Development of plasma and/or chemically induced graft co-polymerized electrospun poly(vinylidene fluoride) membranes for solute separation

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• 作者：Houman Savoji^a ; ^b ; ¹ ; Dipak Rana^a ; ^{rana@uottawa.ca} ; ^{rana@eng.uottawa.ca} ; Takeshi Matsuura^a ; Shahram Tabe^c ; Chaoyang Feng^a
• 关键词：Electrospun nanofibrous membranes ; Plasma and chemically induced graft copolymer ; Solute separation ; Tight micro-filtration membranes
• 刊名：Separation and Purification Technology
• 出版年：2013
• 出版时间：19 April, 2013
• 年：2013
• 卷：108
• 期：Complete
• 页码：196-204
• 全文大小：1208 K

文摘

Nanofiber membranes were fabricated by electrospinning poly(vinylidene fluoride). The electrospun nanofiber membranes were further modified by grafting of acrylic acid (AA) and methacrylic acid (MAA) over the surfaces of the membranes. Plasma AA graft was attempted only, and the results indicated the partial membrane pore filling with grafted AA. For MAA grafting, chemically induced polymerization using benzoyl peroxide and hydrogen peroxide was attempted. The combination of plasma and chemically induced MAA graft polymerization was also attempted. The membranes were characterized by scanning electron microscopy (SEM), X-ray photoelectron spectroscopy (XPS) and static contact angle (SCA) measurement. SEM surface analysis indicated partial pore narrowing of grafted membranes. The average pore size was reduced from 0.97 ¦Ìm for the untreated membrane to 0.15 ¦Ìm for the two step plasma and chemically induced grafted membranes. XPS analysis confirmed that grafting has taken place on the top surface of the membranes. The surfaces of the grafted membrane were significantly hydrophilic as observed by SCA. It was also found that the combination of plasma and chemically induced grafting using hydrogen peroxide was the most effective in terms of flux and selectivity. The grafting reduced the pore size by filling the pores of the original membranes by the graft polymers. This practice resulted in producing tight micro-filtration (MF) membranes from loose MF ones. An impressive high water flux of 150 kg/h m² at an operating pressure of 4 psig, and a 79 % removal of polyethylene oxide (molecular weight 400 kilo-Daltons) were achieved.