POROUS MATERIAL FOR CONCENTRATING GAS CONTAINING SILICA, MANUFACTURE THEREOF AND METHOD OF CONCENTRATING GAS BY USINGSAID MANUFACTURE

A hollow, porous, silica-rich fiber, a process for producing the same, and a process for enriching at least one gas from a gaseous mixture utilizing at least one fiber to result in gas separations with good permeability and good selectivity. The fiber is non-crystalline and has pore sizes having a r...

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Hauptverfasser: UORUTAA JIEEMUSU ROBAATOSON, UIRIAMU PATORITSUKU MAASHIYARU, HAABAATO UIRIAMU BAACHI, JIYOSEFU JIYON HAMUMERU
Format: Patent
Sprache:eng
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Zusammenfassung:A hollow, porous, silica-rich fiber, a process for producing the same, and a process for enriching at least one gas from a gaseous mixture utilizing at least one fiber to result in gas separations with good permeability and good selectivity. The fiber is non-crystalline and has pore sizes having a range of 1 to around 50 Angstroms in diameter and a mean pore size of around less than 20 Angstroms in diameter and a filament diameter in the range of 1 to around 200 microns and a wall thickness in the range of around 1 to 30 microns. The fibers with a fine pore structure and thin walls are produced by forming hollow glass fibers hindered or fully phase-separable boron and/or alkali metal glass composition, by attenuation from melt at speeds in the range of 500 ft/min to around 20,000 ft/min. The phase-separable glass fibers are heat treated to yield limited phase-separated hollow glass fibers and these fibers are leached to extract acid and/or water soluble components. For fully phase-separable, hollow glass fibers, a limited heat treatment is used before leaching, where the heat treatment is at a temperature of around 300 to less than 480 DEG C for a time of around 5 minutes to 24 hours. The hindered, phase-separable, hollow glass fibers are heat treated at a temperature in the range of about 400 to about 600 DEG C. At least one hollow, porous, silica-rich fiber is used in a device suitable to contain a gaseous mixture and the permeate is withdrawn from the silica-rich fiber at the opposite side from that at which the gaseous mixture contacts the hollow, porous fiber.