Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies

Sulphuric acid (H2SO4) was utilized as an activator for the preparation of activated carbon from a biomass solid waste, coconut leaves. The sulphuric acid-treated activated carbon (SAC) was used as low-cost adsorbent for the removal of methylene blue (MB) cationic dye from aqueous solution. Adsorpti...

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Published in:Desalination and Water Treatment
Main Author: Jawad A.H.; Rashid R.A.; Ishak M.A.M.; Wilson L.D.
Format: Article
Language:English
Published: Taylor and Francis Inc. 2016
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-84958039789&doi=10.1080%2f19443994.2016.1144534&partnerID=40&md5=41bc07f2d2fab5a5bbdfe9b740a98ee4
id 2-s2.0-84958039789
spelling 2-s2.0-84958039789
Jawad A.H.; Rashid R.A.; Ishak M.A.M.; Wilson L.D.
Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
2016
Desalination and Water Treatment
57
52
10.1080/19443994.2016.1144534
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84958039789&doi=10.1080%2f19443994.2016.1144534&partnerID=40&md5=41bc07f2d2fab5a5bbdfe9b740a98ee4
Sulphuric acid (H2SO4) was utilized as an activator for the preparation of activated carbon from a biomass solid waste, coconut leaves. The sulphuric acid-treated activated carbon (SAC) was used as low-cost adsorbent for the removal of methylene blue (MB) cationic dye from aqueous solution. Adsorption of MB using SAC from aqueous solution under equilibrium and kinetic conditions in batch mode was evaluated by varying adsorbent dose (0.2–2.5 g/L), solution pH (3–11), initial dye concentration (30–400 mg/L), contact time (0–180 min) and temperature (303–323 K). The Langmuir isotherm model showed better fit to the equilibrium data than the Freundlich model. The adsorption capacity (qm) of SAC increased with temperature where qm varied as follows: 126.9 (303 K), 137.0 (313 K) and 149.3 mg/g (323 K). The kinetic uptake results were well described by the pseudo-second-order (PSO) kinetic for each temperatures. The thermodynamic adsorption parameters (∆G°, ∆H° and ∆S°) were driven by favourable entropic factors, in accordance with the low activation energy (29.70 kJ/mol) of the system. This study reveals that SAC is an effective and low-cost adsorbent for the removal of MB from aqueous solution. © 2016 Balaban Desalination Publications. All rights reserved.
Taylor and Francis Inc.
19443994
English
Article

author Jawad A.H.; Rashid R.A.; Ishak M.A.M.; Wilson L.D.
spellingShingle Jawad A.H.; Rashid R.A.; Ishak M.A.M.; Wilson L.D.
Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
author_facet Jawad A.H.; Rashid R.A.; Ishak M.A.M.; Wilson L.D.
author_sort Jawad A.H.; Rashid R.A.; Ishak M.A.M.; Wilson L.D.
title Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
title_short Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
title_full Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
title_fullStr Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
title_full_unstemmed Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
title_sort Adsorption of methylene blue onto activated carbon developed from biomass waste by H2SO4 activation: kinetic, equilibrium and thermodynamic studies
publishDate 2016
container_title Desalination and Water Treatment
container_volume 57
container_issue 52
doi_str_mv 10.1080/19443994.2016.1144534
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-84958039789&doi=10.1080%2f19443994.2016.1144534&partnerID=40&md5=41bc07f2d2fab5a5bbdfe9b740a98ee4
description Sulphuric acid (H2SO4) was utilized as an activator for the preparation of activated carbon from a biomass solid waste, coconut leaves. The sulphuric acid-treated activated carbon (SAC) was used as low-cost adsorbent for the removal of methylene blue (MB) cationic dye from aqueous solution. Adsorption of MB using SAC from aqueous solution under equilibrium and kinetic conditions in batch mode was evaluated by varying adsorbent dose (0.2–2.5 g/L), solution pH (3–11), initial dye concentration (30–400 mg/L), contact time (0–180 min) and temperature (303–323 K). The Langmuir isotherm model showed better fit to the equilibrium data than the Freundlich model. The adsorption capacity (qm) of SAC increased with temperature where qm varied as follows: 126.9 (303 K), 137.0 (313 K) and 149.3 mg/g (323 K). The kinetic uptake results were well described by the pseudo-second-order (PSO) kinetic for each temperatures. The thermodynamic adsorption parameters (∆G°, ∆H° and ∆S°) were driven by favourable entropic factors, in accordance with the low activation energy (29.70 kJ/mol) of the system. This study reveals that SAC is an effective and low-cost adsorbent for the removal of MB from aqueous solution. © 2016 Balaban Desalination Publications. All rights reserved.
publisher Taylor and Francis Inc.
issn 19443994
language English
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