2021
DOI: 10.1016/j.jhazmat.2020.124548
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Enhancement of UV disinfection of urine matrixes by electrochemical oxidation

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Cited by 28 publications
(17 citation statements)
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“…Free and combined chlorine species are expected to be generated from the oxidation of chlorides contained in urine and the subsequent reaction with ammonium [23]. In addition, the MIKROZON® cell used in this work is specially designed for the electrochemical production of ozone during the electrolysis which can also contribute to the disinfection process [14,15].…”
Section: Resultsmentioning
confidence: 99%
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“…Free and combined chlorine species are expected to be generated from the oxidation of chlorides contained in urine and the subsequent reaction with ammonium [23]. In addition, the MIKROZON® cell used in this work is specially designed for the electrochemical production of ozone during the electrolysis which can also contribute to the disinfection process [14,15].…”
Section: Resultsmentioning
confidence: 99%
“…Likewise, the experimental data were fitted to a first order kinetics model [23] and the resulting rate constants for urine (kU) and urine without chlorides (kUWC) were also compared throughout the ratio kU/kUWC. Values higher than 1 indicate that the disinfection process is more efficient by the combination of electrogenerated chlorine and ozone disinfectants whereas ratios lower than 1 suggest a more contribution of ozone on the disinfection process.…”
Section: Resultsmentioning
confidence: 99%
“…( Herraiz-Carboné et al., 2020b ) reported that the electric energy consumption for UV assisted electrochemical oxidation using a BDD anode at the high applied current density of 50 A m −2 , is slightly higher than that required for the UV disinfection process (0.395 vs . 0.389 kWh m −3 order −1 ).…”
Section: Economic Aspects and Scale-up Of The Photo-assisted Eaopsmentioning
confidence: 99%
“…In terms of energy requirements for pathogen inactivation promoted by EAOPs, the specific electric energy (E EO ) in kWh m −3 order −1 , can be calculated using Eq. (36) , where E is the cell voltage (V), W lamp the power of the lamp (kW), I the current intensity (kA), t the operation time (h), V the volume (m 3 ) and C 0 and C f the initial and final pathogen concentration after 1 order of magnitude removal (CFU mL −1 ), respectively ( Herraiz-Carboné et al., 2020b ). …”
Section: Economic Aspects and Scale-up Of The Photo-assisted Eaopsmentioning
confidence: 99%
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