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Discoloration and organic matter removal from coffee wastewater by electrochemical advanced oxidation processes

Villanueva Rodríguez, Minerva | Bello Mendoza, Ricardo [autor/a] | Wareham, D. G [autor/a] | Ruiz Ruiz, E. J [autor/a] | Maya Treviño, M. L [autor/a].
Tipo de material: Artículo ArtículoTema(s): Tratamiento de aguas residuales | Café | Remoción de materia orgánica | Oxidación anódica de metalesTema(s) en inglés: Wastewater treatment | Coffee | Organic matter removal | Anodic oxidation of metalsDescriptor(es) geográficos: Finca La Concepción, Tapachula (Chiapas, México) Nota de acceso: Disponible para usuarios de ECOSUR con su clave de acceso En: Water, Air, & Soil Pollution. volumen 225, número 12 (December 2014), páginas 1-11. --ISSN: 0049-6979Número de sistema: 9480Resumen:
Inglés

The coffee agro-industry generates a large volume of wastewater that is notable for its high organic strength as well as its color content. Due to the seasonal nature of the harvest (3-4 months per year), this particular industrial waste needs a treatment method that is both reliable and fast (in terms of start-up time). As part of investigating a system capable of treating a coffee wastewater, this research evaluated four electrochemical advanced oxidation processes (EAOPs) using boron-doped diamond (BDD) electrodes. The processes were anodic oxidation (AO), anodic oxidation with electrogenerated H2O2 (AO-H2O2), electro-Fenton (EF), and photoelectro-Fenton (PEF). Experimental conditions were as follows: 40 mA cm−2 current density (all EAOPs), 0.3 mmol Fe2+ L−1 (Fenton systems), 300 mL air min−1 (AO-H2O2, EF, PEF), and 500 μW cm−2 UV irradiation (photo-Fenton systems). The performance of the four EAOP treatment methods (in terms of color and organic carbon removal) was compared against two conventional chemical oxidation methods, namely, Fenton and photo-Fenton. The research indicated that the four EAOPs were better at removing color (89-93 %) and total organic carbon (TOC) (73-84 %) than the respective chemical Fenton (58 and 4.8 %) and photo-Fenton (61 and 7 %) methods. The trend in performance was as follows: AO-H2O2 > AO > PEF ≈ EF. It appeared that the ferrous iron reagent formed a dark-colored complex with some coffee components, diminishing the effect of Fenton reactions. In addition, the dark color of the wastewater limited the effect of light in the UV-Fenton processes. Analysis showed that acceptable levels of Fe2+ (0.3 mmol L−1) and energy (0.082-0.098 kWh g−1 TOC) were required by the EAOPs after 4-h treatment time. In conclusion, the use of electrochemical methods (equipped with BDD electrodes) seems a promising method for the effective treatment of coffee wastewaters.
Lista(s) en las que aparece este ítem: Agua, salud y ambiente
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Disponible para usuarios de ECOSUR con su clave de acceso

The coffee agro-industry generates a large volume of wastewater that is notable for its high organic strength as well as its color content. Due to the seasonal nature of the harvest (3-4 months per year), this particular industrial waste needs a treatment method that is both reliable and fast (in terms of start-up time). As part of investigating a system capable of treating a coffee wastewater, this research evaluated four electrochemical advanced oxidation processes (EAOPs) using boron-doped diamond (BDD) electrodes. The processes were anodic oxidation (AO), anodic oxidation with electrogenerated H2O2 (AO-H2O2), electro-Fenton (EF), and photoelectro-Fenton (PEF). Experimental conditions were as follows: 40 mA cm−2 current density (all EAOPs), 0.3 mmol Fe2+ L−1 (Fenton systems), 300 mL air min−1 (AO-H2O2, EF, PEF), and 500 μW cm−2 UV irradiation (photo-Fenton systems). The performance of the four EAOP treatment methods (in terms of color and organic carbon removal) was compared against two conventional chemical oxidation methods, namely, Fenton and photo-Fenton. The research indicated that the four EAOPs were better at removing color (89-93 %) and total organic carbon (TOC) (73-84 %) than the respective chemical Fenton (58 and 4.8 %) and photo-Fenton (61 and 7 %) methods. The trend in performance was as follows: AO-H2O2 > AO > PEF ≈ EF. It appeared that the ferrous iron reagent formed a dark-colored complex with some coffee components, diminishing the effect of Fenton reactions. In addition, the dark color of the wastewater limited the effect of light in the UV-Fenton processes. Analysis showed that acceptable levels of Fe2+ (0.3 mmol L−1) and energy (0.082-0.098 kWh g−1 TOC) were required by the EAOPs after 4-h treatment time. In conclusion, the use of electrochemical methods (equipped with BDD electrodes) seems a promising method for the effective treatment of coffee wastewaters. eng

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