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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
来源:
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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