2019
DOI: 10.1016/j.jhazmat.2019.02.005
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Simultaneous removal of tetracycline and disinfection by a flow-through electro-peroxone process for reclamation from municipal secondary effluent

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Cited by 53 publications
(11 citation statements)
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“…The energy consumption for the electrochemical oxidation of TC was 0.25 kWh m −3 at an optimal applied voltage of −2.5 V with a corresponding current of 0.002 A at pH 6.7. This was competitive with state-of-the-art electrochemical processes, which use 0.1−40 kWh m −3 , 49 and even advanced oxidation processes (AOPs) such as electrolysis with O 3 (0.47 kWh m −3 for TC), 50 photo-Fenton using UV/ pre-Fe 0 /H 2 O 2 (1.22 kWh m −3 for TC), 51 and electro-Fenton with FeOCl (0.336 kWh m −3 for TC). 52 It is noted that these results were obtained under different operational conditions, which may influence the apparent power consumption levels, and further investigation is essential to calculate accurately the energy consumption of these processes.…”
mentioning
confidence: 99%
“…The energy consumption for the electrochemical oxidation of TC was 0.25 kWh m −3 at an optimal applied voltage of −2.5 V with a corresponding current of 0.002 A at pH 6.7. This was competitive with state-of-the-art electrochemical processes, which use 0.1−40 kWh m −3 , 49 and even advanced oxidation processes (AOPs) such as electrolysis with O 3 (0.47 kWh m −3 for TC), 50 photo-Fenton using UV/ pre-Fe 0 /H 2 O 2 (1.22 kWh m −3 for TC), 51 and electro-Fenton with FeOCl (0.336 kWh m −3 for TC). 52 It is noted that these results were obtained under different operational conditions, which may influence the apparent power consumption levels, and further investigation is essential to calculate accurately the energy consumption of these processes.…”
mentioning
confidence: 99%
“…This process was found also cost-effective and promising for simultaneous tetracycline removal and disinfection of municipal secondary effluents. The main disinfection by-products such as trihalomethanes, haloacetonitrile and halonitromethanes were particularly much lower than the WHO's thresholds for drinking water [432].…”
Section: Electro-peroxonementioning
confidence: 78%
“…The supernatant was taken at regular intervals after a certain reaction time and analysed to determine its COD and BOD 5 values, respectively, in order to observe the changes in B/C values before and after treatment. The mixture of oxygen and ozone (1 g/L) from the ozone generator was passed into the 250 mL petrochemical wastewater water sample [19]. Different intake air flows were used to oxidize petrochemical wastewater for a certain period of time in an environment of 25 • C. The COD and BOD 5 values were measured by taking samples regularly.…”
Section: Methodsmentioning
confidence: 99%