2019
DOI: 10.1080/10643389.2018.1542916
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Physico-Chemical Processes for the Treatment of Per- And Polyfluoroalkyl Substances (PFAS): A review

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Cited by 187 publications
(149 citation statements)
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“…Most mechanisms support the hypothesis of the sulfonate group being cleaved first instead of shorter chain sulfonates being formed (Franke, Schafers, Lindberg, & Ahrens, 2019). The degradation pathway using the hydrated electron approach involves a reductive process resulting in defluorination before the formation of shorter chain intermediates that retain the terminal SO 3 − group (Bentel et al, 2019; Nzeribe et al, 2019).…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…Most mechanisms support the hypothesis of the sulfonate group being cleaved first instead of shorter chain sulfonates being formed (Franke, Schafers, Lindberg, & Ahrens, 2019). The degradation pathway using the hydrated electron approach involves a reductive process resulting in defluorination before the formation of shorter chain intermediates that retain the terminal SO 3 − group (Bentel et al, 2019; Nzeribe et al, 2019).…”
Section: Resultsmentioning
confidence: 99%
“…The most common technologies, at this point, for PFAS treatment in water involve sorption of the PFAS onto media such as activated carbon or ion exchange media resulting in a waste stream that requires further treatment such as incineration and/or thermal regeneration if treating above ground. Alternative technologies that destroy PFAS such as oxidative and reductive technologies are currently being investigated (Nzeribe, Crimi, Thagard, & Holsen, 2019; Wang et al, 2017). It is unclear whether the destructive technologies will be effective or economical in comparison to the sorption/incineration remedies.…”
Section: Introductionmentioning
confidence: 99%
“…The alternative approaches are emerging as more mobile options using small‐scale plants, which could be applied at sites where PFAS waste concentrates are generated. Based on numerous sources, an approximate range of energy demand per volume treated for plasma, electrochemical treatment, and sonolysis is 0.01 to 0.5‐kW h per liter (kW‐h/L; 0.04 to 1.9 kW‐h per gallon [kW‐h/gal]; e.g., Gomez‐Ruiz et al ; Soriano et al ; Kempisty et al ; Nzeribe et al ; Singh et al , ). However, approximating a range of energy demand for these relevant technologies is difficult to accurately summarize due to the variety of operating conditions within the respective studies when the energy demand was determined.…”
Section: Identifying the Destructive Technology “Strike Zone”mentioning
confidence: 99%
“…Residence times associated with PFAS destruction are believed to approximately range from 30 min to 8 h (e.g., Mader et al ; Mitchell et al ; Gomez‐Ruiz et al ; Bentel et al ; Nzeribe et al ; Singh et al , ). The broad range of residence times provided represents the different applications reported in the literature and varies according to the targeted destructive mechanism, the influent PFAS concentration, the geochemistry of the treated matrix, and the targeted degree of defluorination.…”
Section: Identifying the Destructive Technology “Strike Zone”mentioning
confidence: 99%
“…To lower the required energy amount, the use of catalytically active materials can be advisable [ 59 , 60 , 61 ]. The latest developments of advanced oxidation processes (AOPs), including chemical oxidation (e.g., persulfate oxidation, ozonation), photooxidation, electrochemical or thermal oxidation, have been recently reviewed by several authors [ 62 , 63 , 64 , 65 ]. In contrast to oxidative processes, reduction involves the direct transformation of electrons from a reducing agent with a lower reduction potential compared to the substrate.…”
Section: State-of-the-art Liquid Reactionsmentioning
confidence: 99%