Removal of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbents
In this study, adsorbents were produced from sewage sludge via chemical and thermal activation processes. Experiments were carried out in a tubular furnace at the heating rate of 20˚C min-1 and temperature of 550 ˚C with a nitrogen flow rate of 400 mL min-1 for 1 h. Dye adsorption experimen...
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Association of the Chemical Engineers of Serbia
2016-01-01
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doaj-1c2107897aa44facaed6299a39225aa92020-11-24T23:18:49ZengAssociation of the Chemical Engineers of SerbiaChemical Industry and Chemical Engineering Quarterly1451-93722217-74342016-01-0122216717910.2298/CICEQ141128029O1451-93721500029ORemoval of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbentsÖzçimen Didem0Salan Tufan1Yıldız Technical University, Faculty of Chemical and Metallurgical Engineering, Department of Bioengineering, Istanbul, TurkeyKahramanmaras Sutcu Imam University, Department of Material Science and Engineering, Kahramanmaras, TurkeyIn this study, adsorbents were produced from sewage sludge via chemical and thermal activation processes. Experiments were carried out in a tubular furnace at the heating rate of 20˚C min-1 and temperature of 550 ˚C with a nitrogen flow rate of 400 mL min-1 for 1 h. Dye adsorption experiments were performed with Remazol Brilliant Blue R for its several concentrations under batch equilibrium conditions by comparing sewage sludge based adsorbents with raw material and a commercial activated carbon. Maximum adsorption capacities of carbonized sewage sludge (CSWS) and activated sewage sludge (ASWS) were found as 7.413 mg g-1 and 9.376 mg g-1 for 100 mg L-1 dye solution, whereas commercial activated carbon had a capacity of 11.561 mg g-1. Freundlich and Langmuir isotherms were used to explain the adsorption mechanism together with pseudo-first-order and pseudo-second-order kinetic models. Langmuir isotherm, which had adsorption capacities of 34.60 mg g-1 (CSWS) and 72.99 mg g-1 (ASWS), provided better fit to the equilibrium data than that of Freundlich isotherm. Pseudo second-order, model which had adsorption capacities of 7.451 mg g-1 (CSWS) and 9.319 mg g-1 (ASWS), was very favorable to explain the adsorption kinetics of the dye with high regression coefficients.http://www.doiserbia.nb.rs/img/doi/1451-9372/2016/1451-93721500029O.pdfsewage sludgecarbonizationactivated carbonadsorptionRemazol Brilliant Blue R |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Özçimen Didem Salan Tufan |
spellingShingle |
Özçimen Didem Salan Tufan Removal of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbents Chemical Industry and Chemical Engineering Quarterly sewage sludge carbonization activated carbon adsorption Remazol Brilliant Blue R |
author_facet |
Özçimen Didem Salan Tufan |
author_sort |
Özçimen Didem |
title |
Removal of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbents |
title_short |
Removal of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbents |
title_full |
Removal of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbents |
title_fullStr |
Removal of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbents |
title_full_unstemmed |
Removal of reactive dye Remazol Brilliant Blue R from aqueous solutions by using anaerobically digested sewage sludge based adsorbents |
title_sort |
removal of reactive dye remazol brilliant blue r from aqueous solutions by using anaerobically digested sewage sludge based adsorbents |
publisher |
Association of the Chemical Engineers of Serbia |
series |
Chemical Industry and Chemical Engineering Quarterly |
issn |
1451-9372 2217-7434 |
publishDate |
2016-01-01 |
description |
In this study, adsorbents were produced from sewage sludge via chemical and
thermal activation processes. Experiments were carried out in a tubular
furnace at the heating rate of 20˚C min-1 and temperature of 550 ˚C with a
nitrogen flow rate of 400 mL min-1 for 1 h. Dye adsorption experiments were
performed with Remazol Brilliant Blue R for its several concentrations under
batch equilibrium conditions by comparing sewage sludge based adsorbents with
raw material and a commercial activated carbon. Maximum adsorption capacities
of carbonized sewage sludge (CSWS) and activated sewage sludge (ASWS) were
found as 7.413 mg g-1 and 9.376 mg g-1 for 100 mg L-1 dye solution, whereas
commercial activated carbon had a capacity of 11.561 mg g-1. Freundlich and
Langmuir isotherms were used to explain the adsorption mechanism together
with pseudo-first-order and pseudo-second-order kinetic models. Langmuir
isotherm, which had adsorption capacities of 34.60 mg g-1 (CSWS) and 72.99 mg
g-1 (ASWS), provided better fit to the equilibrium data than that of
Freundlich isotherm. Pseudo second-order, model which had adsorption
capacities of 7.451 mg g-1 (CSWS) and 9.319 mg g-1 (ASWS), was very favorable
to explain the adsorption kinetics of the dye with high regression
coefficients. |
topic |
sewage sludge carbonization activated carbon adsorption Remazol Brilliant Blue R |
url |
http://www.doiserbia.nb.rs/img/doi/1451-9372/2016/1451-93721500029O.pdf |
work_keys_str_mv |
AT ozcimendidem removalofreactivedyeremazolbrilliantbluerfromaqueoussolutionsbyusinganaerobicallydigestedsewagesludgebasedadsorbents AT salantufan removalofreactivedyeremazolbrilliantbluerfromaqueoussolutionsbyusinganaerobicallydigestedsewagesludgebasedadsorbents |
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