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               <dc:title>In-situ dosage of Fe2+ catalyst using natural pyrite for thiamphenicol mineralization by photoelectro-Fenton process</dc:title>
               <dc:creator>Thiam, Abdoulaye</dc:creator>
               <dc:creator>Salazar, Ricardo</dc:creator>
               <dc:creator>Brillas, Enric</dc:creator>
               <dc:creator>Ignés i Mullol, Jordi</dc:creator>
               <dc:subject>Antibiòtics</dc:subject>
               <dc:subject>Catàlisi</dc:subject>
               <dc:subject>Oxidació electroquímica</dc:subject>
               <dc:subject>Antibiotics</dc:subject>
               <dc:subject>Catalysis</dc:subject>
               <dc:subject>Electrolytic oxidation</dc:subject>
               <dc:description>The degradation of the antibiotic thiamphenicol has been studied by photoelectro-Fenton (PEF) process with UVA light using pyrite particles as catalyst source. Pyrite is a sulfide mineral that naturally acidifies the reaction medium and releases Fe2+, thus promoting the effective generation of ¿OH from Fenton's reaction. The assays were made in an IrO2/air-diffusion cell, which yielded similar results to a boron-doped diamond (BDD)/air-diffusion one at a lower cost. In dark conditions, electro-Fenton (EF) process showed an analogous ability for drug removal, but mineralization was much poorer because of the large persistence of highly stable by-products. Their photolysis explained the higher performance of PEF. Conventional homogeneous PEF directly using dissolved Fe2+ exhibited a lower mineralization power. This suggests the occurrence of heterogeneous Fenton's reaction over the pyrite surface. The effect of current density and drug content on pyrite-catalyzed PEF performance was examined. The drug heteroatoms were gradually converted into SO42-, Cl- and NO3- ions. Nine aromatic derivatives and two dichloroaliphatic amines were identified by GC-MS, and five short-chain carboxylic acids were detected by ion-exclusion HPLC. A reaction route for thiamphenicol mineralization by PEF process with continuous H2O2 and Fe2+ supply on site is proposed.</dc:description>
               <dc:date>2020-06-11T07:49:07Z</dc:date>
               <dc:date>2022-06-02T05:10:17Z</dc:date>
               <dc:date>2020-06-02</dc:date>
               <dc:date>2020-06-11T07:49:07Z</dc:date>
               <dc:type>info:eu-repo/semantics/article</dc:type>
               <dc:type>info:eu-repo/semantics/acceptedVersion</dc:type>
               <dc:relation>Versió postprint del document publicat a: https://doi.org/10.1016/j.jenvman.2020.110835</dc:relation>
               <dc:relation>Journal of Environmental Management, 2020, vol. 270, p. 110835</dc:relation>
               <dc:relation>https://doi.org/10.1016/j.jenvman.2020.110835</dc:relation>
               <dc:rights>cc-by-nc-nd (c) Elsevier, 2020</dc:rights>
               <dc:rights>http://creativecommons.org/licenses/by-nc-nd/3.0/es</dc:rights>
               <dc:rights>info:eu-repo/semantics/openAccess</dc:rights>
               <dc:publisher>Elsevier</dc:publisher>
               <dc:source>Articles publicats en revistes (Ciència dels Materials i Química Física)</dc:source>
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