电纺纳米纤维负载正渗透脱盐薄膜复合膜的制备

Q2 Engineering
M. Al-Furaiji, M. Kadhom, Khairi R. Kalash, B. Waisi, N. Albayati
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引用次数: 19

摘要

摘要就能耗和经济运行而言,与反渗透等传统工艺相比,正渗透(FO)工艺被认为是一种可行的海水淡化选择。本工作采用静电纺丝工艺制备了聚丙烯腈(PAN)纳米纤维支撑层。然后,在间苯二胺(MPD)和三聚氯(TMC)之间进行界面聚合反应,在支撑层上制备聚酰胺选择性薄膜复合材料(TFC)膜。使用标准方法在FO模式(面向活性层的进料溶液)下测试TFC膜,并将其与市售的纤维素三乙酸酯膜(CTA)进行比较。合成的膜在水通量方面表现出高性能(16 Lm  −2. h−1),但交易了拒盐(4 gm−2 h−1)与商用CTA膜(水通量  =  13 Lm−2 h−1和排盐  =  3. gm−2 h−1)。通过扫描电子显微镜(SEM)、接触角、力学性能、孔隙率和性能表征对膜进行了检测。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Preparation of thin-film composite membranes supported with electrospun nanofibers for desalination by forward osmosis
Abstract. The forward osmosis (FO) process has been considered to be a viable option for water desalination in comparison to the traditional processes like reverse osmosis, regarding energy consumption and economical operation. In this work, a polyacrylonitrile (PAN) nanofiber support layer was prepared using the electrospinning process as a modern method. Then, an interfacial polymerization reaction between m -phenylenediamine (MPD) and trimesoyl chloride (TMC) was carried out to generate a polyamide selective thin-film composite (TFC) membrane on the support layer. The TFC membrane was tested in FO mode (feed solution facing the active layer) using the standard methodology and compared to a commercially available cellulose triacetate membrane (CTA). The synthesized membrane showed a high performance in terms of water flux (16 Lm  −2  h −1 ) but traded the salt rejection (4 gm −2  h −1 ) compared with the commercial CTA membrane (water flux  =  13 Lm −2  h −1 and salt rejection  =  3 gm −2  h −1 ) at no applied pressure and room temperature. Scanning electron microscopy (SEM), contact angle, mechanical properties, porosity, and performance characterizations were conducted to examine the membrane.
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来源期刊
Drinking Water Engineering and Science
Drinking Water Engineering and Science Environmental Science-Water Science and Technology
CiteScore
3.90
自引率
0.00%
发文量
3
审稿时长
40 weeks
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