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Porous siliceous-containing gas enriching material and process of manufacture and use
Porous siliceous-containing gas enriching material and process of manufacture and use
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机译:多孔含硅气体富集材料及其制造和使用方法
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摘要
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°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°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one hollow, porous, silica-rich fiber is used in a device suitable to contain a gaseous mixture and the permeate is withdrawn from the silica-rich fiber at the opposite side from that at which the gaseous mixture contacts the hollow, porous fiber.
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机译:一种中空的,富含二氧化硅的多孔纤维,其生产方法以及一种利用至少一种纤维从气态混合物中富集至少一种气体的方法,从而可以实现具有良好渗透性和选择性的气体分离。该纤维是非晶体的,并且具有在1至约50埃的直径范围内的孔径,在直径内小于约20埃的平均孔径以及在1至约200微米范围内的长丝直径和壁。厚度在1至30微米左右。具有细孔结构和薄壁的纤维是通过以500 ft / min至约20,000 ft的速度从熔体中衰减而形成受阻或完全可相分离的硼和/或碱金属玻璃组合物制成的中空玻璃纤维而制成的/分钟。将相分离的玻璃纤维进行热处理以产生有限的相分离的中空玻璃纤维,并沥滤这些纤维以提取酸和/或水溶性组分。对于完全可相分离的中空玻璃纤维,在浸出之前使用有限的热处理,其中在约300至480℃以下的温度下进行约5分钟至24小时的热处理。在约400至约600℃的温度范围内对受阻的,相分离的中空玻璃纤维进行热处理。在适于容纳气态混合物的装置中使用至少一根中空的,多孔的,富含二氧化硅的纤维,并且从富含二氧化硅的纤维中在与气体混合物接触中空的多孔纤维的一侧相反的一侧排出渗透液。 。
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