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Treating oily wastewater by porous ceramic membranes derived from solid waste is of great significance. In the present work, porous ceramic membranes were fabricated using the dry-pressing and solid-state sintering method with red mud as the primary raw material and polymethyl methacrylate (PMMA) microspheres as pore-forming agents. The obtained membrane with a PMMA percentage of 35 % in the green body and sintering at 1100 °C (PCM35) possesses an open porosity of 57.22 %, a most probable pore size of 0.38 μm, an average pore size of 0.64 μm, and a flexural strength of 5.130 MPa, exhibiting amphiphilicity in air with the contact angle decreasing finally to 0° in 1.52 s for water and in 69.0 s for oil, and underwater oleophobicity with an oil contact angle of 148.9 ± 9.4°. The membrane was used for the separation of simulated oil-in-water emulsion. The separation performance depends on the oil concentration, the pH of the emulsion, and the transmembrane pressure. Membrane fouling occurs during the separation process, where four models, namely, complete blocking, intermediate blocking, standard blocking, and cake formation, are all involved in the fouling within 60 min. However, if the separation time is extended to 120 min, only the cake formation model will control the fouling. The membrane exhibits desirable long-term stability in separating the emulsion with an oil concentration of 500 ppm and a pH of 7 under a transmembrane pressure of 0.3 bar. The steady permeate fluxes remain relatively stable at approximate 131.4 L/(m2·h·bar), and the oil rejections exceed 95.8 % (higher than 99 % in the vast majority of cases) during the recycling process(totally for 25 cycles, 3000 min). The membrane was further adopted for real wastewater (with a high oil concentration of 21.5 g/L) treatment. The results show that the membrane can intercept most oil droplets within the wastewater with an oil rejection as high as 80.7 %, and with a steady permeate flux of 15.3 L/(m2·h·bar). Although the oil–water separation performance in this work is inferior to some of those reported previously, our ceramic membranes are highly competitive since they provide a promising strategy for comprehensively utilizing red mud. © 2025 Elsevier B.V.
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Separation and Purification Technology
ISSN: 1383-5866
Year: 2025
Volume: 364
8 . 6 0 0
JCR@2022
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ESI Highly Cited Papers on the List: 0 Unfold All
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30 Days PV: 11
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