首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Polyvinyl alcohol)/ZSM-5 zeolite mixed matrix membranes for pervaporation dehydration of isopropanol/water solution through response surface methodology
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Polyvinyl alcohol)/ZSM-5 zeolite mixed matrix membranes for pervaporation dehydration of isopropanol/water solution through response surface methodology

机译:聚乙烯醇)/ ZSM-5沸石混合基质膜,用于通过响应表面方法渗透异丙醇/水溶液的渗透脱水

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Mixed matrix membranes (MMMs) of poly(vinyl alcohol) (PVA) containing certain amounts of ZSM-5 zeolite were evaluated for pervaporation dehydration of highly concentrated isopropanol aqueous solution. The effects of zeolite content, feed composition and feed temperature on the membrane separation performance are in detail examined by using a preliminarily one-factor-each time method and a systematically response surface methodology (RSM). Preliminarily results show the dehydration separation factor/selectivity have been greatly boosted but without the cost of pervaporation flux/permeance after adding zeolite ZSM-5, and it is consistent very well with the Arrhenius activation energy estimations where water molecules require much less energy whereas ethanol molecules need much more energy to transport through the membrane, probably because of the favorable hydrophilic and porous features of zeolite ZSM-5 as revealed by swelling and water contact angle results. High feed isopropanol concentration and low feed temperature are both observed to lead to very low pervaporation flux/permeance but very relatively high separation factor/selectivity. The RSM results suggest that zeolite content, feed composition and feed temperature all have highly significant impacts on total pervaporation flux and separation factor. The interaction effect of zeolite content and feed temperature on separation factor is for the first time found to be also significant. The polynomial models established according to the RSM analysis can fit very well against the experimental data with a very high coefficient of determination and the predictions given for optimized conditions have been experimentally confirmed by the validation results with a deviation of less than 2.0%. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
机译:含有一定量的ZSM-5沸石的聚(乙烯醇)(PVA)的混合基质膜(MMM)用于高浓度异丙醇水溶液的渗透蒸发脱水。通过使用初步的单因素 - 每种时间方法和系统响应表面方法(RSM),详细研究了沸石含量,进料组合物和进料温度对膜分离性能的影响。初步结果表明,脱水分离因子/选择性大大提升但是在添加沸石ZSM-5后没有渗透渗透磁通/渗透率的成本,并且与Arrhenius激活能量估计相一致,水分子需要更少的能量,而乙醇分子需要更多的能量来通过膜运输,可能是因为沸石ZSM-5的有利亲水和多孔特征,如通过溶胀和水接触角度透露。观察到高进料异丙醇浓度和低进料温度,以导致极低的渗透熔剂通量/渗透性,但具有非常高的分离因子/选择性。 RSM结果表明,沸石含量,饲料组合物和饲料温度都对总渗透熔剂和分离因子具有显着的影响。沸石含量和饲料温度对分离因子的相互作用效应是第一次发现也是显着的。根据RSM分析建立的多项式模型可以非常适合于具有非常高的测定系数的实验数据,并且通过验证结果实验证实了对优化条件的预测,其偏差小于2.0%。 (c)2019化学工程师机构。 elsevier b.v出版。保留所有权利。

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