Export Ready — 

High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane

Bibliographic Details
Main Author: Dutra A.C.
Publication Date: 2024
Other Authors: Guindani C., Beltrame J.M., da Silva A., Rebelatto E.A., Oliveira J.V., Mayer, Diego Alex
Format: Article
Language: eng
Source: Repositório Institucional da Udesc
dARK ID: ark:/33523/001300000n3n0
Download full: https://repositorio.udesc.br/handle/UDESC/2081
Summary: © 2023 Elsevier B.V.The growing interest in producing biocompatible polymers, free of any kind of toxic residues, increasingly encourages the development of researches on clean processes. The use of supercritical carbon dioxide, replacing organic solvents, has shown to be a green alternative to traditional polymerization processes. Aiming at providing fundamental information to conduct polymerization reactions in supercritical carbon dioxide, this work reports experimental phase equilibrium data for the quinary system involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane. The experiments were performed using a variable-volume view cell over the temperature range from 313.15 to 343.15 K, and different mass fractions of carbon dioxide in relation to monomers and copolymer (globalide + ε-caprolactone + poly(globalide-co-ε-caprolactone)) and a fixed mass ratio of dichloromethane to globalide + ε-caprolactone + poly(globalide-co-ε-caprolactone), of 1:1, were studied. To simulate a polymerization reaction of ε-caprolactone + globalide to poly(globalide-co-ε-caprolactone) different monomers to copolymer conversions (1.25, 2.50, 3.75 and 5.00%) were analyzed. Phase transition of vapor-liquid bubble point (VLE-BP), in a pressure range from 6.31 to 12.58 MPa, and liquid-liquid (LLE), in a pressure range from 10.49 to 26.50 MPa, are reported, together with the lower critical solution temperature (LCST) behavior observed for the systems investigated. The pressure of the systems varied from 6.31 MPa to 26.50 MPa.
id UDESC-2_e49fcc3e15c199be63394896d8eb9a8b
oai_identifier_str oai:repositorio.udesc.br:UDESC/2081
network_acronym_str UDESC-2
network_name_str Repositório Institucional da Udesc
repository_id_str 6391
spelling High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane© 2023 Elsevier B.V.The growing interest in producing biocompatible polymers, free of any kind of toxic residues, increasingly encourages the development of researches on clean processes. The use of supercritical carbon dioxide, replacing organic solvents, has shown to be a green alternative to traditional polymerization processes. Aiming at providing fundamental information to conduct polymerization reactions in supercritical carbon dioxide, this work reports experimental phase equilibrium data for the quinary system involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane. The experiments were performed using a variable-volume view cell over the temperature range from 313.15 to 343.15 K, and different mass fractions of carbon dioxide in relation to monomers and copolymer (globalide + ε-caprolactone + poly(globalide-co-ε-caprolactone)) and a fixed mass ratio of dichloromethane to globalide + ε-caprolactone + poly(globalide-co-ε-caprolactone), of 1:1, were studied. To simulate a polymerization reaction of ε-caprolactone + globalide to poly(globalide-co-ε-caprolactone) different monomers to copolymer conversions (1.25, 2.50, 3.75 and 5.00%) were analyzed. Phase transition of vapor-liquid bubble point (VLE-BP), in a pressure range from 6.31 to 12.58 MPa, and liquid-liquid (LLE), in a pressure range from 10.49 to 26.50 MPa, are reported, together with the lower critical solution temperature (LCST) behavior observed for the systems investigated. The pressure of the systems varied from 6.31 MPa to 26.50 MPa.2024-12-05T13:48:30Z2024info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article0378-381210.1016/j.fluid.2023.113932https://repositorio.udesc.br/handle/UDESC/2081ark:/33523/001300000n3n0Fluid Phase Equilibria576Dutra A.C.Guindani C.Beltrame J.M.da Silva A.Rebelatto E.A.Oliveira J.V.Mayer, Diego Alexengreponame:Repositório Institucional da Udescinstname:Universidade do Estado de Santa Catarina (UDESC)instacron:UDESCinfo:eu-repo/semantics/openAccess2024-12-07T20:37:44Zoai:repositorio.udesc.br:UDESC/2081Biblioteca Digital de Teses e Dissertaçõeshttps://pergamumweb.udesc.br/biblioteca/index.phpPRIhttps://repositorio-api.udesc.br/server/oai/requestri@udesc.bropendoar:63912024-12-07T20:37:44Repositório Institucional da Udesc - Universidade do Estado de Santa Catarina (UDESC)false
dc.title.none.fl_str_mv High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
title High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
spellingShingle High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
Dutra A.C.
