Spinning device
US-9222200-B2 · Dec 29, 2015 · US
US9731250B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9731250-B2 |
| Application number | US-201414769062-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 26, 2014 |
| Priority date | Feb 27, 2013 |
| Publication date | Aug 15, 2017 |
| Grant date | Aug 15, 2017 |
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Official abstract text for this publication.
Disclosed is a method for producing a hollow fiber carbon membrane using a hollow fiber carbon membrane-forming material by means of a dry method or dry-wet method comprising a spinning step, a drying step, an infusibilization step, and a carbonization step as basic steps; wherein in the infusibilization step, heat treatment is performed at least two times at different temperatures, with the second temperature being higher than the first temperature. It is preferable that the second heat treatment is performed directly after the first treatment is performed, without once cooling to room temperature. The obtained hollow fiber carbon membrane has improved permeability, without reducing its separation coefficient.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a hollow fiber carbon membrane using a hollow fiber carbon membrane-forming material by means of a dry method or dry-wet method comprising a spinning step, a drying step, an infusibilization step, and a carbonization step as basic steps; wherein in the infusibilization step, heat treatment is performed at least two times at different temperatures, with the second temperature being higher than the first temperature; in the spinning step, spinning is performed using a water-soluble organic polyamine aqueous solution having a concentration of 10 to 30 wt. % as a core liquid. 2. The method for producing a hollow fiber carbon membrane according to claim 1 , wherein in the infusibilization step, after the first heat treatment is performed, the temperature is changed directly to the second heating temperature without once being cooled to room temperature, and the second heat treatment is performed. 3. The method for producing a hollow fiber carbon membrane according to claim 1 , wherein in the infusibilization step, after the first heat treatment is performed at a heating temperature of 150 to 280° C., the second heat treatment is performed at a heating temperature of 200 to 350° C., which is higher than the first heating temperature. 4. The method for producing a hollow fiber carbon membrane according to claim 1 , wherein the hollow fiber carbon membrane-forming material is a polyphenylene oxide-based polymer. 5. The method for producing a hollow fiber carbon membrane according to claim 1 , wherein the water-soluble organic polyamine is an alkylenediamine, polyethylene polyamine, aminoalkyl group-containing amine, ether group-containing amine, or water-soluble organic amine-based polymer having a weight average molecular weight Mw of 200 to 5,000. 6. The method for producing a hollow fiber carbon membrane according to claim 2 , wherein in the infusibilization step, after the first heat treatment is performed at a heating temperature of 150 to 280° C., the second heat treatment is performed at a heating temperature of 200 to 350° C., which is higher than the first heating temperature.
Details relating to the spinning process · CPC title
porous · CPC title
Core-skin structure; Spinnerette packs therefor · CPC title
from macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds · CPC title
Carbon · CPC title
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