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Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column
A continuous mode fixed-bed up-flow column adsorption analysis was conducted utilizing Acacia nilotica sawdust activated carbon (ASAC) as an adsorbent for the adsorption treatment of toxic Indigo Carmine Dye (ICD). The effect on the adsorption characteristics of ASAC of the influent ICD concentratio...
Autores principales: | , , , , , , , |
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Formato: | Online Artículo Texto |
Lenguaje: | English |
Publicado: |
Nature Publishing Group UK
2022
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Materias: | |
Acceso en línea: | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9478148/ https://www.ncbi.nlm.nih.gov/pubmed/36109547 http://dx.doi.org/10.1038/s41598-022-19595-6 |
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author | Gupta, Tripti Ansari, Khalid Lataye, Dilip Kadu, Mahendra Khan, Mohammad Amir Mubarak, Nabisab Mujawar Garg, Rishav Karri, Rama Rao |
author_facet | Gupta, Tripti Ansari, Khalid Lataye, Dilip Kadu, Mahendra Khan, Mohammad Amir Mubarak, Nabisab Mujawar Garg, Rishav Karri, Rama Rao |
author_sort | Gupta, Tripti |
collection | PubMed |
description | A continuous mode fixed-bed up-flow column adsorption analysis was conducted utilizing Acacia nilotica sawdust activated carbon (ASAC) as an adsorbent for the adsorption treatment of toxic Indigo Carmine Dye (ICD). The effect on the adsorption characteristics of ASAC of the influent ICD concentration, flow rate, and column bed depth has been investigated. According to the column study, the highest efficiency of ICD removal was approximately 79.01% at a preliminary concentration of 100 mg/L with a flow rate of 250 mL/h at a bed depth of 30 cm and adsorption power of 24.67 mg/g. The experimental work confirmed the dependency of break-through curves on dye concentration and flow rate for a given bed depth. Kinetic models were implemented by Thomas, Yoon–Nelson, and Bed-depth-service-time analysis along with error analysis to interpret experimental data for bed depth of 15 cm and 30 cm, ICD concentration of 100 mg/L and 200 mg/L and flow rate of 250 mL/h, and 500 mL/h. The analysis predicted the breakthrough curves using a regression basin. It indicated that all three models were comparable for the entire break-through curve depiction. The characteristic parameters determined by process design and error analysis revealed that the Thomas model was better followed by the BDST and Yoon–Nelson models in relating the procedure of ICD adsorption onto ASAC. B-E-T surface area and B-E-T pore volume of ASAC were 737.76 m(2)/g and 0.2583 cm(3)/g, respectively. S-E-M and X-R-D analysis reveal the micro-porous and amorphous nature of ASAC. F-T-I-R spectroscope indicate distinctive functional assemblies like -OH group, C–H bond, C–C bond, C–OH, and C–O groups on ASAC. It could be computed that the ASAC can be used efficiently as an alternative option for industrial wastewater treatment |
format | Online Article Text |
id | pubmed-9478148 |
institution | National Center for Biotechnology Information |
language | English |
publishDate | 2022 |
publisher | Nature Publishing Group UK |
record_format | MEDLINE/PubMed |
spelling | pubmed-94781482022-09-17 Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column Gupta, Tripti Ansari, Khalid Lataye, Dilip Kadu, Mahendra Khan, Mohammad Amir Mubarak, Nabisab Mujawar Garg, Rishav Karri, Rama Rao Sci Rep Article A continuous mode fixed-bed up-flow column adsorption analysis was conducted utilizing Acacia nilotica sawdust activated carbon (ASAC) as an adsorbent for the adsorption treatment of toxic Indigo Carmine Dye (ICD). The effect on the adsorption characteristics of ASAC of the influent ICD concentration, flow rate, and column bed depth has been investigated. According to the column study, the highest efficiency of ICD removal was approximately 79.01% at a preliminary concentration of 100 mg/L with a flow rate of 250 mL/h at a bed depth of 30 cm and adsorption power of 24.67 mg/g. The experimental work confirmed the dependency of break-through curves on dye concentration and flow rate for a given bed depth. Kinetic models were implemented by Thomas, Yoon–Nelson, and Bed-depth-service-time analysis along with error analysis to interpret experimental data for bed depth of 15 cm and 30 cm, ICD concentration of 100 mg/L and 200 mg/L and flow rate of 250 mL/h, and 500 mL/h. The analysis predicted the breakthrough curves using a regression basin. It indicated that all three models were comparable for the entire break-through curve depiction. The characteristic parameters determined by process design and error analysis revealed that the Thomas model was better followed by the BDST and Yoon–Nelson models in relating the procedure of ICD adsorption onto ASAC. B-E-T surface area and B-E-T pore volume of ASAC were 737.76 m(2)/g and 0.2583 cm(3)/g, respectively. S-E-M and X-R-D analysis reveal the micro-porous and amorphous nature of ASAC. F-T-I-R spectroscope indicate distinctive functional assemblies like -OH group, C–H bond, C–C bond, C–OH, and C–O groups on ASAC. It could be computed that the ASAC can be used efficiently as an alternative option for industrial wastewater treatment Nature Publishing Group UK 2022-09-15 /pmc/articles/PMC9478148/ /pubmed/36109547 http://dx.doi.org/10.1038/s41598-022-19595-6 Text en © The Author(s) 2022 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 Gupta, Tripti Ansari, Khalid Lataye, Dilip Kadu, Mahendra Khan, Mohammad Amir Mubarak, Nabisab Mujawar Garg, Rishav Karri, Rama Rao Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column |
title | Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column |
title_full | Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column |
title_fullStr | Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column |
title_full_unstemmed | Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column |
title_short | Adsorption of Indigo Carmine Dye by Acacia nilotica sawdust activated carbon in fixed bed column |
title_sort | adsorption of indigo carmine dye by acacia nilotica sawdust activated carbon in fixed bed column |
topic | Article |
url | https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9478148/ https://www.ncbi.nlm.nih.gov/pubmed/36109547 http://dx.doi.org/10.1038/s41598-022-19595-6 |
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