Continuous-flow titration of low iron doses to promote photo-Fenton and photo-Fenton-like processes at neutral pH

[Display omitted] •Continuous titration of low [Fe2+] with no additional chemicals for PF at mild pH.•S2O82− a promising alternative oxidant to H2O2 for PF-like treatment at neutral pH.•Higher residual [Fe2+] and [TDI] and lower PO43− precipitation when using S2O82−.•Short-chain perfluorinated compo...

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Published inChemical engineering journal (Lausanne, Switzerland : 1996) Vol. 476; p. 146655
Main Authors Santos, Carla, Herraiz-Carboné, Miguel, Lacasa, Engracia, Sáez, Cristina, Montes, Rosa, Benito Quintana, José, Rodil, Rosario, Gomes, Ana I., Vilar, Vítor J.P.
Format Journal Article
LanguageEnglish
Published Elsevier B.V 15.11.2023
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Summary:[Display omitted] •Continuous titration of low [Fe2+] with no additional chemicals for PF at mild pH.•S2O82− a promising alternative oxidant to H2O2 for PF-like treatment at neutral pH.•Higher residual [Fe2+] and [TDI] and lower PO43− precipitation when using S2O82−.•Short-chain perfluorinated compounds HFBA, PFBS, and TFMS were not oxidized. Photo-Fenton (PF) is a promising process for degrading a wide range of contaminants of emerging concern (CECs) present in urban wastewater (UWW) after secondary treatment, mitigating their spread in aquatic systems. However, the near-neutral pH of UWW poses a challenge to PF performance. In this research, a tubular membrane photoreactor, designed for continuous “titration” of Fe2+, is explored to promote the PF process for the tertiary treatment of UWW. The application of persulfate (PF-like) as an alternative oxidant and the impact of phosphate (PO43−) content in UWW were also assessed. Process efficiency was evaluated in continuous mode, applying low residence times (RT: 6.1, 36.6, and 73.2 s) and low Fe2+ doses (1, 2, and 5 mg L−1), for the oxidation of 19 CECs (each spiked at 10 µg/L), in demineralized water (DW) and secondary-treated UWW. Despite the persistence of certain short-chain perfluoroalkyl substances (PFAS) and saccharine across all conditions tested, the PF-like process exhibited superior performance when compared with PF, attaining higher removals for most target CECs, especially for melamine. In UWW, for an RT = 73.2 s, [Fe2+] = 5 mg L−1, and [oxidant] = 1.2 mM, PF process removed 7 CECs > 60 % and PF-like 10 CECs > 60 %. Moreover, higher residual concentrations of Fe2+ and lower precipitation of PO43− were observed for PF-like treatments, evidencing its advantages for tertiary treatment. These results emphasize the importance of photoreactor design to achieve efficient PF/PF-like at neutral pH, avoiding the use of chelating agents while managing iron concentrations compatible with UWW discharge or reuse limits.
ISSN:1385-8947
1873-3212
DOI:10.1016/j.cej.2023.146655