title_short High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
title_full High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
title_fullStr High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
title_full_unstemmed High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
title_sort High-pressure phase equilibrium data for systems involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane
author Dutra A.C.
author_facet Dutra A.C.
Guindani C.
Beltrame J.M.
da Silva A.
Rebelatto E.A.
Oliveira J.V.
Mayer, Diego Alex
author_role author
author2 Guindani C.
Beltrame J.M.
da Silva A.
Rebelatto E.A.
Oliveira J.V.
Mayer, Diego Alex
author2_role author
author
author
author
author
author
dc.contributor.author.fl_str_mv Dutra A.C.
Guindani C.
Beltrame J.M.
da Silva A.
Rebelatto E.A.
Oliveira J.V.
Mayer, Diego Alex
description © 2023 Elsevier B.V.The growing interest in producing biocompatible polymers, free of any kind of toxic residues, increasingly encourages the development of researches on clean processes. The use of supercritical carbon dioxide, replacing organic solvents, has shown to be a green alternative to traditional polymerization processes. Aiming at providing fundamental information to conduct polymerization reactions in supercritical carbon dioxide, this work reports experimental phase equilibrium data for the quinary system involving carbon dioxide, globalide, ε-caprolactone, poly(globalide-co-ε-caprolactone) and dichloromethane. The experiments were performed using a variable-volume view cell over the temperature range from 313.15 to 343.15 K, and different mass fractions of carbon dioxide in relation to monomers and copolymer (globalide + ε-caprolactone + poly(globalide-co-ε-caprolactone)) and a fixed mass ratio of dichloromethane to globalide + ε-caprolactone + poly(globalide-co-ε-caprolactone), of 1:1, were studied. To simulate a polymerization reaction of ε-caprolactone + globalide to poly(globalide-co-ε-caprolactone) different monomers to copolymer conversions (1.25, 2.50, 3.75 and 5.00%) were analyzed. Phase transition of vapor-liquid bubble point (VLE-BP), in a pressure range from 6.31 to 12.58 MPa, and liquid-liquid (LLE), in a pressure range from 10.49 to 26.50 MPa, are reported, together with the lower critical solution temperature (LCST) behavior observed for the systems investigated. The pressure of the systems varied from 6.31 MPa to 26.50 MPa.
publishDate 2024
dc.date.none.fl_str_mv 2024-12-05T13:48:30Z
2024
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv 0378-3812
10.1016/j.fluid.2023.113932
https://repositorio.udesc.br/handle/UDESC/2081
dc.identifier.dark.fl_str_mv ark:/33523/001300000n3n0
identifier_str_mv 0378-3812
10.1016/j.fluid.2023.113932
ark:/33523/001300000n3n0
url https://repositorio.udesc.br/handle/UDESC/2081
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Fluid Phase Equilibria
576
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.source.none.fl_str_mv reponame:Repositório Institucional da Udesc
instname:Universidade do Estado de Santa Catarina (UDESC)
instacron:UDESC
instname_str Universidade do Estado de Santa Catarina (UDESC)
instacron_str UDESC
institution UDESC
reponame_str Repositório Institucional da Udesc
collection Repositório Institucional da Udesc
repository.name.fl_str_mv Repositório Institucional da Udesc - Universidade do Estado de Santa Catarina (UDESC)
repository.mail.fl_str_mv ri@udesc.br
_version_ 1842258149352931328