渗透汽化
大孔隙
膜
材料科学
涂层
化学工程
色谱法
高分子化学
复合材料
化学
有机化学
渗透
催化作用
介孔材料
工程类
生物化学
作者
Chengye Zuo,Xue Wang,Xiaobin Ding,Zhaoxiang Zhong,Wanqin Jin,Weihong Xing
标识
DOI:10.1016/j.memsci.2024.122908
摘要
High-performance polydimethylsiloxane (PDMS)/ceramic tubular pervaporation membranes have potential in industrial separation applications, but realizing the preparation of PDMS layer on the ceramic supports with micrometer-scale pore size (0.8 μm or 4.3 μm) for improving performance remains a challenge. We report a strategy (combined dip-coating and rotate-drying, DCRD) to preparation of PDMS on silicon carbide (SiC) tubular support with macropore. Response surface methodology was employed to optimize the dip-coating process, and the influence of friction velocity on tubular composite membranes was investigated. The results indicate that pulling speed, casting solution viscosity, and their interaction have significant effects on the pervaporation performance of PDMS/SiC tubular composite membranes. Moreover, increasing friction velocity results in uneven PDMS layer thickness, which in turn impacts the pervaporation performance of the composite membrane. Furthermore, the rigid structure of SiC restricts the movement of PDMS polymer chains, enabling the composite membrane to maintain stable pervaporation performance at higher isobutanol feed concentrations (3 wt%) or elevated feed temperatures (60 °C). After continuous operation for 200 hours, the developed PDMS/SiC tubular composite membrane consistently maintained the total flux of 650 g·m-2·h-1 and the separation factor of 39 for isobutanol/water. Eventually, this novel fabrication method offers new insights into the preparation of various other organic-inorganic tubular composite membranes.
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