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Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth

Industrial wastewater polluted with high concentrations of Cr is commonly discharged into water resources without proper treatment. This gives rise to the deterioration of water quality and imposes adverse effects on public health. Therefore, this study is aimed at removing Cr from electroplating wa...

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Autores principales: Worku, Zemene, Tibebu, Samuel, Nure, Jemal Fito, Tibebu, Solomon, Moyo, Welldone, Ambaye, Abera Demeke, Nkambule, Thabo T. I.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: Springer International Publishing 2023
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10367414/
https://www.ncbi.nlm.nih.gov/pubmed/37488644
http://dx.doi.org/10.1186/s13065-023-00993-4
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author Worku, Zemene
Tibebu, Samuel
Nure, Jemal Fito
Tibebu, Solomon
Moyo, Welldone
Ambaye, Abera Demeke
Nkambule, Thabo T. I.
author_facet Worku, Zemene
Tibebu, Samuel
Nure, Jemal Fito
Tibebu, Solomon
Moyo, Welldone
Ambaye, Abera Demeke
Nkambule, Thabo T. I.
author_sort Worku, Zemene
collection PubMed
description Industrial wastewater polluted with high concentrations of Cr is commonly discharged into water resources without proper treatment. This gives rise to the deterioration of water quality and imposes adverse effects on public health. Therefore, this study is aimed at removing Cr from electroplating wastewater using activated carbon produced from water hyacinth under a full factorial experimental design with three factors and three levels (pH,2,5 and 8, adsorbent dose 0.5,1and1.5 in 100 mL and contact time 30, 60 and120 min). A phosphoric acid solution of 37% was used to activate the carbon, which was then subjected to thermal decomposition for 15 min at 500 °C. The activated carbon was characterized by the presence of a high surface area (203.83 m(2)/g) of BET, cracking of adsorbent beads of SEM morphology, amorphous nature of XRD, and many functional groups of FTIR such as hydroxyl (3283 cm(−1)), alkane (2920 cm(−1)), nitrile (2114 cm(−1)) and aromatics (1613 cm(−1)). The minimum Cr adsorption performance of 15.6% was obtained whereas maximum removal of 90.4% was recorded at the experimental condition of pH 2, adsorbent dose of 1.5 g/100 mL, and contact time of 120 min at a fixed value of initial Cr concentration of 100 mg/L. Similarly, the maximum Cr removal from real electroplating wastewater was 81.2% at this optimum point. Langmuir's model best described the experimental value at R(2) 0.96 which implies the adsorption is chemically bonded, homogeneous, and monolayer. Pseudo-second-order model best fits with the experimental data with R(2) value of 0.99. The adsorbent was regenerated for seven cycles and the removal efficiency decreased from 93.25% to 21.35%. Finally, this technology is promising to be scaled up to an industrial level.
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spelling pubmed-103674142023-07-26 Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth Worku, Zemene Tibebu, Samuel Nure, Jemal Fito Tibebu, Solomon Moyo, Welldone Ambaye, Abera Demeke Nkambule, Thabo T. I. BMC Chem Research Industrial wastewater polluted with high concentrations of Cr is commonly discharged into water resources without proper treatment. This gives rise to the deterioration of water quality and imposes adverse effects on public health. Therefore, this study is aimed at removing Cr from electroplating wastewater using activated carbon produced from water hyacinth under a full factorial experimental design with three factors and three levels (pH,2,5 and 8, adsorbent dose 0.5,1and1.5 in 100 mL and contact time 30, 60 and120 min). A phosphoric acid solution of 37% was used to activate the carbon, which was then subjected to thermal decomposition for 15 min at 500 °C. The activated carbon was characterized by the presence of a high surface area (203.83 m(2)/g) of BET, cracking of adsorbent beads of SEM morphology, amorphous nature of XRD, and many functional groups of FTIR such as hydroxyl (3283 cm(−1)), alkane (2920 cm(−1)), nitrile (2114 cm(−1)) and aromatics (1613 cm(−1)). The minimum Cr adsorption performance of 15.6% was obtained whereas maximum removal of 90.4% was recorded at the experimental condition of pH 2, adsorbent dose of 1.5 g/100 mL, and contact time of 120 min at a fixed value of initial Cr concentration of 100 mg/L. Similarly, the maximum Cr removal from real electroplating wastewater was 81.2% at this optimum point. Langmuir's model best described the experimental value at R(2) 0.96 which implies the adsorption is chemically bonded, homogeneous, and monolayer. Pseudo-second-order model best fits with the experimental data with R(2) value of 0.99. The adsorbent was regenerated for seven cycles and the removal efficiency decreased from 93.25% to 21.35%. Finally, this technology is promising to be scaled up to an industrial level. Springer International Publishing 2023-07-24 /pmc/articles/PMC10367414/ /pubmed/37488644 http://dx.doi.org/10.1186/s13065-023-00993-4 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/) . The Creative Commons Public Domain Dedication waiver (http://creativecommons.org/publicdomain/zero/1.0/ (https://creativecommons.org/publicdomain/zero/1.0/) ) applies to the data made available in this article, unless otherwise stated in a credit line to the data.
spellingShingle Research
Worku, Zemene
Tibebu, Samuel
Nure, Jemal Fito
Tibebu, Solomon
Moyo, Welldone
Ambaye, Abera Demeke
Nkambule, Thabo T. I.
Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth
title Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth
title_full Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth
title_fullStr Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth
title_full_unstemmed Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth
title_short Adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth
title_sort adsorption of chromium from electroplating wastewater using activated carbon developed from water hyacinth
topic Research
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10367414/
https://www.ncbi.nlm.nih.gov/pubmed/37488644
http://dx.doi.org/10.1186/s13065-023-00993-4
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