-23 | 日本バイリーン株式会社 | Fiber sheet and method for producing fiber sheet |
Also Published As
Publication number | Publication date |
---|---|
JPH0753925B2 (en) | 1995-06-07 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8967391B2 (en) | Method for preparing composite multilayer porous hollow membrane and device and product thereof | |
EP1321178B1 (en) | A braid-reinforced hollow fiber membrane | |
US4481260A (en) | Aromatic polysulfone type resin hollow fiber membrane and process for producing the same | |
US4822489A (en) | Aromatic polysulfone type resin hollow fiber membrane and a process for producing the same | |
CN1050773C (en) | Polyvinylidene fluoride hollow fibre porous membrane manufacturing method | |
ES494186A0 (en) | MEMBRANE IN THE FORM OF A FLAT SHEET, A SLEEVE SHEET OR A HOLLOW THREAD. | |
CA2075098A1 (en) | Hollow fiber membranes | |
CN101642683A (en) | Double-layer composite hollow fiber nano-filtration membrane and preparation method and special tool thereof | |
JPS62162007A (en) | Production of electric field-applied hollow fiber | |
JPH057051B2 (en) | ||
JPH0647066B2 (en) | Porous separation membrane and method for producing the same | |
CN1158135C (en) | Preparation method of hollow fibre supermicro filtration membrane | |
JPS62117812A (en) | Hollow fiber and its production | |
JPH0569571B2 (en) | ||
KR20070103187A (en) | Porous poly(vinylidene fluoride) hollow fiber membranes composed of both fibril and nodular structures | |
JPS6321914A (en) | Porous hollow yarn membrane of modified cross section | |
JPS61249504A (en) | Ultrafilter membrane | |
JPH0832295B2 (en) | Method for producing composite hollow fiber membrane | |
JP2512909B2 (en) | Method for producing hollow fiber porous membrane | |
Askari et al. | Parametric optimization of poly (ether sulfone) electrospun membrane for effective oil/water separation | |
EP0418082A1 (en) | Membrane fabrication | |
CN113737393B (en) | Electrostatic spinning nanofiber membrane and preparation method thereof | |
CN114307644B (en) | Preparation method of in-situ hollow fiber composite nanofiltration membrane | |
KR20030042790A (en) | A hollow fiber membrane made of polyacrylonitrile and a preparation method thereof | |
CN110982100B (en) | Low-melting-point hot-melt-wire-reinforced toughened polyvinylidene fluoride porous membrane material and preparation method thereof |