Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processes
<p class="PaperAbstract">Small volumes (100 mL) of acidic aqueous solutions with 30-200 mg L<sup>-1</sup> TOC of the toxic azo dye Acid Red 1 (AR1) have been comparatively treated by various electrochemical advanced oxidation processes (EAOPs). The electrolytic system con...
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doaj-125cfebce9444eec88ffe91222cbb9a92020-11-24T23:49:24ZengInternational Association of Physical Chemists (IAPC)Journal of Electrochemical Science and Engineering1847-92862014-12-014423524510.5599/jese.2014.005860Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processesCamilo González-Vargas0Ricardo Salazar1Ignasi Sirés2Laboratorio de Electroquímica Medio Ambiental, LEQMA, Departamento de Ciencias del Ambiente, Facultad de Química y Biología, Universidad de Santiago de Chile, USACh, Casilla 40, Correo 33, SantiagoLaboratorio de Electroquímica Medio Ambiental, LEQMA, Departamento de Ciencias del Ambiente, Facultad de Química y Biología, Universidad de Santiago de Chile, USACh, Casilla 40, Correo 33, SantiagoLaboratori d’Electroquímica dels Materials i del Medi Ambient, Departament de Química Física, Facultat de Química, Universitat de Barcelona, Martí i Franquès 1-11, 08028 Barcelona<p class="PaperAbstract">Small volumes (100 mL) of acidic aqueous solutions with 30-200 mg L<sup>-1</sup> TOC of the toxic azo dye Acid Red 1 (AR1) have been comparatively treated by various electrochemical advanced oxidation processes (EAOPs). The electrolytic system consisted of a BDD anode able to produce <sup>·</sup>OH and an air-diffusion cathode that generated H<sub>2</sub>O<sub>2</sub>, which subsequently reacted with added Fe<sup>2+</sup> to yield additional <sup>·</sup>OH from Fenton’s reaction. Under optimized conditions (i.e., 1.0 mM Fe<sup>2+</sup>, 60 mA cm<sup>-2</sup>, pH 3.0, 35 ºC), the analysis of the initial rates for decolourization and AR1 decay assuming a pseudo-first-order kinetics revealed a much higher rate constant for photoelectro-Fenton (PEF, ~ 2.7x10<sup>-3</sup> s<sup>-1</sup>) compared to electro-Fenton (EF, ~ 0.6x10<sup>-3</sup> s<sup>-1</sup>). Mineralization after 180 min was also greater in the former treatment (90 % vs 63 %). The use of UV radiation in PEF contributed to Fe(III) photoreduction as well as to photodecarboxylation of refractory intermediates, yielding a mineralization current efficiency as high as 85% during the treatment of solutions of 200 mg L<sup>-1</sup> TOC. Primary reaction intermediates included three aromatic derivatives with the initial naphthalenic structure and four molecules only featuring benzenic rings, which were totally mineralized in PEF.</p><p class="PaperTitle"> </p>http://www.pub.iapchem.org/ojs/index.php/JESE/article/view/88 |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Camilo González-Vargas Ricardo Salazar Ignasi Sirés |
spellingShingle |
Camilo González-Vargas Ricardo Salazar Ignasi Sirés Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processes Journal of Electrochemical Science and Engineering |
author_facet |
Camilo González-Vargas Ricardo Salazar Ignasi Sirés |
author_sort |
Camilo González-Vargas |
title |
Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processes |
title_short |
Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processes |
title_full |
Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processes |
title_fullStr |
Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processes |
title_full_unstemmed |
Electrochemical treatment of Acid Red 1 by electro-Fenton and photoelectro-Fenton processes |
title_sort |
electrochemical treatment of acid red 1 by electro-fenton and photoelectro-fenton processes |
publisher |
International Association of Physical Chemists (IAPC) |
series |
Journal of Electrochemical Science and Engineering |
issn |
1847-9286 |
publishDate |
2014-12-01 |
description |
<p class="PaperAbstract">Small volumes (100 mL) of acidic aqueous solutions with 30-200 mg L<sup>-1</sup> TOC of the toxic azo dye Acid Red 1 (AR1) have been comparatively treated by various electrochemical advanced oxidation processes (EAOPs). The electrolytic system consisted of a BDD anode able to produce <sup>·</sup>OH and an air-diffusion cathode that generated H<sub>2</sub>O<sub>2</sub>, which subsequently reacted with added Fe<sup>2+</sup> to yield additional <sup>·</sup>OH from Fenton’s reaction. Under optimized conditions (i.e., 1.0 mM Fe<sup>2+</sup>, 60 mA cm<sup>-2</sup>, pH 3.0, 35 ºC), the analysis of the initial rates for decolourization and AR1 decay assuming a pseudo-first-order kinetics revealed a much higher rate constant for photoelectro-Fenton (PEF, ~ 2.7x10<sup>-3</sup> s<sup>-1</sup>) compared to electro-Fenton (EF, ~ 0.6x10<sup>-3</sup> s<sup>-1</sup>). Mineralization after 180 min was also greater in the former treatment (90 % vs 63 %). The use of UV radiation in PEF contributed to Fe(III) photoreduction as well as to photodecarboxylation of refractory intermediates, yielding a mineralization current efficiency as high as 85% during the treatment of solutions of 200 mg L<sup>-1</sup> TOC. Primary reaction intermediates included three aromatic derivatives with the initial naphthalenic structure and four molecules only featuring benzenic rings, which were totally mineralized in PEF.</p><p class="PaperTitle"> </p> |
url |
http://www.pub.iapchem.org/ojs/index.php/JESE/article/view/88 |
work_keys_str_mv |
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