Feasible synthesis of anti-fouling amphiphobic composite membrane by surface modification with SiO2 nanoparticles for effective membrane distillation

被引:0
|
作者
Zhou, Weiran [1 ,2 ]
Geng, Yuchen [1 ,2 ]
Zhou, Tao [3 ]
Wang, Yu [1 ,2 ]
Zhao, Huazhang [2 ]
Wu, Xiaohui [3 ]
Li, Jianfeng [1 ,2 ]
机构
[1] Shanxi Univ, Inst Resources & Environm Engn, Shanxi Lab Yellow River, Taiyuan 030006, Peoples R China
[2] Shanxi Univ, Coll Environm & Resource Sci, China Shanxi Lab Yellow River, Taiyuan 030006, Peoples R China
[3] Huazhong Univ Sci & Technol, Sch Environm Sci & Engn, Hubei Key Lab Multimedia Pollut Cooperat Control Y, Wuhan 430074, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
Membrane distillation; Amphiphobic membrane; Non fluorination; Saline wastewaters; SiO2; nanoparticles; COKING WASTE-WATER; GAS PRODUCED WATER; PVDF MEMBRANE; SUPERHYDROPHOBIC SURFACE; FLUORINE-FREE; HIGH-FLUX; PERFORMANCE; REMOVAL; DESALINATION; PRETREATMENT;
D O I
10.1016/j.seppur.2024.130366
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Membrane distillation (MD) technology has shown unique advantages in treating saline organic wastewaters, however, improving membrane materials of anti-wetting/fouling properties is still agap for the large-scale application. In this study, a non-fluorinated composite membrane showing both good amphiphobic properties and high flux was synthesized by feasible electrostatic attraction. Characterizations indicated that SiO2nano- particles were successfully loaded on the PVDF membrane (SiO2/PVDF) surface to form a multi-level rough amphiphobic structure, with contact angles of water and ethylene glycol as 139 degrees and 128 degrees, respectively. In MD tests, the SiO2/PVDF membrane exhibited a stable flux of 15 LMH with 3.5 wt% NaCl and 19.5 LMH with 50 mg/ L kerosene. Notably, after a 24-hour continuous test, the flux remained above 9 LMH for NaCl and 11 LMH for kerosene, with salt rejection rates exceeding 98 %, indicating excellent anti-fouling characteristics. This study is expected to provide a feasible membrane modification for MD process in treating high saline organic wastewater.
引用
收藏
页数:9
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