Adsorption of congo red onto bottom ash

The adsorption of Congo Red (CR) onto Bottom Ash (BA) was studied in batch process. The objective of this study was to compare the adsorption capacity between physical-activated BA and untreated BA for removal of CR. Bottom ash was modified by undergoing pyrolysis process where it was activated in t...

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Published in:Journal of Applied Sciences
Main Author: Saleh S.M.; Maarof H.I.; Rahim S.N.S.A.; Nasuha N.
Format: Article
Language:English
Published: 2012
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-84864019513&doi=10.3923%2fjas.2012.1181.1185&partnerID=40&md5=c9564ec2d76130013226d175c5675d1a
id 2-s2.0-84864019513
spelling 2-s2.0-84864019513
Saleh S.M.; Maarof H.I.; Rahim S.N.S.A.; Nasuha N.
Adsorption of congo red onto bottom ash
2012
Journal of Applied Sciences
12
11
10.3923/jas.2012.1181.1185
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84864019513&doi=10.3923%2fjas.2012.1181.1185&partnerID=40&md5=c9564ec2d76130013226d175c5675d1a
The adsorption of Congo Red (CR) onto Bottom Ash (BA) was studied in batch process. The objective of this study was to compare the adsorption capacity between physical-activated BA and untreated BA for removal of CR. Bottom ash was modified by undergoing pyrolysis process where it was activated in the vertical tubular furnace with the flowing of carbon dioxide at 700°C. Then, the adsorption process was carried out on an orbital shaker at 150 rpm for 24 h. Adsorption equilibrium of CR was attained after 24 h of contact time. The equilibrium adsorption data were interpreted by using Langmuir and Freundlich models. The data shows that physical-activated BA and untreated BA were well described by the Freundlich model. In addition, the amount of CR adsorbed on the adsorbent, q e was higher using physical-activated BA (106.61 mg g -1) as compared to untreated BA (24.36 mg g -1). In conclusion, the modification of BA using pyrolysis process offered a significant affects to the performance of the BA for removal of CR. © 2012 Asian Network for Scientific Information.

18125662
English
Article

author Saleh S.M.; Maarof H.I.; Rahim S.N.S.A.; Nasuha N.
spellingShingle Saleh S.M.; Maarof H.I.; Rahim S.N.S.A.; Nasuha N.
Adsorption of congo red onto bottom ash
author_facet Saleh S.M.; Maarof H.I.; Rahim S.N.S.A.; Nasuha N.
author_sort Saleh S.M.; Maarof H.I.; Rahim S.N.S.A.; Nasuha N.
title Adsorption of congo red onto bottom ash
title_short Adsorption of congo red onto bottom ash
title_full Adsorption of congo red onto bottom ash
title_fullStr Adsorption of congo red onto bottom ash
title_full_unstemmed Adsorption of congo red onto bottom ash
title_sort Adsorption of congo red onto bottom ash
publishDate 2012
container_title Journal of Applied Sciences
container_volume 12
container_issue 11
doi_str_mv 10.3923/jas.2012.1181.1185
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-84864019513&doi=10.3923%2fjas.2012.1181.1185&partnerID=40&md5=c9564ec2d76130013226d175c5675d1a
description The adsorption of Congo Red (CR) onto Bottom Ash (BA) was studied in batch process. The objective of this study was to compare the adsorption capacity between physical-activated BA and untreated BA for removal of CR. Bottom ash was modified by undergoing pyrolysis process where it was activated in the vertical tubular furnace with the flowing of carbon dioxide at 700°C. Then, the adsorption process was carried out on an orbital shaker at 150 rpm for 24 h. Adsorption equilibrium of CR was attained after 24 h of contact time. The equilibrium adsorption data were interpreted by using Langmuir and Freundlich models. The data shows that physical-activated BA and untreated BA were well described by the Freundlich model. In addition, the amount of CR adsorbed on the adsorbent, q e was higher using physical-activated BA (106.61 mg g -1) as compared to untreated BA (24.36 mg g -1). In conclusion, the modification of BA using pyrolysis process offered a significant affects to the performance of the BA for removal of CR. © 2012 Asian Network for Scientific Information.
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