Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor

Vinal-derived Activated Carbon (VAC) developed by phosphoric acid activation of sawdust from Prosopis ruscifolia native wood was tested for the adsorption of Ni(II) ions from dilute solutions in both batch and dynamic modes, comparing it with a Commercial Activated Carbon (CAC). Batch experiments we...

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Autores principales: Nabarlatz, D., de Celis, J., Bonelli, P., Cukierman, A.L.
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Acceso en línea:http://hdl.handle.net/20.500.12110/paper_03014797_v97_n1_p109_Nabarlatz
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spelling todo:paper_03014797_v97_n1_p109_Nabarlatz2023-10-03T15:18:26Z Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor Nabarlatz, D. de Celis, J. Bonelli, P. Cukierman, A.L. Breakthrough Native wood-derived activated carbon Nickel adsorption Regeneration activated carbon lignocellulose nickel activated carbon adsorption cellulose concentration (composition) inorganic acid ion isotherm legume lignin nickel numerical model reaction kinetics regeneration adsorption kinetics article flow rate isotherm waste water management Adsorption Carbon Environmental Remediation Kinetics Nickel Prosopis Water Purification Prosopis ruscifolia Vinal-derived Activated Carbon (VAC) developed by phosphoric acid activation of sawdust from Prosopis ruscifolia native wood was tested for the adsorption of Ni(II) ions from dilute solutions in both batch and dynamic modes, comparing it with a Commercial Activated Carbon (CAC). Batch experiments were performed to determine adsorption kinetics and equilibrium isotherms for both carbons. It was possible to remove near 6.55mg Nig -1 VAC and 7.65mg Nig -1 CAC after 5h and 10h contact time, respectively. A pseudo second order equation fitted well with the kinetics of the process, and Langmuir adsorption model was used to adjust the experimental results concerning the adsorption isotherm. The parameters obtained indicate a stronger interaction between sorbent and sorbate for VAC (K=26.56Lmmol -1) than for CAC (K=19.54Lmmol -1). Continuous experiments were performed in a fixed-bed column packed with the investigated carbons, evaluating the influence of operational parameters such as flow rate, bed height and feed concentration on the breakthrough curves obtained. The breakthrough occurred more slowly for low concentrations of the metal ion in the feed, low flow rates and high bed height. The breakthrough curves were properly represented by Hall's model for both carbon types. Regeneration of the vinal activated carbon in column was tested, obtaining the same breakthrough curve in a new cycle of use. Finally, vinal-derived activated carbon can effectively be used to treat wastewater having until 30ppm Ni(II). © 2011 Elsevier Ltd. Fil:Bonelli, P. Universidad de Buenos Aires. Facultad de Ciencias Exactas y Naturales; Argentina. Fil:Cukierman, A.L. Universidad de Buenos Aires. Facultad de Ciencias Exactas y Naturales; Argentina. JOUR info:eu-repo/semantics/openAccess http://creativecommons.org/licenses/by/2.5/ar http://hdl.handle.net/20.500.12110/paper_03014797_v97_n1_p109_Nabarlatz
institution Universidad de Buenos Aires
institution_str I-28
repository_str R-134
collection Biblioteca Digital - Facultad de Ciencias Exactas y Naturales (UBA)
topic Breakthrough
Native wood-derived activated carbon
Nickel adsorption
Regeneration
activated carbon
lignocellulose
nickel
activated carbon
adsorption
cellulose
concentration (composition)
inorganic acid
ion
isotherm
legume
lignin
nickel
numerical model
reaction kinetics
regeneration
adsorption kinetics
article
flow rate
isotherm
waste water management
Adsorption
Carbon
Environmental Remediation
Kinetics
Nickel
Prosopis
Water Purification
Prosopis ruscifolia
spellingShingle Breakthrough
Native wood-derived activated carbon
Nickel adsorption
Regeneration
activated carbon
lignocellulose
nickel
activated carbon
adsorption
cellulose
concentration (composition)
inorganic acid
ion
isotherm
legume
lignin
nickel
numerical model
reaction kinetics
regeneration
adsorption kinetics
article
flow rate
isotherm
waste water management
Adsorption
Carbon
Environmental Remediation
Kinetics
Nickel
Prosopis
Water Purification
Prosopis ruscifolia
Nabarlatz, D.
de Celis, J.
Bonelli, P.
Cukierman, A.L.
Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor
topic_facet Breakthrough
Native wood-derived activated carbon
Nickel adsorption
Regeneration
activated carbon
lignocellulose
nickel
activated carbon
adsorption
cellulose
concentration (composition)
inorganic acid
ion
isotherm
legume
lignin
nickel
numerical model
reaction kinetics
regeneration
adsorption kinetics
article
flow rate
isotherm
waste water management
Adsorption
Carbon
Environmental Remediation
Kinetics
Nickel
Prosopis
Water Purification
Prosopis ruscifolia
description Vinal-derived Activated Carbon (VAC) developed by phosphoric acid activation of sawdust from Prosopis ruscifolia native wood was tested for the adsorption of Ni(II) ions from dilute solutions in both batch and dynamic modes, comparing it with a Commercial Activated Carbon (CAC). Batch experiments were performed to determine adsorption kinetics and equilibrium isotherms for both carbons. It was possible to remove near 6.55mg Nig -1 VAC and 7.65mg Nig -1 CAC after 5h and 10h contact time, respectively. A pseudo second order equation fitted well with the kinetics of the process, and Langmuir adsorption model was used to adjust the experimental results concerning the adsorption isotherm. The parameters obtained indicate a stronger interaction between sorbent and sorbate for VAC (K=26.56Lmmol -1) than for CAC (K=19.54Lmmol -1). Continuous experiments were performed in a fixed-bed column packed with the investigated carbons, evaluating the influence of operational parameters such as flow rate, bed height and feed concentration on the breakthrough curves obtained. The breakthrough occurred more slowly for low concentrations of the metal ion in the feed, low flow rates and high bed height. The breakthrough curves were properly represented by Hall's model for both carbon types. Regeneration of the vinal activated carbon in column was tested, obtaining the same breakthrough curve in a new cycle of use. Finally, vinal-derived activated carbon can effectively be used to treat wastewater having until 30ppm Ni(II). © 2011 Elsevier Ltd.
format JOUR
author Nabarlatz, D.
de Celis, J.
Bonelli, P.
Cukierman, A.L.
author_facet Nabarlatz, D.
de Celis, J.
Bonelli, P.
Cukierman, A.L.
author_sort Nabarlatz, D.
title Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor
title_short Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor
title_full Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor
title_fullStr Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor
title_full_unstemmed Batch and dynamic sorption of Ni(II) ions by activated carbon based on a native lignocellulosic precursor
title_sort batch and dynamic sorption of ni(ii) ions by activated carbon based on a native lignocellulosic precursor
url http://hdl.handle.net/20.500.12110/paper_03014797_v97_n1_p109_Nabarlatz
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AT bonellip batchanddynamicsorptionofniiiionsbyactivatedcarbonbasedonanativelignocellulosicprecursor
AT cukiermanal batchanddynamicsorptionofniiiionsbyactivatedcarbonbasedonanativelignocellulosicprecursor
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