Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different Solvents

The extraction of L(+) tartaric acid from aqueous solutions by amberlite LA-2 is a secondary amine mixture in different diluent solvents. Extraction equilibria of L(+) tartaric acid by amberlite LA-2 in 1-octanol, cyclohexane, isooctane, hexane, methyl isobutyl ketone (MIBK) solvents at temperature...

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Main Authors: I. Inci, Y. S. Asçi, A. F. Tuyun
Format: Article
Language:English
Published: Wiley 2011-01-01
Series:E-Journal of Chemistry
Online Access:http://dx.doi.org/10.1155/2011/167945
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author I. Inci
Y. S. Asçi
A. F. Tuyun
author_facet I. Inci
Y. S. Asçi
A. F. Tuyun
author_sort I. Inci
collection DOAJ
description The extraction of L(+) tartaric acid from aqueous solutions by amberlite LA-2 is a secondary amine mixture in different diluent solvents. Extraction equilibria of L(+) tartaric acid by amberlite LA-2 in 1-octanol, cyclohexane, isooctane, hexane, methyl isobutyl ketone (MIBK) solvents at temperature 298.15 K have been measured. The batch extraction experiments distribution coefficients (D), loading factors ( Z) and extraction efficiency (E) were calculated. The maximum removal of L(+) tartaric acid is 91 % with MIBK and 0.92 mol.L-1 initial concentration of Amberlite LA-2.
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publishDate 2011-01-01
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series E-Journal of Chemistry
spelling doaj-art-ac3bc5fbaf7142a5b7308e097e4a62952025-08-20T02:20:23ZengWileyE-Journal of Chemistry0973-49452090-98102011-01-018S1S509S51510.1155/2011/167945Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different SolventsI. Inci0Y. S. Asçi1A. F. Tuyun2Chemical Engineering Department, Faculty of Engineering, İstanbul University, 34320, İstanbul, TurkeyChemical Engineering Department, Faculty of Engineering, İstanbul University, 34320, İstanbul, TurkeyDepartment of Chemical Engineering, Engineering & Architecture Faculty, Beykent University, Ayazağa, Istanbul, TurkeyThe extraction of L(+) tartaric acid from aqueous solutions by amberlite LA-2 is a secondary amine mixture in different diluent solvents. Extraction equilibria of L(+) tartaric acid by amberlite LA-2 in 1-octanol, cyclohexane, isooctane, hexane, methyl isobutyl ketone (MIBK) solvents at temperature 298.15 K have been measured. The batch extraction experiments distribution coefficients (D), loading factors ( Z) and extraction efficiency (E) were calculated. The maximum removal of L(+) tartaric acid is 91 % with MIBK and 0.92 mol.L-1 initial concentration of Amberlite LA-2.http://dx.doi.org/10.1155/2011/167945
spellingShingle I. Inci
Y. S. Asçi
A. F. Tuyun
Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different Solvents
E-Journal of Chemistry
title Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different Solvents
title_full Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different Solvents
title_fullStr Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different Solvents
title_full_unstemmed Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different Solvents
title_short Reactive Extraction of L (+) Tartaric Acid by Amberlite LA-2 in Different Solvents
title_sort reactive extraction of l tartaric acid by amberlite la 2 in different solvents
url http://dx.doi.org/10.1155/2011/167945
work_keys_str_mv AT iinci reactiveextractionofltartaricacidbyamberlitela2indifferentsolvents
AT ysasci reactiveextractionofltartaricacidbyamberlitela2indifferentsolvents
AT aftuyun reactiveextractionofltartaricacidbyamberlitela2indifferentsolvents