Monolayer, composite, gas separation material, filter, gas separation device and method for manufacturing composite
US-12128366-B2 · Oct 29, 2024 · US
US9901883B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9901883-B2 |
| Application number | US-201515539355-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 25, 2015 |
| Priority date | Dec 26, 2014 |
| Publication date | Feb 27, 2018 |
| Grant date | Feb 27, 2018 |
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An object of the present invention is to provide a porous hollow-fiber membrane having high strength while maintaining high pure-water permeation performance. A porous hollow-fiber membrane of the present invention is a porous hollow-fiber membrane including a fluororesin-based polymer, in which the porous hollow-fiber membrane has a columnar texture oriented in a longitudinal direction of the porous hollow-fiber membrane, and a molecular chain of the fluororesin-based polymer is oriented in the longitudinal direction of the porous hollow-fiber membrane.
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The invention claimed is: 1. A porous hollow-fiber membrane comprising a fluororesin-based polymer, wherein the porous hollow-fiber membrane has a columnar texture oriented in a longitudinal direction of the porous hollow-fiber membrane, a molecular chain of the fluororesin-based polymer is oriented in the longitudinal direction of the porous hollow-fiber membrane, an orientation degree π of the molecular chain calculated based on the following formula (1) is 0.4 or more and less than 1.0: Orientation degree π=(180°- H )/180° (1) provided that H is a half-width)(°)of a diffraction intensity distribution in a circumferential direction of a wide-angle X-ray diffraction image, and the columnar texture has a short-side length of from 0.5 μm to 3 μm, and has an aspect ratio of 3 or more. 2. The porous hollow-fiber membrane according to claim 1 , wherein the columnar texture has a thickness uniformity of 0.60 or more. 3. The porous hollow-fiber membrane according to claim 1 , wherein the half-width H is a half-width of an intensity distribution obtained by circumferentially scanning a crystal peak (2θ=20.4°) derived from a (110) plane of polyvinylidene fluoride in wide-angle X-ray diffraction measurement. 4. The porous hollow-fiber membrane according to claim 1 , wherein, when the wide-angle X-ray diffraction measurement is performed at measurement points at 1 cm intervals in the longitudinal direction of the porous hollow-fiber membrane, the orientation degree π is 0.4 or more and less than 1.0 at 80% or more of the measurement points. 5. The porous hollow-fiber membrane according to claim 1 , wherein the fluororesin-based polymer is polyvinylidene fluoride, and a Raman orientation parameter v of the molecular chain obtained by Raman spectroscopy is 3.0 or more. 6. The porous hollow-fiber membrane according to claim 1 , which has a porosity of from 50 to 80%. 7. The porous hollow-fiber membrane according to claim 1 , which has a pure-water permeation performance at 50 kPa and 25° C. of 0.7 m 3 /m 2 /hr or more and a breaking strength of 25 MPa or more. 8. The porous hollow-fiber membrane according to claim 1 , which is formed by thermally induced phase separation.
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