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首页> 外文期刊>Journal of Applied Polymer Science >Preparation of zeolite-incorporated poly(dimethyl siloxane) membranes for the pervaporation separation of isopropyl alcohol/water mixtures
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Preparation of zeolite-incorporated poly(dimethyl siloxane) membranes for the pervaporation separation of isopropyl alcohol/water mixtures

机译:含沸石的聚二甲基硅氧烷膜的制备,用于异丙醇/水混合物的全蒸发分离

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ZSM-5 zeolite-incorporated poly(dimethyl siloxane) membranes were prepared, and the molecular dispersion of the zeolite in the membrane matrix was confirmed with scanning electron microscopy. After the swelling of the membranes was studied at 30 degrees C, the membranes were subjected to the pervaporation separation of isopropyl alcohol/water mixtures at 30,40, and 50 degrees C. The effects of the zeolite loading and feed composition on the pervaporation performances of the membranes were analyzed. Both the permeation flux and selectivity increased simultaneously with increasing zeolite content in the membrane matrix. This was examined on the basis of the enhancement of hydrophobicity, selective adsorption, and the establishment of molecular sieving action. The membrane containing the highest zeolite loading (30 mass %) had the highest separation selectivity (80.84) and flux (6.78 x 10(-2) kg m(-2) h(-1)) at 30 degrees C with 5 mass % isopropyl alcohol in the feed. From the temperature dependence of the diffusion and permeation values, the Arrhenius activation parameters were estimated. A pure membrane exhibited higher activation energy values for permeability (E-p) and diffusivity (E-D) than zeolite-incorporated membranes, and signified that permeation and diffusion required more energy for transport through the pure membrane because of its dense nature. Obviously, the zeolite-incorporated membranes required less energy because of their molecular sieving action, which was attributed to the presence of straight and sinusoidal channels in the framework of the zeolite. For the zeolite-incorporated membranes, the activation energy values obtained for isopropyl alcohol permeation were significantly lower than the water permeation values, and this suggested that the zeolite-incorporated membranes had higher selectivity toward isopropyl alcohol. The EP and ED values ranged between 21.81 and 31.12 kJ/mol and between 15.27 and 41.49 kJ/mol, respectively. All the zeolite-incorporated membranes exhibited positive values of the heat of sorption, and this suggested that the heat of sorption was dominated by Henry's mode of sorption. (c) 2005 Wiley Periodicals, Inc.
机译:制备掺有ZSM-5沸石的聚(二甲基硅氧烷)膜,并通过扫描电子显微镜确认沸石在膜基质中的分子分散性。在30°C下研究了膜的溶胀之后,将膜在30,40和50°C下进行异丙醇/水混合物的全蒸发分离。沸石负载量和进料组成对全蒸发性能的影响分析膜的数量。渗透通量和选择性都随着膜基质中沸石含量的增加而增加。在增强疏水性,选择性吸附和建立分子筛作用的基础上进行了检查。含有最高沸石负载量(30质量%)的膜在30°C和5质量%的情况下具有最高的分离选择性(80.84)和通量(6.78 x 10(-2)kg m(-2)h(-1))饲料中的异丙醇。根据扩散和渗透值的温度依赖性,估算了阿累尼乌斯活化参数。纯膜比掺有沸石的膜表现出更高的渗透性(E-p)和扩散性(E-D)活化能值,并表明渗透和扩散由于其致密性而需要更多能量才能通过纯膜运输。显然,掺入沸石的膜由于其分子筛作用而需要较少的能量,这归因于沸石骨架中存在直通道和正弦通道。对于掺有沸石的膜,获得的异丙醇渗透的活化能值明显低于水的渗透值,这表明掺有沸石的膜对异丙醇具有更高的选择性。 EP和ED值分别在21.81和31.12kJ / mol之间和15.27和41.49kJ / mol之间。所有掺有沸石的膜均表现出正的吸附热值,这表明吸附热主要由亨利的吸附模式决定。 (c)2005年Wiley Periodicals,Inc.

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