The integration of ZVI-dehalogenation and electrochemical oxidation for the treatment of complex effluents polluted with iodinated compounds

This work evaluates the integration of dehalogenation with Zero Valent Iron (ZVI) and electrochemical oxidation (EO) for the treatment of urines polluted with iodinated X-ray contrast media (ICM). To do this, different strategies were evaluated: pretreatment with ZVI followed by EO (ZVI-EO) or elect...

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Main Authors: Cañizares, P. (Author), Correia, S.E (Author), Cotillas, S. (Author), Lacasa, E. (Author), Moratalla, Á (Author), Rodrigo, M.A (Author), Sáez, C. (Author)
Format: Article
Language:English
Published: Elsevier Ltd 2022
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Online Access:View Fulltext in Publisher
LEADER 03119nam a2200469Ia 4500
001 10.1016-j.jece.2022.107587
008 220510s2022 CNT 000 0 und d
020 |a 22133437 (ISSN) 
245 1 0 |a The integration of ZVI-dehalogenation and electrochemical oxidation for the treatment of complex effluents polluted with iodinated compounds 
260 0 |b Elsevier Ltd  |c 2022 
856 |z View Fulltext in Publisher  |u https://doi.org/10.1016/j.jece.2022.107587 
520 3 |a This work evaluates the integration of dehalogenation with Zero Valent Iron (ZVI) and electrochemical oxidation (EO) for the treatment of urines polluted with iodinated X-ray contrast media (ICM). To do this, different strategies were evaluated: pretreatment with ZVI followed by EO (ZVI-EO) or electrolysis enhanced with ZVI-dehalogenation (EO/ZVI). For comparison purposes, single electrolysis was also performed to check the best treatment strategy. Results showed that EO was less efficient than EO/ZVI and ZVI-EO processes. Removal percentages of 74.9%, 87.6% and 99.5% were reached after passing 13.8 Ah dm−3 at 10 mA cm−2 during EO, EO/ZVI and ZVI-EO, respectively. EO/ZVI process favored the production of large amounts of hydroxyl radicals in the effluent through Fenton´s reaction, enhancing the degradation rate of iopamidol (IPM). The pretreatment with ZVI allowed to transform up to 95% of IPM to C17H25N3O8. Then, electrolysis attained the almost complete removal of the raw pollutant (ZVI-EO). The different iodine species formed at the end of the treatment were also monitored, finding similar proportions of organic iodine species for EO and EO/ZVI processes, although single EO promoted the formation of the stable inorganic iodine (IO3-) and EO/ZVI favored the release of I-. Total organic carbon removal percentages lower than 20% were achieved, suggesting that the technologies employed were selective for the removal of the target pollutant under the operating conditions studied. Finally, the organic IPM by-products were also identified by LC-MS and the chromatographic area profiles showed higher values for EO/ZVI followed by ZVI-EO and EO. © 2022 The Authors 
650 0 4 |a Degradation 
650 0 4 |a Degradation rate 
650 0 4 |a Effluents 
650 0 4 |a Electrochemical oxidation 
650 0 4 |a Electrolysis 
650 0 4 |a Electrolysis 
650 0 4 |a Hydroxyl radicals 
650 0 4 |a Iodinated X-ray contrast media 
650 0 4 |a Iodine 
650 0 4 |a Iodine species 
650 0 4 |a Iopamidol 
650 0 4 |a Iopamidol 
650 0 4 |a Iron 
650 0 4 |a Large amounts 
650 0 4 |a Organic carbon 
650 0 4 |a Oxidation process 
650 0 4 |a Pollution 
650 0 4 |a Pre-treatments 
650 0 4 |a Urine 
650 0 4 |a Urine 
650 0 4 |a Zero valent iron 
650 0 4 |a Zero-valent iron 
700 1 |a Cañizares, P.  |e author 
700 1 |a Correia, S.E.  |e author 
700 1 |a Cotillas, S.  |e author 
700 1 |a Lacasa, E.  |e author 
700 1 |a Moratalla, Á.  |e author 
700 1 |a Rodrigo, M.A.  |e author 
700 1 |a Sáez, C.  |e author 
773 |t Journal of Environmental Chemical Engineering