Composite porous hollow fiber membrane, production method for composite porous hollow fiber membrane, composite porous hollow fiber membrane module, and operation method for composite porous hollow fiber membrane module

Patent metadata

Field	Value
Publication number	US-11020709-B2
Application number	US-201716312852-A
Country	US
Kind code	B2
Filing date	Jun 23, 2017
Priority date	Jun 24, 2016
Publication date	Jun 1, 2021
Grant date	Jun 1, 2021

Abstract

The present invention relates to a composite porous hollow-fiber membrane including a first layer and a second layer which each include a fluororesin-based polymer, in which the first layer has a columnar texture oriented in a longitudinal direction of the composite porous hollow-fiber membrane, the columnar texture has an average value v of a Raman orientation parameter calculated with the specific formula, and the second layer has a three-dimensional network texture and has an average surface-pore diameter of 5.0 nm to 5.0 μm.

First claim

The invention claimed is:

1. A composite porous hollow-fiber membrane comprising a first layer and a second layer which each comprise a fluororesin-based polymer,
wherein the first layer has a columnar texture oriented in a longitudinal direction of the composite porous hollow-fiber membrane,
the columnar texture has an average value v of a Raman orientation parameter calculated with the following formula (1) of 1.5-4.0, and
the second layer has a three-dimensional network texture and has an average surface-pore diameter of 5.0 nm to 5.0 μm:
Raman orientation parameter=( I 1270-parallel/ I 840-parallel)/( I 1270-vertical/ I 840-vertical)  (1),

provided that,
I1270-parallel: Raman band intensity at 1,270 cm −1 under parallel conditions,
I1270-vertical: Raman band intensity at 1,270 cm −1 under vertical conditions,
I840-parallel: Raman band intensity at 840 cm −1 under the parallel conditions,
I840-vertical: Raman band intensity at 840 cm −1 under the vertical conditions,
the parallel conditions: the longitudinal direction of the composite porous hollow-fiber membrane is parallel with a polarization direction, and
the vertical conditions: the longitudinal direction of the composite porous hollow-fiber membrane is orthogonal with the polarization direction.

2. The composite porous hollow-fiber membrane according to claim 1 , wherein the columnar texture has a short-side length of 0.5 μm to 3 μm and an aspect ratio of 3 or higher.

3. The composite porous hollow-fiber membrane according to claim 1 , wherein the columnar texture has a thickness uniformity of 0.50 or higher.

4. The composite porous hollow-fiber membrane according to claim 1 , wherein molecular chains in the columnar texture have a ratio between a maximum Raman orientation parameter M and a minimum Raman orientation parameter m, M/m, of from 1.5 to 4.0.

5. The composite porous hollow-fiber membrane according to claim 1 , wherein molecular chains in the columnar texture have a maximum Raman orientation parameter M of 4.0 or less.

6. The composite porous hollow-fiber membrane according to claim 1 , wherein the first layer has a porosity of 40-80%.

7. The composite porous hollow-fiber membrane according to claim 1 , which has a pure-water permeation performance at 50 kPa and 25° C. of 0.1 m 3 /m 2 /hr or higher, a breaking strength of 23 MPa or higher, and a Young's modulus of 0.15 GPa to 0.40 GPa.

8. The composite porous hollow-fiber membrane according to claim 1 , wherein molecular chains of the fluororesin-based polymer have a degree of orientation π in the longitudinal direction of the composite porous hollow-fiber membrane of less than 0.4, or the molecular chains of the fluororesin-based polymer are in a non-oriented state, the degree of orientation π being calculated with the following formula (4):
Degree of orientation π=(180°- H )/180°  (4),

provided that H is a half-value width (°) of a circumferential-direction diffraction intensity distribution of a wide-angle X-ray diffraction image.

9. A composite porous hollow-fiber membrane module comprising:
a tubular case having, in a height direction thereof, a first end and a second end;
a plurality of the composite porous hollow-fiber membranes according to claim 1 disposed in the tubular case;
a fluid inflow/outflow port located in a sidewall of the tubular case further toward the second-end side than the center of the tubular case; and
a fluid inflow/outflow port located in a first-end-side end face of the tubular case,
wherein hollows of the composite porous hollow-fiber membranes are opened on the second-end side and closed on the first-end side.

10. A method for operating the composite porous hollow-fiber membrane module according to claim 9 , the method comprising simultaneously performing the following step (A) and step (B):
(A) a step in which a liquid to be filtrated is introduced into the tubular case through the fluid inflow/outflow port located in the first-end-side end face, and the liquid to be filtrated is discharged from the tubular case through the fluid inflow/outflow port located in the sidewall on the second-end side; and
(B) a step in which a filtrate is taken out from the hollows of the composite porous hollow-fiber membranes toward the second end.

11. The method for operating the composite porous hollow-fiber membrane module according to claim 10 , wherein the step (B) and the following step (D) are repeatedly performed:
(D) a step in which, after the step (B), a fluid is filtrated by passing the fluid from the hollows of the composite porous hollow-fiber membranes on the second-end side to an outside of the composite porous hollow-fiber membranes.

12. The method for operating the composite porous hollow-fiber membrane module according to claim 11 , wherein the step (B) and the step (D) are repeatedly performed and the following step (E) is further performed:
(E) a step in which a gas is introduced into the tubular case through the fluid inflow/outflow port located in the first-end-side end face, and the gas is discharged from the tubular case through the fluid inflow/outflow port located in the sidewall on the second-end side.

13. A method for operating the composite porous hollow-fiber membrane module according to claim 9 , the method comprising simultaneously performing the following step (B) and step (C):
(B) a step in which a filtrate is taken out from the hollows of the composite porous hollow-fiber membranes toward the second end; and
(C) a step in which a liquid to be filtrated is introduced into the tubular case through the fluid inflow/outflow port located in the sidewall on the second-end side, and the liquid to be filtrated is discharged from the tubular case through the fluid inflow/outflow port located in the first-end-side end face.

14. The method for operating the composite porous hollow-fiber membrane module according to claim 13 , wherein the step (B) and the following step (D) are repeatedly performed:
(D) a step in which, after the step (B), a fluid is filtrated by passing the fluid from the hollows of the composite porous hollow-fiber membranes on the second-end side to an outside of the composite porous hollow-fiber membranes.

15. The method for operating the composite porous hollow-fiber membrane module according to claim 14 , wherein the step (B) and the step (D) are repeatedly performed and the following step (E) is further performed:
(E) a step in which a gas is introduced into the tubular case through the fluid inflow/outflow port located in the first-end-side end face, and the gas is discharged from the tubular case through the fluid inflow/outflow port located in the sidewall on the second-end side.

Assignees

• Toray Industries

Inventors

• SHIMURA Shun
• Iwai Kenta
• Hanakawa Masayuki
• Kitade Tamotsu
• Kimura Masahiro

Classifications

• B01D67/00165

  Composition of the coagulation baths · CPC title

• B01D2323/08

  Specific temperatures applied · CPC title

• B01D2325/34

  Molecular weight or degree of polymerisation · CPC title

• B01D69/12

  Composite membranes; Ultra-thin membranes · CPC title

• B01D2325/021

  Pore shapes · CPC title