Method for producing hollow fiber membrane and hollow fiber membrane-spinning nozzle

Patent metadata

Field	Value
Publication number	US-2017348644-A1
Application number	US-201515539776-A
Country	US
Kind code	A1
Filing date	Sep 3, 2015
Priority date	Sep 3, 2015
Publication date	Dec 7, 2017
Grant date	—

Abstract

A method for manufacturing a hollow fiber membrane has a spinning step of applying a first membrane forming stock solution and a second membrane forming stock solution for forming a porous membrane layer to the outer peripheral surface of a hollow porous base material using a nozzle for hollow fiber membrane spinning and solidifying these membrane forming stock solutions, wherein a draft ratio (V B /V A ), which is the ratio of feed velocity V B for hollow porous base material fed out from a base material feed opening to linear velocity V A for the first membrane forming stock solution and the second membrane forming stock solution discharged from a membrane forming stock solution discharge opening of the nozzle for hollow fiber membrane spinning, is set to 1-6.

First claim

1 . A method for producing a hollow fiber membrane using a hollow fiber membrane-spinning nozzle configured as below, comprising:
a spinning step for applying and coagulating a film-forming dope on the peripheral surface of a hollow porous substrate to form a porous membrane layer, wherein the linear velocity (V A ) of discharging the film-forming dope from the dope discharge port relative to the feed rate (V B ) of feeding out the hollow porous substrate from the substrate feed port is set to have a draft ratio (V B /V A ) of 1 to 6, wherein the hollow fiber membrane-spinning nozzle is configured to have a substrate insertion hole for the hollow porous substrate to be inserted and a dope flow channel for the film-forming dope to be distributed, in which a ring-shaped dope discharge port for discharging the film-forming dope distributed through the dope flow channel is formed on the outer side of a substrate feed port with a tube-shaped wall disposed between them so as to surround the substrate feed port for feeding out the hollow porous substrate coming through the substrate insertion hole.

2 . The method for producing a hollow fiber membrane according to claim 1 , wherein the aperture area of the dope discharge port is set to be no greater than 3 times the cross-sectional area of the hollow porous substrate cut perpendicular to its longitudinal direction.

3 . The method for producing a hollow fiber membrane according to claim 1 , wherein the aperture area of the dope discharge port is set to be no greater than 15 mm 2 .

4 . The method for producing a hollow fiber membrane according to claim 1 , set to use a film-forming dope having a viscosity at 40° C. of 30,000 mPa·s or higher.

5 . A hollow fiber membrane-spinning nozzle for applying a film-forming dope to form a porous membrane layer on the peripheral surface of a hollow porous substrate, configured to have a substrate insertion hole into which the hollow porous substrate is to be inserted and a dope flow channel through which the film-forming dope is to be distributed,
wherein a ring-shaped dope discharge port for discharging the film-forming dope distributed through the dope flow channel is formed on the outer side of a substrate feed port with a tube-shaped wall disposed between them so as to surround the substrate feed port for feeding out the hollow porous substrate coming through the substrate insertion hole, the thickness of the tip end of the tube-shaped wall is set at 0.1 mm to 0.75 mm, and the aperture area of the dope discharge port is set to be no greater than 15 mm 2 .

6 . The hollow fiber membrane-spinning nozzle according to claim 5 , wherein the aperture area of the dope discharge port is set to be no greater than 3 times the cross-sectional area, cut to be perpendicular to a longitudinal direction, of the hollow porous substrate to be inserted in the substrate insertion hole.

7 . (canceled)

8 . The hollow fiber membrane-spinning nozzle according to claim 5 , the diameter of the substrate feed port is set to be 1.01 times to 1.20 times the diameter of the hollow porous substrate inserted in the substrate insertion port.

9 . The hollow fiber membrane-spinning nozzle according to claim 5 , wherein a straight portion having the same diameter as that of the dope discharge port and a length of at least 1 mm is formed in the dope flow channel extending from near the dope discharge port to the dope discharge port.

10 . The hollow fiber membrane-spinning nozzle according to claim 5 , wherein a diameter tapering portion is arranged in the dope flow channel near the dope discharge port to have a diameter decreasing toward the dope discharge port.

11 . The hollow fiber membrane-spinning nozzle according to claim 5 , wherein a branching-merging mechanism is formed in the dope flow channel and the film-forming dope passes through the dope flow channel while branching and merging repeatedly.

12 . The hollow fiber membrane-spinning nozzle according to claim 5 , wherein at least two dope flow channels are formed, and a dope lamination portion is formed for the dope flow channels to merge near the dope discharge port so that film-forming dopes coming from the dope flow channels are formed into a composite laminate inside the nozzle.

13 . The hollow fiber membrane-spinning nozzle according to claim 5 , wherein at least two dope flow channels are formed, each dope flow channel is configured to have a dope distribution hole for distributing a film-forming dope and a ring-shaped dope reservoir for the film-forming dope coming through the dope distribution hole to be stored on the outer side of the substrate insertion hole, and the dope reservoir for storing a film-forming dope to be laminated on the outer side is shifted in an axis direction of the substrate insertion hole so as to be located on the downstream side of the dope reservoir for storing a film-forming dope to be laminated on the inner side.

14 . The hollow fiber membrane-spinning nozzle according to claim 13 , wherein the dope distribution holes are formed to have an interval at least 60 degrees apart from each other around the central axis of the substrate insertion hole.

15 . The hollow fiber membrane-spinning nozzle according to claim 11 , wherein the branching-merging mechanism is a porous element and the film-forming dope passes through the element while repeatedly branching and merging.

16 . The hollow fiber membrane-spinning nozzle according to claim 11 , wherein the dope flow channel is configured to have a dope reservoir where the film-forming dope is stored in a ring shape on the outer side of the substrate insertion hole, and the branching-merging mechanism is a filler layer with particles filled inside the dope reservoir.

17 . The hollow fiber membrane-spinning nozzle according to claim 11 , wherein the dope flow channel is configured to have a dope reservoir where the film-forming dope is stored in a ring shape on the outer side of the substrate insertion hole, and the dope reservoir is vertically divided into two or more storage cells.

18 . The hollow fiber membrane-spinning nozzle according to claim 13 , wherein a delay mechanism is formed in the dope flow channel to delay the passage of a film-forming dope, and the delay mechanism is configured to be a meandering portion that causes the film-forming dope to meander vertically between the dope reservoir and the dope shaping portion for forming the film-forming dope into a tube shape.

Assignees

• Mitsubishi Chem Corp

Inventors

• Mizuta Masahiko
• Shinada Katsuhiko
• Sumi Toshinori

Classifications

• B01D69/085

  Details relating to the spinneret · CPC title

• B01D69/087 Primary

  Details relating to the spinning process · CPC title

• B01D69/10

  Supported membranes; Membrane supports · CPC title

• D01D5/24

  with a hollow structure; Spinnerette packs therefor (D01D5/38 takes precedence; producing tubes of plastic material B29D; addition of agents forming hollow filaments D01F1/08) · CPC title

• B01D67/0016

  Coagulation · CPC title