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Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production

[Image: see text] Hydrogen peroxide (H(2)O(2)) is frequently used in combination with ultraviolet (UV) light to treat trace organic contaminants in advanced oxidation processes (AOPs). In small-scale applications, such as wellhead and point-of-entry water treatment systems, the need to maintain a st...

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Autores principales: Barazesh, James M., Hennebel, Tom, Jasper, Justin T., Sedlak, David L.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: American Chemical Society 2015
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4473729/
https://www.ncbi.nlm.nih.gov/pubmed/26039560
http://dx.doi.org/10.1021/acs.est.5b01254
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author Barazesh, James M.
Hennebel, Tom
Jasper, Justin T.
Sedlak, David L.
author_facet Barazesh, James M.
Hennebel, Tom
Jasper, Justin T.
Sedlak, David L.
author_sort Barazesh, James M.
collection PubMed
description [Image: see text] Hydrogen peroxide (H(2)O(2)) is frequently used in combination with ultraviolet (UV) light to treat trace organic contaminants in advanced oxidation processes (AOPs). In small-scale applications, such as wellhead and point-of-entry water treatment systems, the need to maintain a stock solution of concentrated H(2)O(2) increases the operational cost and complicates the operation of AOPs. To avoid the need for replenishing a stock solution of H(2)O(2), a gas diffusion electrode was used to generate low concentrations of H(2)O(2) directly in the water prior to its exposure to UV light. Following the AOP, the solution was passed through an anodic chamber to lower the solution pH and remove the residual H(2)O(2). The effectiveness of the technology was evaluated using a suite of trace contaminants that spanned a range of reactivity with UV light and hydroxyl radical (HO(•)) in three different types of source waters (i.e., simulated groundwater, simulated surface water, and municipal wastewater effluent) as well as a sodium chloride solution. Irrespective of the source water, the system produced enough H(2)O(2) to treat up to 120 L water d(–1). The extent of transformation of trace organic contaminants was affected by the current density and the concentrations of HO(•) scavengers in the source water. The electrical energy per order (E(EO)) ranged from 1 to 3 kWh m(–3), with the UV lamp accounting for most of the energy consumption. The gas diffusion electrode exhibited high efficiency for H(2)O(2) production over extended periods and did not show a diminution in performance in any of the matrices.
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spelling pubmed-44737292015-06-22 Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production Barazesh, James M. Hennebel, Tom Jasper, Justin T. Sedlak, David L. Environ Sci Technol [Image: see text] Hydrogen peroxide (H(2)O(2)) is frequently used in combination with ultraviolet (UV) light to treat trace organic contaminants in advanced oxidation processes (AOPs). In small-scale applications, such as wellhead and point-of-entry water treatment systems, the need to maintain a stock solution of concentrated H(2)O(2) increases the operational cost and complicates the operation of AOPs. To avoid the need for replenishing a stock solution of H(2)O(2), a gas diffusion electrode was used to generate low concentrations of H(2)O(2) directly in the water prior to its exposure to UV light. Following the AOP, the solution was passed through an anodic chamber to lower the solution pH and remove the residual H(2)O(2). The effectiveness of the technology was evaluated using a suite of trace contaminants that spanned a range of reactivity with UV light and hydroxyl radical (HO(•)) in three different types of source waters (i.e., simulated groundwater, simulated surface water, and municipal wastewater effluent) as well as a sodium chloride solution. Irrespective of the source water, the system produced enough H(2)O(2) to treat up to 120 L water d(–1). The extent of transformation of trace organic contaminants was affected by the current density and the concentrations of HO(•) scavengers in the source water. The electrical energy per order (E(EO)) ranged from 1 to 3 kWh m(–3), with the UV lamp accounting for most of the energy consumption. The gas diffusion electrode exhibited high efficiency for H(2)O(2) production over extended periods and did not show a diminution in performance in any of the matrices. American Chemical Society 2015-06-03 2015-06-16 /pmc/articles/PMC4473729/ /pubmed/26039560 http://dx.doi.org/10.1021/acs.est.5b01254 Text en Copyright © 2015 American Chemical Society This is an open access article published under an ACS AuthorChoice License (http://pubs.acs.org/page/policy/authorchoice_termsofuse.html) , which permits copying and redistribution of the article or any adaptations for non-commercial purposes.
spellingShingle Barazesh, James M.
Hennebel, Tom
Jasper, Justin T.
Sedlak, David L.
Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production
title Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production
title_full Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production
title_fullStr Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production
title_full_unstemmed Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production
title_short Modular Advanced Oxidation Process Enabled by Cathodic Hydrogen Peroxide Production
title_sort modular advanced oxidation process enabled by cathodic hydrogen peroxide production
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC4473729/
https://www.ncbi.nlm.nih.gov/pubmed/26039560
http://dx.doi.org/10.1021/acs.est.5b01254
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