Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state

Detalhes bibliográficos
Autor(a) principal: Freitas,A. C. D.
Data de Publicação: 2013
Outros Autores: Cunico,L. P., Aznar,M., Guirardello,R.
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=S0104-66322013000100008
Resumo: Ionic liquids (IL) have been described as novel environmentally benign solvents because of their remarkable characteristics. Numerous applications of these solvents continue to grow at an exponential rate. In this work, high pressure vapor liquid equilibria for 17 different IL + gas binary systems were modeled at different temperatures with Peng-Robinson (PR) and Soave-Redlich-Kwong (SRK) equations of state, combined with the van der Waals mixing rule with two binary interaction parameters (vdW-2). The experimental data were taken from the literature. The optimum binary interaction parameters were estimated by minimization of an objective function based on the average absolute relative deviation of liquid and vapor phases, using the modified Simplex algorithm. The solubilities of all gases studied in this work decrease as the temperature increases and increase with increasing pressure. The correlated results were highly satisfactory, with average absolute relative deviations of 2.10% and 2.25% for PR-vdW-2 and SRK-vdW-2, respectively.
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spelling Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of stateIonic liquidsVapor-liquid equilibriaPR and SRK EosIonic liquids (IL) have been described as novel environmentally benign solvents because of their remarkable characteristics. Numerous applications of these solvents continue to grow at an exponential rate. In this work, high pressure vapor liquid equilibria for 17 different IL + gas binary systems were modeled at different temperatures with Peng-Robinson (PR) and Soave-Redlich-Kwong (SRK) equations of state, combined with the van der Waals mixing rule with two binary interaction parameters (vdW-2). The experimental data were taken from the literature. The optimum binary interaction parameters were estimated by minimization of an objective function based on the average absolute relative deviation of liquid and vapor phases, using the modified Simplex algorithm. The solubilities of all gases studied in this work decrease as the temperature increases and increase with increasing pressure. The correlated results were highly satisfactory, with average absolute relative deviations of 2.10% and 2.25% for PR-vdW-2 and SRK-vdW-2, respectively.Brazilian Society of Chemical Engineering2013-03-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000100008Brazilian Journal of Chemical Engineering v.30 n.1 2013reponame:Brazilian Journal of Chemical Engineeringinstname:Associação Brasileira de Engenharia Química (ABEQ)instacron:ABEQ10.1590/S0104-66322013000100008info:eu-repo/semantics/openAccessFreitas,A. C. D.Cunico,L. P.Aznar,M.Guirardello,R.eng2013-03-01T00:00:00Zoai:scielo:S0104-66322013000100008Revistahttps://www.scielo.br/j/bjce/https://old.scielo.br/oai/scielo-oai.phprgiudici@usp.br||rgiudici@usp.br1678-43830104-6632opendoar:2013-03-01T00:00Brazilian Journal of Chemical Engineering - Associação Brasileira de Engenharia Química (ABEQ)false
dc.title.none.fl_str_mv Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
title Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
spellingShingle Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
Freitas,A. C. D.
Ionic liquids
Vapor-liquid equilibria
PR and SRK Eos
title_short Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
title_full Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
title_fullStr Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
title_full_unstemmed Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
title_sort Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
author Freitas,A. C. D.
author_facet Freitas,A. C. D.
Cunico,L. P.
Aznar,M.
Guirardello,R.
author_role author
author2 Cunico,L. P.
Aznar,M.
Guirardello,R.
author2_role author
author
author
dc.contributor.author.fl_str_mv Freitas,A. C. D.
Cunico,L. P.
Aznar,M.
Guirardello,R.
dc.subject.por.fl_str_mv Ionic liquids
Vapor-liquid equilibria
PR and SRK Eos
topic Ionic liquids
Vapor-liquid equilibria
PR and SRK Eos
description Ionic liquids (IL) have been described as novel environmentally benign solvents because of their remarkable characteristics. Numerous applications of these solvents continue to grow at an exponential rate. In this work, high pressure vapor liquid equilibria for 17 different IL + gas binary systems were modeled at different temperatures with Peng-Robinson (PR) and Soave-Redlich-Kwong (SRK) equations of state, combined with the van der Waals mixing rule with two binary interaction parameters (vdW-2). The experimental data were taken from the literature. The optimum binary interaction parameters were estimated by minimization of an objective function based on the average absolute relative deviation of liquid and vapor phases, using the modified Simplex algorithm. The solubilities of all gases studied in this work decrease as the temperature increases and increase with increasing pressure. The correlated results were highly satisfactory, with average absolute relative deviations of 2.10% and 2.25% for PR-vdW-2 and SRK-vdW-2, respectively.
publishDate 2013
dc.date.none.fl_str_mv 2013-03-01
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=S0104-66322013000100008
url http://old.scielo.br/scielo.php?script=sci_arttext&pid=S0104-66322013000100008
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv 10.1590/S0104-66322013000100008
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.30 n.1 2013
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
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