Electrochemical degradation of RB-5 dye by anodic oxidation, electro-Fenton and by combining anodic oxidation–electro-Fenton in a filter-press flow cell
Electrochemical degradation of RB-5 dye by anodic oxidation, electro-Fenton and by combining anodic oxidation–electro-Fenton in a filter-press flow cell
This paper reports the removal of a recalcitrant and toxic dye, Reactive Black 5 (RB-5) by threemethods; 1) anodic oxidation (AO) on Boron-Doped Diamond (BDD), 2) by electro-Fenton (EF) process where hydrogen peroxide was produced by oxygen reduction on reticulated vitreous carbon (RVC) electrodes and 3) by the combination of AO–EF. The BDD and RVC electrodes were fitted in a filter-press flow cell in recycle batch mode of operation. The experimental set-up for the AO and EF processes consisted of two electrolyte compartments separated by a Nafion membrane with the dye contained in the anolyte and the catholyte, respectively. The combined AO–EF process used only one electrolyte compartment. The colour and total organic carbon (TOC) removal were more efficientwhen the AO and EF processes were used separately than the combined process, AO–EF. The influence of current density and initial concentration of ferrous ions were examined. The lowest energy efficiency (208 kWh kg?1) with the EF process was found when ?0.4 V vs. Ag/AgCl was applied to a RVC electrode and the concentration of Fe2+ was 1.0 × 10?4 mol dm?3 achieving total colour and 74% of TOC removals in less than 90 min electrolysis. All proposed processeswere able to promote high percentages of TOC removal following a pseudo-first order kinetic oxidation. The BDD electrode was the most effective material to remove RB-5 dye within 7.5 min and presented the highest apparent rate constant (0.835 min?1) with 82% TOC removal within 30 min at an energy consumption of 291 kWh kg?1 and 41.1 mA cm?2 current density. In the case of the combined process AO–EF the electrodegradation rate of RB-5 was at least three times lower, apparent rate constant (0.269 min?1), and 32% of TOC was removed with a high EC (682 kWh kg?1). Therefore oxidation process applied separately was more efficient
boron-doped diamond, electrochemical oxidation, electro-Fenton process, filter-press flow cell, reactive black 5 dye, reticulated vitreous carbon
179-187
Vasconcelos, Vanessa M.
ed5d7911-79c3-47e2-b129-1ca59fae627f
Ponce de Leon, Carlos
508a312e-75ff-4bcb-9151-dacc424d755c
Nava, Jose L.
266d748b-426f-4300-9306-0a2fe549bd15
Lanza, Marcos R.V.
cbf2c772-89be-411d-b3f0-0c835fd5300a
15 March 2016
Vasconcelos, Vanessa M.
ed5d7911-79c3-47e2-b129-1ca59fae627f
Ponce de Leon, Carlos
508a312e-75ff-4bcb-9151-dacc424d755c
Nava, Jose L.
266d748b-426f-4300-9306-0a2fe549bd15
Lanza, Marcos R.V.
cbf2c772-89be-411d-b3f0-0c835fd5300a
Vasconcelos, Vanessa M., Ponce de Leon, Carlos, Nava, Jose L. and Lanza, Marcos R.V.
(2016)
Electrochemical degradation of RB-5 dye by anodic oxidation, electro-Fenton and by combining anodic oxidation–electro-Fenton in a filter-press flow cell.
Journal of Electroanalytical Chemistry, 765, .
(doi:10.1016/j.jelechem.2015.07.040).
Abstract
This paper reports the removal of a recalcitrant and toxic dye, Reactive Black 5 (RB-5) by threemethods; 1) anodic oxidation (AO) on Boron-Doped Diamond (BDD), 2) by electro-Fenton (EF) process where hydrogen peroxide was produced by oxygen reduction on reticulated vitreous carbon (RVC) electrodes and 3) by the combination of AO–EF. The BDD and RVC electrodes were fitted in a filter-press flow cell in recycle batch mode of operation. The experimental set-up for the AO and EF processes consisted of two electrolyte compartments separated by a Nafion membrane with the dye contained in the anolyte and the catholyte, respectively. The combined AO–EF process used only one electrolyte compartment. The colour and total organic carbon (TOC) removal were more efficientwhen the AO and EF processes were used separately than the combined process, AO–EF. The influence of current density and initial concentration of ferrous ions were examined. The lowest energy efficiency (208 kWh kg?1) with the EF process was found when ?0.4 V vs. Ag/AgCl was applied to a RVC electrode and the concentration of Fe2+ was 1.0 × 10?4 mol dm?3 achieving total colour and 74% of TOC removals in less than 90 min electrolysis. All proposed processeswere able to promote high percentages of TOC removal following a pseudo-first order kinetic oxidation. The BDD electrode was the most effective material to remove RB-5 dye within 7.5 min and presented the highest apparent rate constant (0.835 min?1) with 82% TOC removal within 30 min at an energy consumption of 291 kWh kg?1 and 41.1 mA cm?2 current density. In the case of the combined process AO–EF the electrodegradation rate of RB-5 was at least three times lower, apparent rate constant (0.269 min?1), and 32% of TOC was removed with a high EC (682 kWh kg?1). Therefore oxidation process applied separately was more efficient
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Accepted/In Press date: 23 July 2015
Published date: 15 March 2016
Keywords:
boron-doped diamond, electrochemical oxidation, electro-Fenton process, filter-press flow cell, reactive black 5 dye, reticulated vitreous carbon
Organisations:
Energy Technology Group
Identifiers
Local EPrints ID: 380668
URI: http://eprints.soton.ac.uk/id/eprint/380668
ISSN: 1572-6657
PURE UUID: b9adb9ed-8fba-4f31-8bae-4706d15cf042
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Date deposited: 14 Sep 2015 10:04
Last modified: 15 Mar 2024 03:22
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Author:
Vanessa M. Vasconcelos
Author:
Jose L. Nava
Author:
Marcos R.V. Lanza
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