Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon

The equilibrium adsorption isotherms of carbon dioxide on a commercial granular activated carbon (GAC) and an ammonia-modified GAC (OXA-GAC) were measured using a static volumetric method. CO2 adsorption measurements were performed at three different temperatures (303, 318, and 333 K), and pressures...

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Main Authors: Shafeeyan, M.S., Daud, Wan Mohd Ashri Wan, Shamiri, A., Aghamohammadi, N.
Format: Article
Published: Elsevier 2015
Subjects:
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author Shafeeyan, M.S.
Daud, Wan Mohd Ashri Wan
Shamiri, A.
Aghamohammadi, N.
author_facet Shafeeyan, M.S.
Daud, Wan Mohd Ashri Wan
Shamiri, A.
Aghamohammadi, N.
author_sort Shafeeyan, M.S.
collection UM
description The equilibrium adsorption isotherms of carbon dioxide on a commercial granular activated carbon (GAC) and an ammonia-modified GAC (OXA-GAC) were measured using a static volumetric method. CO2 adsorption measurements were performed at three different temperatures (303, 318, and 333 K), and pressures up to 1 atm. The obtained equilibrium data were fitted to the Freundlich, Sips, and Toth isotherms using a semi-empirical approach to differentiate the contributions of physical and chemical adsorption to the total CO2 uptake. The isotherm parameters were determined independently for each mechanism by non-linear regression. To evaluate the adequacy of the fit of the isotherm models, two different error functions (i.e., the average relative error and the nonlinear regression coefficient) were calculated. The Toth semi-empirical equilibrium model provided the best fit to the experimental data, with average relative errors of less than 3% observed at all temperatures. The isosteric heats of CO2 adsorption onto the ammonia-modified adsorbent and onto the untreated adsorbent were determined using the Clausius-Clapeyron equation. The loading dependence of the isosteric enthalpy of CO2 adsorption over the OXA-GAC reflected an energetic heterogeneity of the adsorbent surface. The initial isosteric heats of adsorption of 70.5 kJ mol(-1) and 25.5 kJ mol(-1) correspond to the adsorption of CO2 on the modified and untreated adsorbents, respectively, and these values were in excellent agreement with the zero-coverage heats of adsorption obtained using the temperature-dependent parameters of the proposed model. (C) 2015 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
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spelling um.eprints-163522019-09-25T09:17:38Z http://eprints.um.edu.my/16352/ Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon Shafeeyan, M.S. Daud, Wan Mohd Ashri Wan Shamiri, A. Aghamohammadi, N. TA Engineering (General). Civil engineering (General) The equilibrium adsorption isotherms of carbon dioxide on a commercial granular activated carbon (GAC) and an ammonia-modified GAC (OXA-GAC) were measured using a static volumetric method. CO2 adsorption measurements were performed at three different temperatures (303, 318, and 333 K), and pressures up to 1 atm. The obtained equilibrium data were fitted to the Freundlich, Sips, and Toth isotherms using a semi-empirical approach to differentiate the contributions of physical and chemical adsorption to the total CO2 uptake. The isotherm parameters were determined independently for each mechanism by non-linear regression. To evaluate the adequacy of the fit of the isotherm models, two different error functions (i.e., the average relative error and the nonlinear regression coefficient) were calculated. The Toth semi-empirical equilibrium model provided the best fit to the experimental data, with average relative errors of less than 3% observed at all temperatures. The isosteric heats of CO2 adsorption onto the ammonia-modified adsorbent and onto the untreated adsorbent were determined using the Clausius-Clapeyron equation. The loading dependence of the isosteric enthalpy of CO2 adsorption over the OXA-GAC reflected an energetic heterogeneity of the adsorbent surface. The initial isosteric heats of adsorption of 70.5 kJ mol(-1) and 25.5 kJ mol(-1) correspond to the adsorption of CO2 on the modified and untreated adsorbents, respectively, and these values were in excellent agreement with the zero-coverage heats of adsorption obtained using the temperature-dependent parameters of the proposed model. (C) 2015 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved. Elsevier 2015 Article PeerReviewed Shafeeyan, M.S. and Daud, Wan Mohd Ashri Wan and Shamiri, A. and Aghamohammadi, N. (2015) Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon. Chemical Engineering Research and Design, 104. pp. 42-52. ISSN 0263-8762, DOI https://doi.org/10.1016/j.cherd.2015.07.018 <https://doi.org/10.1016/j.cherd.2015.07.018>. https://doi.org/10.1016/j.cherd.2015.07.018 doi:10.1016/j.cherd.2015.07.018
spellingShingle TA Engineering (General). Civil engineering (General)
Shafeeyan, M.S.
Daud, Wan Mohd Ashri Wan
Shamiri, A.
Aghamohammadi, N.
Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon
title Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon
title_full Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon
title_fullStr Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon
title_full_unstemmed Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon
title_short Adsorption equilibrium of carbon dioxide on ammonia-modified activated carbon
title_sort adsorption equilibrium of carbon dioxide on ammonia modified activated carbon
topic TA Engineering (General). Civil engineering (General)
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