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Dehydration of monohydric alcohols via pervaporation using nano NaX zeolite/ polyvinyl alcohol mixed matrix membranes for biofuel production

机译:使用纳米NaX沸石/聚乙烯醇混合基质膜通过渗透蒸发对一元醇进行脱水以生产生物燃料

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摘要

This paper focuses on the dehydration of monohydric alcohols via pervaporation process for using as biofuel additive. For this purpose, two-layer polyvinyl alcohol (PVA)/polyethersulfone (PES) mixed matrix membranes containing nano NaX zeolite were fabricated. The ATR-FTIR, SEM, AFM and swelling tests were employed to characterize surface properties and morphology of the prepared membranes. The results revealed that incorporation of nano NaX zeolites into the cross-linked PVA layer of membranes improved the separation performance. The total and water fluxes enhanced by increasing the zeolite content, whereas the water separation factor had a maximum at the zeolite concentration of 2%wt. for dehydration of a 90% wt. aqueous ethanol solution. The pervaporative dehydration of aqueous solution of methanol, ethanol and isopropanol indicated that the total permeation flux decreased in the order of methanol > ethanol > isopropanol, while the water separation factor had a reverse trend. Finally, the performance of the papered mixed matrix membranes was compared with a commercial hydrophilic PVA membrane and it was observed that the mixed matrix membrane containing 2% wt. NaX zeolite had higher permeation flux and separation factor than the commercial membrane.
机译:本文重点研究了通过全蒸发过程对一元醇进行脱水以用作生物燃料添加剂。为此目的,制备了包含纳米NaX沸石的两层聚乙烯醇(PVA)/聚醚砜(PES)混合基质膜。使用ATR-FTIR,SEM,AFM和溶胀测试来表征所制备膜的表面性质和形态。结果表明,将纳米NaX沸石掺入膜的交联的PVA层中改善了分离性能。总通量和水通量通过增加沸石含量而增加,而在沸石浓度为2%wt时,水分离系数最大。用于90%wt的脱水乙醇水溶液。甲醇,乙醇和异丙醇水溶液的全蒸发脱水表明,总渗透通量按甲醇>乙醇>异丙醇的顺序降低,而水分离因子却有相反的趋势。最后,将纸化的混合基质膜的性能与商业亲水性PVA膜进行比较,并且观察到含有2重量%的混合基质膜。 NaX沸石比商业膜具有更高的渗透通量和分离系数。

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