A self-cleaning thermocatalytic membrane for bisphenol a abatement and fouling removal

被引:2
作者
Ostergaard, Martin B. [1 ]
Egea-Corbacho, Agata [2 ]
Wang, Deyong [3 ]
Deganello, Francesca [4 ]
Boffa, Vittorio [1 ]
Jorgensen, Mads K. [1 ]
机构
[1] Aalborg Univ, Ctr Membrane Technol, Dept Chem & Biosci, DK-9220 Aalborg, Denmark
[2] Univ Cadiz, Dept Environm Technol, Fac Marine & Environm Sci, INMAR Marine Res Inst,CEIMAR Int Campus Excellence, Campus Univ Puerto Real, Puerto Real 11510, Cadiz, Spain
[3] Aalborg Univ, Dept Mat & Prod, DK-9220 Aalborg, Denmark
[4] Consiglio Nazl Ric CNR ISMN, Ist Studio Mat Nanostrutturati, Via Ugo La Malfa 153, I-90146 Palermo, Italy
关键词
Pore blocking; Advanced oxidation; Perovskites; Membrane cleaning; Microfiltration; Thermocatalytic membrane; PHOTOCATALYTIC DEGRADATION; WASTE-WATER; SUBSEQUENT REUSE; ULTRAFILTRATION; POLLUTANTS; KINETICS; LIGHT;
D O I
10.1016/j.memsci.2023.122336
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Thermocatalytic, ceramic microfiltration membranes for continuous micropollutants removal and simultaneous degradation of organic fouling were synthesized by integrating a Sr0.85Ce0.15FeO3 (SCF) perovskite in alumina membranes and tested for the bisphenol A (BPA) abatement under different experimental conditions. Scanning electron microscopy (SEM) and Energy Dispersive X-ray spectroscopy (EDX) characterization techniques were used to characterize the samples. The effect of water flux, BPA concentration and temperature on the BPA and fouling removal was investigated in detail. Up to 55 % of BPA was removed by filtration of a 9.6 mg L-1 BPA solution at 40 degrees C and a flux of 25 LMH. Degradation studies with BPA feed concentrations of 3.4, 5.5 and 9.6 mg L-1 showed higher degradation rate by the membrane with higher concentrations of BPA. Furthermore, the rate of BPA degradation increases with lower permeate flux, due to the longer retention time of pollutant in the membrane. Membranes were fouled with humic acid to study the thermocatalytic fouling removal. After fouling, membranes were rinsed to remove external, removable fouling, which was followed by 20-120 min of thermal treatment at 40 degrees C. This showed up to complete recovery of permeability by reduction of hydraulic resistance from the internal fouling in the membranes. No effect of heat treatment was observed for fouled nonfunctionalized membranes. Hence, the novel membrane studied in this article is a promising solution for simultaneous degradation of micropollutants and recovery of permeability during filtration, e.g. in wastewater treatment.
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页数:9
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