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Electrocoagulation/flotation process for removing copper from an aqueous environment

The presence of copper in aqueous environments such as drinking water has led to several environmental effects, such as flavor and odor. The increase in Cu levels in ground and surface water has been mainly attributed to anthropogenic and natural sources. Consequently, this applied-analytical study...

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Autor principal: Kashi, Giti
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Nature Publishing Group UK 2023
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10432402/
https://www.ncbi.nlm.nih.gov/pubmed/37587185
http://dx.doi.org/10.1038/s41598-023-40512-y
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author Kashi, Giti
author_facet Kashi, Giti
author_sort Kashi, Giti
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description The presence of copper in aqueous environments such as drinking water has led to several environmental effects, such as flavor and odor. The increase in Cu levels in ground and surface water has been mainly attributed to anthropogenic and natural sources. Consequently, this applied-analytical study aimed to investigate copper removal from urban drinking water through batch reactor electrocoagulation/flotation (ECF) with aluminum electrodes. The copper removal efficiency was evaluated under various operating conditions of current density (0.8–2.4 mA/cm(2)), initial concentration (1–100 mg/L), pH (3.5–10.5), and time (10–30 min). Cu was determined using the method outlined in the standard procedures (3500-Cu B at 4571 nm). The results indicated that increasing the current density from 0.8 to 2.4 mA/cm(2) and the reaction time from 10 to 30 min improved Cu(+2) removal efficiency (from 95 to 100%). In addition, the results demonstrated that Cu(+2) reduction is 100% with an initial concentration of 100 mg/L, a pH of 7.5, a reaction time of 30 min, and an anode current density of 2.4 mA/cm(2). The Taguchi method results for copper removal efficiency show that reaction time is the most significant variable. Furthermore, Cu removal kinetics models in an ECF reactor are second-order (R(2) > 0.92). The Cu removal in the ECF reactor is due to redox and adsorption. Moreover, the operational costs of Cu treatment with Al electrode pairs are estimated to range from 8857 and 9636 Rial/kg of Cu removed. Thus, it can be concluded that the ECF process is very efficient in removing Cu from aqueous environments under optimum conditions.
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spelling pubmed-104324022023-08-18 Electrocoagulation/flotation process for removing copper from an aqueous environment Kashi, Giti Sci Rep Article The presence of copper in aqueous environments such as drinking water has led to several environmental effects, such as flavor and odor. The increase in Cu levels in ground and surface water has been mainly attributed to anthropogenic and natural sources. Consequently, this applied-analytical study aimed to investigate copper removal from urban drinking water through batch reactor electrocoagulation/flotation (ECF) with aluminum electrodes. The copper removal efficiency was evaluated under various operating conditions of current density (0.8–2.4 mA/cm(2)), initial concentration (1–100 mg/L), pH (3.5–10.5), and time (10–30 min). Cu was determined using the method outlined in the standard procedures (3500-Cu B at 4571 nm). The results indicated that increasing the current density from 0.8 to 2.4 mA/cm(2) and the reaction time from 10 to 30 min improved Cu(+2) removal efficiency (from 95 to 100%). In addition, the results demonstrated that Cu(+2) reduction is 100% with an initial concentration of 100 mg/L, a pH of 7.5, a reaction time of 30 min, and an anode current density of 2.4 mA/cm(2). The Taguchi method results for copper removal efficiency show that reaction time is the most significant variable. Furthermore, Cu removal kinetics models in an ECF reactor are second-order (R(2) > 0.92). The Cu removal in the ECF reactor is due to redox and adsorption. Moreover, the operational costs of Cu treatment with Al electrode pairs are estimated to range from 8857 and 9636 Rial/kg of Cu removed. Thus, it can be concluded that the ECF process is very efficient in removing Cu from aqueous environments under optimum conditions. Nature Publishing Group UK 2023-08-16 /pmc/articles/PMC10432402/ /pubmed/37587185 http://dx.doi.org/10.1038/s41598-023-40512-y Text en © The Author(s) 2023 https://creativecommons.org/licenses/by/4.0/Open Access This article is licensed under a Creative Commons Attribution 4.0 International License, which permits use, sharing, adaptation, distribution and reproduction in any medium or format, as long as you give appropriate credit to the original author(s) and the source, provide a link to the Creative Commons licence, and indicate if changes were made. The images or other third party material in this article are included in the article's Creative Commons licence, unless indicated otherwise in a credit line to the material. If material is not included in the article's Creative Commons licence and your intended use is not permitted by statutory regulation or exceeds the permitted use, you will need to obtain permission directly from the copyright holder. To view a copy of this licence, visit http://creativecommons.org/licenses/by/4.0/ (https://creativecommons.org/licenses/by/4.0/) .
spellingShingle Article
Kashi, Giti
Electrocoagulation/flotation process for removing copper from an aqueous environment
title Electrocoagulation/flotation process for removing copper from an aqueous environment
title_full Electrocoagulation/flotation process for removing copper from an aqueous environment
title_fullStr Electrocoagulation/flotation process for removing copper from an aqueous environment
title_full_unstemmed Electrocoagulation/flotation process for removing copper from an aqueous environment
title_short Electrocoagulation/flotation process for removing copper from an aqueous environment
title_sort electrocoagulation/flotation process for removing copper from an aqueous environment
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10432402/
https://www.ncbi.nlm.nih.gov/pubmed/37587185
http://dx.doi.org/10.1038/s41598-023-40512-y
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