A scalable dual-layer PAN/SAN nanofibrous membrane for treatment of saline oily water using membrane distillation

被引:10
作者
Niknejad, Ali Sallakh [1 ,4 ]
Kargari, Ali [2 ]
Namdari, Mahsa [3 ]
Pishnamazi, Mohammad [1 ]
Barani, Masoud [4 ]
Ranjbari, Esmaeil [4 ]
Sallakhniknezhad, Reza [5 ]
Bazgir, Saeed [4 ,6 ]
Rasouli, Mohsen [7 ]
McAvoy, Drew [1 ]
机构
[1] Univ Cincinnati, Dept Chem & Environm Engn, Cincinnati, OH USA
[2] Amirkabir Univ Technol, Dept Chem Engn, Membrane Proc Res Lab MPRL, Tehran, Iran
[3] Amirkabir Univ Technol, Dept Chem Engn, Tehran, Iran
[4] Islamic Azad Univ, Sci & Res Branch, Nano Polymer Res Lab NPRL, Tehran, Iran
[5] Beijing Inst Technol, Sch Mech Engn, Beijing, Peoples R China
[6] Islamic Azad Univ, Petr & Chem Engn Fac, Dept Polymer Engn, Sci & Res Branch, Tehran, Iran
[7] Amirkabir Univ Technol, Cent Lab, SEM Lab, Tehran, Iran
关键词
Hydrophilicity; Underwater superoleophobicity; Hot-pressing; Dual-layer; DCMD; FOULING RESISTANCE; COMPOSITE MEMBRANE; WASTE-WATER; SURFACE MODIFICATION; JANUS MEMBRANE; ELECTROSPUN; DESALINATION; WETTABILITY; SOLVENT; DESIGN;
D O I
10.1016/j.desal.2023.116895
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Single-layer hydrophobic membranes are prone to fouling while subjected to a feed containing hydrophobic contaminants. In this study, using the green solvent Dimethyl sulfoxide (DMSO), dual-layer nanofibrous polyacrylonitrile (PAN)/styrene-acrylonitrile (SAN) membranes were fabricated using the highly productive electroblowing process. Then through a simple hot-pressing process, the desirable hydrophilicity was achieved for PAN/SAN membrane. The water contact angle (WCA) for the top layer fell from 112.2 +/- 1(circle) to 37.5 +/- 1(circle) after hot-pressing, while the WCA for the bottom layer decreased slightly from 147.1 +/- 1(circle) to 142.3 +/- 1(circle) .Moreover, an underwater oil contact angle (UOCA) of 158.1 +/- 1(circle) was achieved for the PAN/SAN membrane. Direct contact membrane distillation (DCMD) tests were performed for synthetic saline water and synthetic saline oily water. While the permeate flux dropped for the single-layer SAN membrane, the dual-layer PAN/SAN membrane, due to underwater superoleophobicity, achieved a stable permeate flux for 24 h with a nearly complete salt rejection (> 99.9 %). This study addresses the pore wetting and declines in the permeate flux of the membrane distillation (MD) application in the treatment of saline oily water by implementing scalable, cost-efficient, and eco-friendly approaches.
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页数:9
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