Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger
The process in this study was conducted on removal of chromium(III) in a solution simulating a typical spent chrome tanning bath by the resin having matrix of styrene-divinylbenzene-based macroporous sulphonate, Amberjet 1200Na. The column experiments were carried out with the bed volumes of the res...
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Series: | Journal of Chemistry |
Online Access: | http://dx.doi.org/10.1155/2013/158167 |
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doaj-27510875c7434711b500434d56d7c3bb2020-11-25T01:05:09ZengHindawi LimitedJournal of Chemistry2090-90632090-90712013-01-01201310.1155/2013/158167158167Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation ExchangerGulten Cetin0Sevgi Kocaoba1Goksel Akcin2Chemistry Department, Faculty of Science and Art, Yıldız Technical University, Campus of Davutpasa, Esenler, 34220 Istanbul, TurkeyChemistry Department, Faculty of Science and Art, Yıldız Technical University, Campus of Davutpasa, Esenler, 34220 Istanbul, TurkeyChemistry Department, Faculty of Science and Art, Yıldız Technical University, Campus of Davutpasa, Esenler, 34220 Istanbul, TurkeyThe process in this study was conducted on removal of chromium(III) in a solution simulating a typical spent chrome tanning bath by the resin having matrix of styrene-divinylbenzene-based macroporous sulphonate, Amberjet 1200Na. The column experiments were carried out with the bed volumes of the resin as 751 mL and 1016 mL for different installation systems of the laboratory-scale pilot plant. The feeding solutions in the bed volumes of 200 and 190 were used for each installation system. The regeneration behaviour of the resin was determined by using reverse regeneration procedure with the solution of hydrogen peroxide in alkaline. The regeneration kinetics of the exhausted resin was examined with a range of the solutions having different concentration series of the alkaline hydrogen peroxide. The solutions of the basic chromium sulphate were recycled for each installation system following the regeneration cycles. The chromium ions in effluent were quantitatively eluted, and satisfactory removal of chromium(III) and recovery of chromium(VI) were achieved.http://dx.doi.org/10.1155/2013/158167 |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Gulten Cetin Sevgi Kocaoba Goksel Akcin |
spellingShingle |
Gulten Cetin Sevgi Kocaoba Goksel Akcin Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger Journal of Chemistry |
author_facet |
Gulten Cetin Sevgi Kocaoba Goksel Akcin |
author_sort |
Gulten Cetin |
title |
Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger |
title_short |
Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger |
title_full |
Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger |
title_fullStr |
Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger |
title_full_unstemmed |
Removal and Recovery of Chromium from Solutions Simulating Tannery Wastewater by Strong Acid Cation Exchanger |
title_sort |
removal and recovery of chromium from solutions simulating tannery wastewater by strong acid cation exchanger |
publisher |
Hindawi Limited |
series |
Journal of Chemistry |
issn |
2090-9063 2090-9071 |
publishDate |
2013-01-01 |
description |
The process in this study was conducted on removal of chromium(III) in a solution simulating a typical spent chrome tanning bath by the resin having matrix of styrene-divinylbenzene-based macroporous sulphonate, Amberjet 1200Na. The column experiments were carried out with the bed volumes of the resin as 751 mL and 1016 mL for different installation systems of the laboratory-scale pilot plant. The feeding solutions in the bed volumes of 200 and 190 were used for each installation system. The regeneration behaviour of the resin was determined by using reverse regeneration procedure with the solution of hydrogen peroxide in alkaline. The regeneration kinetics of the exhausted resin was examined with a range of the solutions having different concentration series of the alkaline hydrogen peroxide. The solutions of the basic chromium sulphate were recycled for each installation system following the regeneration cycles. The chromium ions in effluent were quantitatively eluted, and satisfactory removal of chromium(III) and recovery of chromium(VI) were achieved. |
url |
http://dx.doi.org/10.1155/2013/158167 |
work_keys_str_mv |
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