Advanced oxidation treatment of malachite green dye using a low cost carbon-felt air-diffusion cathode. Issue 2 (June 2016)

• Record Type: Journal Article
• Authors: Bañuelos, Jennifer A.; García-Rodríguez, Orlando; El-Ghenymy, Abdellatif; Rodríguez-Valadez, Francisco J.; Godínez, Luis A.; Brillas, Enric
• Is Part Of: Journal of environmental chemical engineering. Volume 4:Issue 2(2016:Jun.)
• Page Start: 2066
• Page End: 2075
• Publication Date: 2016-06
• Subjects: Malachite green -- Carbon felt -- Water treatment -- Fenton process -- Photo-electro-Fenton process -- Anodic oxidation; Chemical engineering -- Environmental aspects -- Periodicals; Environmental engineering -- Periodicals; Chemical engineering -- Environmental aspects; Environmental engineering; Periodicals; 660.0286
• DOI: 10.1016/j.jece.2016.03.012
• Languages: English
• ISSNs: 2213-2929

Abstract

Highlights: A low cost carbon-felt material was employed as an air-diffusion cathode for the generation of H2 O2 from O2 reduction in acidic aqueous medium. The carbon felt electrode performed technically and economically better than other carbonaceous materials in O2 -saturated solutions. An electro- and photo-electro-Fenton based reactor was constructed for the degradation of malachite green dye. The carbon felt cathode progressively lost performance due to the gradual deposition of Fe species, however this deposition was reversible. Abstract: A low cost carbon-felt (CF) material has been successfully employed as an air-diffusion cathode for the generation of H2 O2 from O2 reduction in 0.05 M Na2 SO4 at pH 3. Using a BDD (Boron Doped Diamond)/CF air-diffusion electrode (3 cm 2 ), a maximum of 94 mg L −1 of H2 O2 were accumulated for the best current density value identified (21.7 mA cm −2 ). These results were technically and economically better than other performances observed for similar cathode materials in O2 -saturated solutions. An electrochemical reactor utilizing these electrodes was employed to degrade malachite green (MG) dye in the same electrolyte containing 0.5 mM of Fe 2+ using the electro-Fenton (EF) and photoelectro-Fenton (PEF) processes. The main oxidant was HO formed at the BDD surface from water oxidation and in the bulk from Fenton's reaction between H2 O2 and added Fe 2+ . As expected, the PEF process was more powerful than the EF due to the enhancement of HO production by photolysis of Fe(III)-hydroxy species and of Fe(III) complexes of the oxalate of the dye, as well as of intermediates. The effect of MG concentration on decolorization and mineralization rates, mineralization current efficiency and energy consumption for both processes were assessed. The CF air-diffusion cathode lost progressively performance upon consecutive PEF treatment of a 150 mg L −1 MG owed to the gradual deposition of Fe species, as well as an enrichment of O, Na and S species on its surface. The deposition of Fe species was reversible since these were dissolved in the medium in consecutive trials without the need of adding new amounts of Fe 2+ .