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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Main Authors: Gulten Cetin, Sevgi Kocaoba, Goksel Akcin
Format: Article
Language:English
Published: Hindawi Limited 2013-01-01
Series:Journal of Chemistry
Online Access:http://dx.doi.org/10.1155/2013/158167
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spelling 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
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