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A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol

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Resumo:The production of methyl and ethyl esters of fatty acids is of great industrial interest, considering the direct application of these esters as biodiesel. For biodiesel purification and by-products recovery processes design and optimization, the prediction of the phase behaviour of mixtures containing fatty esters, alcohols, glycerol and water is of utmost importance. In this work we show the capability of a A-UNIFAC to correlate and predict phase behaviour of these mixtures. This GE model is an extension of UNIFAC that explicitly includes association effects between groups based on the statistical Wertheim theory [1]. For the water-esters binary systems, the residual and association parameters have been previously estimated using low pressure VLE data [1]. The use of these parameters to predict liquid-liquid equilibrium results in good agreement with experimental information on binaries of water with acetic, octanoic or dodecanoic acids methyl esters. The association effect in methanol and glycerol are represented with the same hydrogen bonding hydroxyl groups (OH) with two associating sites, one group in methanol and three in glycerol. For the residual contribution, both molecules are considered as molecular groups (CH3OH and C3H8O3). The residual interaction parameters between CH3OH and C3H8O3 were obtained by fitting isothermal liquid-liquid equilibrium data on the ternary system dodecanoic acid methyl ester-methanol–glycerol [2]. The glycerol/paraffin (C3H8O3/CH2) and glycerol/ester (C3H8O3/CCOO) interaction parameters were estimated by fitting experimental data on liquid-liquid equilibrium and infinite dilution activity coefficients of the binary systems dodecanoic acid methyl ester-glycerol and hexanoic acid methyl ester-glycerol between 320-438 K [2]. A-UNIFAC with the final set of parameters is able to predict with good agreement experimental data on binary and ternary liquid-liquid equilibria of glycerol + methanol + fatty esters as well as infinite dilution activity coefficient for this system. References [1] O. Ferreira, E.A. Macedo, S.B. Bottini, Fluid Phase Equilib. 227 (2005) 165-176. [2] F.M. Korgitzsch, Study of Phase Equilibria as a Fundament for the Refinement of Vegetable and Animal Fats and Oils. Ph.D. Dissertation, TU Berlin, 1993.
Autores principais:Garrido, Nuno M.
Outros Autores:Ferreira, Olga; Lugo, Rafael; Hemptinne, Jean-Charles de; Macedo, Eugénia A.; Bottini, Susana B.
Ano:2009
País:Portugal
Tipo de documento:comunicação em conferência
Tipo de acesso:acesso aberto
Instituição associada:Universidade Politécnica de Bragança
Idioma:inglês
Origem:Biblioteca Digital da UPB
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author Garrido, Nuno M.
author2 Ferreira, Olga
Lugo, Rafael
Hemptinne, Jean-Charles de
Macedo, Eugénia A.
Bottini, Susana B.
author2_role author
author
author
author
author
author_facet Garrido, Nuno M.
Ferreira, Olga
Lugo, Rafael
Hemptinne, Jean-Charles de
Macedo, Eugénia A.
Bottini, Susana B.
author_role author
contributor_name_str_mv Biblioteca Digital da UPB
country_str PT
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datacite.contributors.contributor.contributorName.fl_str_mv Biblioteca Digital da UPB
datacite.creators.creator.creatorName.fl_str_mv Garrido, Nuno M.
Ferreira, Olga
Lugo, Rafael
Hemptinne, Jean-Charles de
Macedo, Eugénia A.
Bottini, Susana B.
datacite.date.Accepted.fl_str_mv 2009-01-01T00:00:00Z
datacite.date.available.fl_str_mv 2010-02-25T15:10:57Z
datacite.date.embargoed.fl_str_mv 2010-02-25T15:10:57Z
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datacite.titles.title.fl_str_mv A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
dc.contributor.none.fl_str_mv Biblioteca Digital da UPB
dc.creator.none.fl_str_mv Garrido, Nuno M.
Ferreira, Olga
Lugo, Rafael
Hemptinne, Jean-Charles de
Macedo, Eugénia A.
