Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state
Autor(a) principal: | |
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Data de Publicação: | 2013 |
Outros Autores: | , , |
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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Brazilian Journal of Chemical Engineering |
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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 |
_version_ |
1754213173884354560 |