4.7 Article

A comparison study of heat-assisted Fe2+/persulfate and powdered activated carbon/persulfate wastewater pre-treatment for membrane fouling alleviation

Journal

JOURNAL OF CLEANER PRODUCTION
Volume 406, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.jclepro.2023.137127

Keywords

Aerobic granular sludge; Membrane fouling; Pretreatment; Heat activation; Persulfate

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The study compared the effects of heat/Fe2+/persulfate (PS) and heat/powdered activated carbon (PAC)/PS systems on membrane fouling mitigation. It was found that heat/Fe2+/PS showed better control of membrane fouling by generating sulfate radicals and Fe3+. Heat/PAC/PS, on the other hand, mitigated fouling through a non-radical effect and efficiently removed COD and suspended solids.
Heat/Fe2+/persulfate (PS) and heat/powdered activated carbon (PAC)/PS exhibit oxidation, coagulation, and adsorption effects, respectively. However, no studies have been conducted to discuss and compare the synergistic contribution to membrane fouling mitigation under thermal synergy. Herein, heat/Fe2+/PS and heat/PAC/PS systems were used to alleviate membrane fouling during municipal wastewater recycling in an aerobic granular sludge membrane bioreactor (AGMBR), and the effects of oxidation, coagulation, and adsorption on the mem-brane fouling mitigation were analyzed. The results showed that heat/Fe2+/PS and heat/PAC/PS effectively increased the filtration flux, decreased the fouling resistance, and maintained the membrane surface morphology. Compared to heat/PAC/PS, the heat/Fe2+/PS exhibited better control of membrane fouling owing to the generation of sulfate radicals and Fe3+. The non-radical effect is an important way to mitigate membrane fouling by heat/PAC/PS. Moreover, the pretreatment systems were effective in decomposition and removal of large-particle-size pollutants owing to their excellent oxidation capacity. According to the extended Derja-guin-Landau-Verwey-Overbeek theory, the heat/Fe2+/PS system had the higher energy barrier values of fou-lant-membrane (155.31 kT) and foulant-foulant (113.75 kT). The cake filtration and intermediate blocking models were the major mechanisms of membrane fouling, and efficient removal of chemical oxygen demand (R2>0.93) and suspended solids (R2>0.92) were beneficial to the membrane fouling mitigation. This study elucidates the differences in the mechanisms of heat/Fe2+/PS and heat/PAC/PS in mitigating AGMBR membrane fouling.

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