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Fouling-resistant Composite Membranes for Separation of Oil-in-water Microemulsions

机译:分离水包油型微乳液的耐污垢复合膜

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摘要

Fouling-resistant ceramic-supported polymer composite membranes were developed for removal of oil-in-water (O/W) microemulsions. The composite membranes were featured with an asymmetric three-layer structure, i.e., a porous ceramic membrane substrate, a polyvinylidene fluoride (PVDF) ultrafiltration sub-layer, and a polyam-ide/polyvinyl alcohol (PVA) composite thin top-layer. The PVDF polymer was cast onto the tubular porous ceramic membranes with an immersion precipitation method, and the polyamide/PVA composite thin top-layer was fabricated with an interfacial polymerization method. The effects of the sub-layer composition and the recipe in the interfacial polymerization for fabricating the top-layer on the structure and performance of composite membranes were systematically investigated. The prepared composite membranes showed a good performance for treating the O/W microemulsions with a mean diameter of about 2.4um. At the operating pressure of 0.4MPa, the hydraulic permeability remained steadily about 190L·m~(-2)·h~(-1), the oil concentration in the permeate was less than 1.6mg·L~(-1) and the oil rejection coefficient was always higher than 98.5% throughout the operation from the beginning.
机译:开发了用于去除水包油(O / W)微乳状液的耐污陶瓷载体聚合物复合膜。复合膜的特征在于具有不对称的三层结构,即多孔陶瓷膜基底,聚偏二氟乙烯(PVDF)超滤子层和聚酰胺-聚乙烯醇(PVA)复合薄顶层。使用浸没沉淀法将PVDF聚合物浇铸到管状多孔陶瓷膜上,并通过界面聚合法制备聚酰胺/ PVA复合薄顶层。系统地研究了子层组成和配方在制备顶层的界面聚合反应中对复合膜结构和性能的影响。制备的复合膜在处理O / W微乳液中表现出良好的性能,平均直径约为2.4um。在0.4MPa的工作压力下,导水率稳定保持在190L·m〜(-2)·h〜(-1)左右,渗透液中的油浓度小于1.6mg·L〜(-1),从一开始就在整个操作过程中,排油系数始终高于98.5%。

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