Journal
ENVIRONMENTAL SCIENCE & TECHNOLOGY
Volume 53, Issue 24, Pages 14528-14537Publisher
AMER CHEMICAL SOC
DOI: 10.1021/acs.est.9b04148
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Funding
- U.S. Department of Defense [ER-2717, ER-1320]
- China Scholar Council
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This study investigated the degradation of perfluorooctanesulfonate (PFOS) in a reactive electrochemical membrane (REM) system in which a porous Magneli phase titanium suboxide ceramic membrane served simultaneously as the anode and the membrane. Near complete removal (98.30 +/- 0.51%) of PFOS was achieved under a cross-flow filtration mode at the anodic potential of 3.15 V vs standard hydrogen electrode (SHE). PFOS removal efficiency during the REM operation is much greater than that of the batch operation mode under the same anodic potential. A systematic reaction rate analysis in combination with electrochemical characterizations quantitatively elucidated the enhancement of PFOS removal in REM operation in relation to the increased electroactive surface area and improved interphase mass transfer. PFOS appeared to undergo rapid mineralization to CO2 and F-, with only trace levels of short-chain perfluorocarboxylic acids (PFCAs, C-4-C-8) identified as intermediate products. Density functional theory (DFT) simulations and experiments involving free radical scavengers indicated that PFOS degradation was initiated by direct electron transfer (DET) on anode to yield PFOS free radicals (PFOS center dot), which further react with hydroxyl radicals that were generated by water oxidation and adsorbed on the anode surface ((OHads)-O-center dot). The attack of (OHads)-O-center dot is essential to PFOS degradation, because, otherwise, PFOS center dot may react with water and revert to PFOS.
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