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Pervaporation of isopropanol-water mixture using poly(vinyl) alcohol-zsm-5 membranes

机译:使用聚乙烯醇-zsm-5膜对异丙醇-水混合物进行全蒸发

摘要

The pervaporation separation of isopropanol-water mixture was carried out using poly(vinyl) alcohol (PVA) membrane incorporated with 0.2 wt% ZSM-5 zeolite. The manipulated variables were feed temperature and feed concentration. Initially, 5 wt% of PVA powder was dissolved in distilled water at 98 °C. The solution was stirred using magnetic stirrer for 1 hour to produce a homogenous solution. It was then cooled to room temperature before added with the zeolite. The PVA-zeolite solution was stirred for 24 hours at room temperature before it was casted on a porous support. The support layers were produced through phase inversion using casting solution of 12 wt% polysulphone, 11 wt% cellusolve and 77 wt% N,N-dimetil formamide (DMF). Finally, the modified composite membranes were produced by casting the PVA- zeolite solution on the porous polysulphone support layers. Pervaporation tests were conducted using SOLTEQudPervaporation Bench Test Unit (Model: TR 12). The results showed the increase of water concentration in the feed and operating temperature, resulted in higher flux and lower selectivity. ZSM-5 filled PVA membrane showed potential as a separation medium for the pervaporation separation of isopropanol-water mixtures.
机译:异丙醇-水混合物的渗透蒸发分离是使用掺有0.2 wt%ZSM-5沸石的聚乙烯醇(PVA)膜进行的。操纵变量是进料温度和进料浓度。最初,将5 wt%的PVA粉末溶于98°C的蒸馏水中。使用磁力搅拌器将溶液搅拌1小时以产生均匀溶液。然后将其冷却至室温,然后加入沸石。将PVA-沸石溶液在室温下搅拌24小时,然后将其浇铸在多孔载体上。使用12重量%的聚砜,11重量%的纤维素和77重量%的N,N-二甲酰胺甲酰胺(DMF)的浇铸溶液通过相转化来制备支撑层。最后,通过将PVA沸石溶液浇铸在多孔聚砜支撑层上来生产改性复合膜。使用SOLTEQ udPervaporation Bench Test Unit(型号:TR 12)进行渗透蒸发测试。结果表明进料中水浓度和操作温度的增加,导致通量较高和选择性较低。 ZSM-5填充的PVA膜显示出作为异丙醇-水混合物全蒸发分离的分离介质的潜力。

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