Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling

Detalhes bibliográficos
Autor(a) principal: Pal,Dharm
Data de Publicação: 2017
Outros Autores: Thakre,Niraj, Keshav,Amit, Kumar,Awanish, Singh,Dhananjay, Kumari,Neetu
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Brazilian Journal of Chemical Engineering
Texto Completo: http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300919
Resumo: ABSTRACT Physical extraction studies of pyruvic acid from dilute aqueous solutions (0.025 kmol·m-3 to 0.200 kmol·m-3) using several pure solvents (tri-n-butylphosphate (TBP), 1-decanol, 1-octanol, toluene, Methyl-isobutylketone (MIBK), and n-heptane) and their binary mixtures are reported in this work. All the batch extraction experiments were carried out at isothermal conditions (T=303±1K) and the results are reported in terms of distribution coefficient (K D). The results obtained by the equilibrium studies of the different extraction system were correlated with solvatochromic parameters of the solvents. A linear solvation energy relationship (LSER) model was applied to interpret the extraction equilibrium which specifically considers physical interactions. The values of the LSER model parameters for the extraction system were optimized by regression technique and the model equations have been proposed. Experimental and model values were in good agreement (RMSD < 0.1).Reported outcomes are useful in the selection of a suitable extraction system and understanding the extraction mechanism for the separation of pyruvic acid from dilute aqueous solutions.
id ABEQ-1_c4753db9660d20caa6ac1b1c5c56c249
oai_identifier_str oai:scielo:S0104-66322017000300919
network_acronym_str ABEQ-1
network_name_str Brazilian Journal of Chemical Engineering
repository_id_str
spelling Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modelingSolvent ExtractionSeparationPyruvic acidLSER modelingEquilibriumABSTRACT Physical extraction studies of pyruvic acid from dilute aqueous solutions (0.025 kmol·m-3 to 0.200 kmol·m-3) using several pure solvents (tri-n-butylphosphate (TBP), 1-decanol, 1-octanol, toluene, Methyl-isobutylketone (MIBK), and n-heptane) and their binary mixtures are reported in this work. All the batch extraction experiments were carried out at isothermal conditions (T=303±1K) and the results are reported in terms of distribution coefficient (K D). The results obtained by the equilibrium studies of the different extraction system were correlated with solvatochromic parameters of the solvents. A linear solvation energy relationship (LSER) model was applied to interpret the extraction equilibrium which specifically considers physical interactions. The values of the LSER model parameters for the extraction system were optimized by regression technique and the model equations have been proposed. Experimental and model values were in good agreement (RMSD < 0.1).Reported outcomes are useful in the selection of a suitable extraction system and understanding the extraction mechanism for the separation of pyruvic acid from dilute aqueous solutions.Brazilian Society of Chemical Engineering2017-07-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300919Brazilian Journal of Chemical Engineering v.34 n.3 2017reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/0104-6632.20170343s20150276info:eu-repo/semantics/openAccessPal,DharmThakre,NirajKeshav,AmitKumar,AwanishSingh,DhananjayKumari,Neetueng2018-02-02T00:00:00Zoai:scielo:S0104-66322017000300919Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2018-02-02T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
title Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
spellingShingle Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
Pal,Dharm
Solvent Extraction
Separation
Pyruvic acid
LSER modeling
Equilibrium
title_short Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
title_full Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
title_fullStr Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
title_full_unstemmed Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
title_sort Liquid-liquid extraction equilibrium for pyruvic acid recovery: experimental data and modeling
author Pal,Dharm
author_facet Pal,Dharm
Thakre,Niraj
Keshav,Amit
Kumar,Awanish
Singh,Dhananjay
Kumari,Neetu
author_role author
author2 Thakre,Niraj
Keshav,Amit
Kumar,Awanish
Singh,Dhananjay
Kumari,Neetu
author2_role author
author
author
author
author
dc.contributor.author.fl_str_mv Pal,Dharm
Thakre,Niraj
Keshav,Amit
Kumar,Awanish
Singh,Dhananjay
Kumari,Neetu
dc.subject.por.fl_str_mv Solvent Extraction
Separation
Pyruvic acid
LSER modeling
Equilibrium
topic Solvent Extraction
Separation
Pyruvic acid
LSER modeling
Equilibrium
description ABSTRACT Physical extraction studies of pyruvic acid from dilute aqueous solutions (0.025 kmol·m-3 to 0.200 kmol·m-3) using several pure solvents (tri-n-butylphosphate (TBP), 1-decanol, 1-octanol, toluene, Methyl-isobutylketone (MIBK), and n-heptane) and their binary mixtures are reported in this work. All the batch extraction experiments were carried out at isothermal conditions (T=303±1K) and the results are reported in terms of distribution coefficient (K D). The results obtained by the equilibrium studies of the different extraction system were correlated with solvatochromic parameters of the solvents. A linear solvation energy relationship (LSER) model was applied to interpret the extraction equilibrium which specifically considers physical interactions. The values of the LSER model parameters for the extraction system were optimized by regression technique and the model equations have been proposed. Experimental and model values were in good agreement (RMSD < 0.1).Reported outcomes are useful in the selection of a suitable extraction system and understanding the extraction mechanism for the separation of pyruvic acid from dilute aqueous solutions.
publishDate 2017
dc.date.none.fl_str_mv 2017-07-01
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300919
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322017000300919
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/0104-6632.20170343s20150276
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv text/html
dc.publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
publisher.none.fl_str_mv Brazilian Society of Chemical Engineering
dc.source.none.fl_str_mv Brazilian Journal of Chemical Engineering v.34 n.3 2017
reponame:Brazilian Journal of Chemical Engineering
instname:Associação Brasileira de Engenharia Química (ABEQ)
instacron:ABEQ
instname_str Associação Brasileira de Engenharia Química (ABEQ)
instacron_str ABEQ
institution ABEQ
reponame_str Brazilian Journal of Chemical Engineering
collection Brazilian Journal of Chemical Engineering
repository.name.fl_str_mv Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)
repository.mail.fl_str_mv rgiudici@usp.br||rgiudici@usp.br
_version_ 1754213175553687552