2018
DOI: 10.1016/j.watres.2018.04.044
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Autocatalytic degradation of perfluorooctanoic acid in a permanganate-ultrasonic system

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Cited by 53 publications
(14 citation statements)
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“…Table S6 shows that the G 50 value of the NPDW/MBs−air system was 2.4−3.5 times that of some photocatalysis system 66−68 and ∼3.3 times those of a microwave system 69 and an ultrasonic electrochemical system, 70 indicating that NPDW/MBs treatment is superior to some of the alternative techniques. The energy consumption (EE/O) of these systems also supports the conclusion, with the EE/O of NPDW/MBs (331.95 kWh/m 3 in the air atmosphere and 216.49 kWh/m 3 in the Ar atmosphere) lower than those of photocatalysis (2666.7 kWh/m 3 ), 67 microwave (3584.0 kWh/ m 3 ), 69 permanganate-ultrasonic (531.69 kWh/m 3 ), 71 and ultrasonic electrochemical (3678.2 kWh/m 3 ) systems. 70 Among the different plasma systems, the G 50 values of the NPDW/MBs in the air and Ar atmospheres are 4.5 and 2.2 times higher than DC plasma in O 2 bubbles 72 and Ar bubbles, 27 respectively, while the EE/O are only 0.16 and 0.30 times that of the latter.…”
Section: ■ Results and Discussionsupporting
confidence: 69%
“…Table S6 shows that the G 50 value of the NPDW/MBs−air system was 2.4−3.5 times that of some photocatalysis system 66−68 and ∼3.3 times those of a microwave system 69 and an ultrasonic electrochemical system, 70 indicating that NPDW/MBs treatment is superior to some of the alternative techniques. The energy consumption (EE/O) of these systems also supports the conclusion, with the EE/O of NPDW/MBs (331.95 kWh/m 3 in the air atmosphere and 216.49 kWh/m 3 in the Ar atmosphere) lower than those of photocatalysis (2666.7 kWh/m 3 ), 67 microwave (3584.0 kWh/ m 3 ), 69 permanganate-ultrasonic (531.69 kWh/m 3 ), 71 and ultrasonic electrochemical (3678.2 kWh/m 3 ) systems. 70 Among the different plasma systems, the G 50 values of the NPDW/MBs in the air and Ar atmospheres are 4.5 and 2.2 times higher than DC plasma in O 2 bubbles 72 and Ar bubbles, 27 respectively, while the EE/O are only 0.16 and 0.30 times that of the latter.…”
Section: ■ Results and Discussionsupporting
confidence: 69%
“…This energy consumption is among the lowest reported in the literature (prior electrochemical [10–1500 kWh mol −1 F − ], microwave [4200 kWh mol −1 F − ], UV [450–2000 kWh mol −1 F − ], and ultrasonic [250–4200 kWh mol −1 F − ]). [ 20b,21 ] The significantly lower energy consumption can be attributed to the high defluorination efficiency, combined with the tuning of redox‐potential through the P(TMA 51 ‐ co ‐TMPMA 49 )‐CNT electrode. Our consideration in the energy aspect demonstrates the possibility of using P(TMA x ‐ co ‐TMPMA 1− x )‐CNT as not only a cost‐effective electrochemically‐mediated adsorbent, but also a sustainable counter electrode enabling energy‐efficient, tandem degradation of PFOA, providing a unique pathway for next‐generation, energy‐integrated water purification devices.…”
Section: Resultsmentioning
confidence: 99%
“…Some advanced oxidation processes (AOPs) in critical conditions have been developed to degrade PFOA. The noticeable treatment technologies are either photo-based approaches, such as: photolysis, photochemical and photocatalysis [7][8][9][10][11] sonochemical treatment [12][13][14][15] or microwavehydrothermal treatment [16][17]. The key factor in these treatment reactions are one-electron oxidants such as persulfate [8][9][10][11][12][13][14][15][16] periodate [10], or photocatalysts such as heteropolyacid [7], TiO2 [9,11], have been used to decompose PFCAs under UV-irradiation.…”
Section: Introductionmentioning
confidence: 99%