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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...
Autores principales: | , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
American
Chemical Society
2015
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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. |
format | Online Article Text |
id | pubmed-4473729 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2015 |
publisher | American
Chemical Society |
record_format | MEDLINE/PubMed |
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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