Superhydrophilic and underwater superoleophobic ceramic membranes grafted by layered polydopamine and polydopamine encapsulated silica particles for efficient separation of oil-in-water emulsions

超亲水性 材料科学 陶瓷 化学工程 水下 润湿 复合材料 化学 工程类 地质学 生物化学 海洋学
作者
Jamilu Usman,Nadeem Baig,Isam H. Aljundi
出处
期刊:Journal of environmental chemical engineering [Elsevier]
卷期号:11 (3): 110011-110011 被引量:39
标识
DOI:10.1016/j.jece.2023.110011
摘要

Owing to frequent oil spills and the increasing discharge of oily wastewater, oil pollution has threatened the sustainability of the ecosystem. Ceramic membranes (CM) have been employed for oily wastewater treatment because of their mechanical and chemical stability, but a suitable separating layer is required to treat surfactant-stabilized oil-in-water emulsions effectively. Herein, a separating layer was rationally designed on the CM surface by combining cross-linked layered polydopamine (CL-LPDA) and polydopamine-encapsulated silica particles (SiO 2 @PDA) with appropriate permeation flux and antifouling characteristics. The resulting CL-LPDA-SiO 2 @PDA-CM demonstrated superhydrophilicity with a water contact angle of 0° and underwater superoleophobicity with an underwater oil contact angle of 157°, making it an ideal membrane for separating oil-in-water emulsions. The designed membrane could treat a surfactant-stabilized oil-in-water emulsion with a maximum separation efficiency of 97 % and a permeation flux of 109.76 L m −2 h −1 . The CL-LPDA-SiO 2 @PDA-CM has also shown significant resistance to fouling under 20 cycles of observation, and the flux recovery ratio (FRR) was higher than 90 %, indicating that pore-clogging could be effectively prevented in the separating layer. • A unique separating layer designed by crosslinking the layered PDA and PDA-coated silica particles (CL-LPDA-SiO 2 @PDA). • CL-LPDA-SiO 2 @PDA-CM demonstrated an underwater oil contact angle of 157.3°. • The designed membrane demonstrated a separation efficiency of 97 %. • The maximum permeation flux of 109.76 L m −2 h −1 was observed with the modified membrane. • The flux recovery ratio of the designed membrane was higher than 90 %.
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