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Carbon Dioxide Enrichment PEBAX/MOF Composite Membrane for CO2 Separation

机译:二氧化碳富集PeBax / MOF复合膜用于二氧化碳分离

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摘要

Zeolitic imidazole framework (ZIF-8) was incorporated into poly(ether-block-amide) (Pebax-1657) in differing ratios to prepare mixed matrix membranes (MMMs) for gas separation. As ZIF-8 loading is increased, gas separation selectivity also gradually increases. For economic considerations, the proportion of the increase in selectivity to the amount of MOF loaded per unit was calculated. The results show that mixing 5% MOF gives the best unit performance. With this, a variety of MOFs (UiO-66, UiO-66-NH2, A520, MIL-68(Al) and MIL-100(Fe)) were mixed with PEBAX at 5 loading to prepare MMMs. In this work, metal-organic frameworks (MOFs) were processed using the dry-free method, where in the synthesized MOF was not dried prior to incorporation. The gas separation performance test carried out shows the highest separation performance was exhibited by P-UiO-66, wherein the CO2/N2 gas selectivity was 85.94, and the permeability was 189.77 (Barrer), which was higher than Robeson’s Upper bound in 2008, and obtained a high permeability and selectivity among mixed matrix membranes. In the preparation of high quality MMMs for gas separation, details regarding the interface phenomenon were assessed.
机译:将沸石咪唑框架(ZIF-8)掺入聚(醚嵌段 - 酰胺)(PeBax-1657)中,以便制备气体分离的混合基质膜(MMMS)。随着ZIF-8负载增加,气体分离选择性也逐渐增加。为了经济考虑,计算了每单位加载的MOF量的选择性增加的比例。结果表明,混合5%MOF提供了最佳的单位性能。由此,将各种MOF(UIO-66,UIO-66-NH2,A520,MIL-68(Al)和MIL-100(Fe))与PeBax混合在5加载以制备MMM。在这项工作中,使用无干法处理金属有机框架(MOF),在合成的MOF中未在掺入之前干燥。进行的气体分离性能试验表明P-UIO-66表现出最高的分离性能,其中CO 2 / N 2气体选择性为85.94,渗透率为189.77(禁止),其高于2008年的罗伯森的上限,并在混合基质膜之间获得高渗透性和选择性。在制备用于气体分离的高质量MMMS中,评估了关于界面现象的细节。

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