Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column

Abstract This work studied the removal of paracetamol through the adsorption process using the granular activated carbon. The results indicated that it was possible to obtain 95% of removal under the experimental conditions of pH 6, 120 min of process and 5 g L−1 of solid adsorbent. The kinetic mode...

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Main Authors: Nathalia Krummenauer Haro, Ivone Vanessa Jurado Dávila, Keila Guerra Pacheco Nunes, Marcela Andrea Espina de Franco, Nilson Romeu Marcilio, Liliana Amaral Féris
Format: Article
Language:English
Published: SpringerOpen 2021-02-01
Series:Applied Water Science
Subjects:
Online Access:https://doi.org/10.1007/s13201-020-01346-5
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spelling doaj-f400f94bfe4e474cad9be0af1e87c65d2021-02-07T12:47:55ZengSpringerOpenApplied Water Science2190-54872190-54952021-02-011121910.1007/s13201-020-01346-5Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed columnNathalia Krummenauer Haro0Ivone Vanessa Jurado Dávila1Keila Guerra Pacheco Nunes2Marcela Andrea Espina de Franco3Nilson Romeu Marcilio4Liliana Amaral Féris5Engineering School, UniRitter - Laureate International UniversitiesDepartment of Chemical Engineering, Federal University of Rio Grande Do Sul (UFRGS)Department of Chemical Engineering, Federal University of Rio Grande Do Sul (UFRGS)Department of Chemical Engineering, Federal University of Rio Grande Do Sul (UFRGS)Department of Chemical Engineering, Federal University of Rio Grande Do Sul (UFRGS)Department of Chemical Engineering, Federal University of Rio Grande Do Sul (UFRGS)Abstract This work studied the removal of paracetamol through the adsorption process using the granular activated carbon. The results indicated that it was possible to obtain 95% of removal under the experimental conditions of pH 6, 120 min of process and 5 g L−1 of solid adsorbent. The kinetic model that best fit the experimental data was the pseudo-first order. The isotherm model that best fit the experimental data was the Sips. The thermodynamic tests indicated that the adsorption process was favorable and spontaneous and confirmed the endothermic nature of the process. In fixed bed column adsorption, the best operating condition found was obtained using the flow rate of 3 mL min−1 and bed mass equal to 0.5 g. In this case, the system presented the highest volume of treated PAR effluent, of 810 mL per gram of carbon in the bed, besides a longer rupture time and bed saturation.https://doi.org/10.1007/s13201-020-01346-5Pharmaceuticals compoundsParacetamolAdsorptionActivated carbonFixed-bed column
collection DOAJ
language English
format Article
sources DOAJ
author Nathalia Krummenauer Haro
Ivone Vanessa Jurado Dávila
Keila Guerra Pacheco Nunes
Marcela Andrea Espina de Franco
Nilson Romeu Marcilio
Liliana Amaral Féris
spellingShingle Nathalia Krummenauer Haro
Ivone Vanessa Jurado Dávila
Keila Guerra Pacheco Nunes
Marcela Andrea Espina de Franco
Nilson Romeu Marcilio
Liliana Amaral Féris
Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column
Applied Water Science
Pharmaceuticals compounds
Paracetamol
Adsorption
Activated carbon
Fixed-bed column
author_facet Nathalia Krummenauer Haro
Ivone Vanessa Jurado Dávila
Keila Guerra Pacheco Nunes
Marcela Andrea Espina de Franco
Nilson Romeu Marcilio
Liliana Amaral Féris
author_sort Nathalia Krummenauer Haro
title Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column
title_short Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column
title_full Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column
title_fullStr Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column
title_full_unstemmed Kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column
title_sort kinetic, equilibrium and thermodynamic studies of the adsorption of paracetamol in activated carbon in batch model and fixed-bed column
publisher SpringerOpen
series Applied Water Science
issn 2190-5487
2190-5495
publishDate 2021-02-01
description Abstract This work studied the removal of paracetamol through the adsorption process using the granular activated carbon. The results indicated that it was possible to obtain 95% of removal under the experimental conditions of pH 6, 120 min of process and 5 g L−1 of solid adsorbent. The kinetic model that best fit the experimental data was the pseudo-first order. The isotherm model that best fit the experimental data was the Sips. The thermodynamic tests indicated that the adsorption process was favorable and spontaneous and confirmed the endothermic nature of the process. In fixed bed column adsorption, the best operating condition found was obtained using the flow rate of 3 mL min−1 and bed mass equal to 0.5 g. In this case, the system presented the highest volume of treated PAR effluent, of 810 mL per gram of carbon in the bed, besides a longer rupture time and bed saturation.
topic Pharmaceuticals compounds
Paracetamol
Adsorption
Activated carbon
Fixed-bed column
url https://doi.org/10.1007/s13201-020-01346-5
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