Bottini, Susana B.
dc.date.Accepted.fl_str_mv 2009-01-01T00:00:00Z
dc.date.available.fl_str_mv 2010-02-25T15:10:57Z
dc.date.embargoed.fl_str_mv 2010-02-25T15:10:57Z
dc.format.none.fl_str_mv application/pdf
application/pdf
dc.identifier.none.fl_str_mv http://hdl.handle.net/10198/2170
dc.language.none.fl_str_mv eng
dc.rights.none.fl_str_mv http://purl.org/coar/access_right/c_abf2
dc.title.fl_str_mv A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
dc.type.none.fl_str_mv http://purl.org/coar/resource_type/c_5794
description The production of methyl and ethyl esters of fatty acids is of great industrial interest, considering the direct application of these esters as biodiesel. For biodiesel purification and by-products recovery processes design and optimization, the prediction of the phase behaviour of mixtures containing fatty esters, alcohols, glycerol and water is of utmost importance. In this work we show the capability of a A-UNIFAC to correlate and predict phase behaviour of these mixtures. This GE model is an extension of UNIFAC that explicitly includes association effects between groups based on the statistical Wertheim theory [1]. For the water-esters binary systems, the residual and association parameters have been previously estimated using low pressure VLE data [1]. The use of these parameters to predict liquid-liquid equilibrium results in good agreement with experimental information on binaries of water with acetic, octanoic or dodecanoic acids methyl esters. The association effect in methanol and glycerol are represented with the same hydrogen bonding hydroxyl groups (OH) with two associating sites, one group in methanol and three in glycerol. For the residual contribution, both molecules are considered as molecular groups (CH3OH and C3H8O3). The residual interaction parameters between CH3OH and C3H8O3 were obtained by fitting isothermal liquid-liquid equilibrium data on the ternary system dodecanoic acid methyl ester-methanol–glycerol [2]. The glycerol/paraffin (C3H8O3/CH2) and glycerol/ester (C3H8O3/CCOO) interaction parameters were estimated by fitting experimental data on liquid-liquid equilibrium and infinite dilution activity coefficients of the binary systems dodecanoic acid methyl ester-glycerol and hexanoic acid methyl ester-glycerol between 320-438 K [2]. A-UNIFAC with the final set of parameters is able to predict with good agreement experimental data on binary and ternary liquid-liquid equilibria of glycerol + methanol + fatty esters as well as infinite dilution activity coefficient for this system. References [1] O. Ferreira, E.A. Macedo, S.B. Bottini, Fluid Phase Equilib. 227 (2005) 165-176. [2] F.M. Korgitzsch, Study of Phase Equilibria as a Fundament for the Refinement of Vegetable and Animal Fats and Oils. Ph.D. Dissertation, TU Berlin, 1993.
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inst_facet_str urn:organizationAcronym:unipb{{{_:::_}}}Universidade Politécnica de Bragança
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oai_identifier_str oai:bibliotecadigital.unipb.pt:10198/2170
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person_str_mv Garrido, Nuno M.
Ferreira, Olga
Ferreira, Olga
https://www.ciencia-id.pt/9F1D-C75A-4A54
9F1D-C75A-4A54
http://orcid.org/0000-0001-8414-3479
0000-0001-8414-3479
Lugo, Rafael
Hemptinne, Jean-Charles de
Macedo, Eugénia A.
Bottini, Susana B.
publishDate 2009
repo_facet_str urn:repositoryAcronym:ipb{{{_:::_}}}Biblioteca Digital da UPB
reponame_str Biblioteca Digital da UPB
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spelling engptThe production of methyl and ethyl esters of fatty acids is of great industrial interest, considering the direct application of these esters as biodiesel. For biodiesel purification and by-products recovery processes design and optimization, the prediction of the phase behaviour of mixtures containing fatty esters, alcohols, glycerol and water is of utmost importance. In this work we show the capability of a A-UNIFAC to correlate and predict phase behaviour of these mixtures. This GE model is an extension of UNIFAC that explicitly includes association effects between groups based on the statistical Wertheim theory [1]. For the water-esters binary systems, the residual and association parameters have been previously estimated using low pressure VLE data [1]. The use of these parameters to predict liquid-liquid equilibrium results in good agreement with experimental information on binaries of water with acetic, octanoic or dodecanoic acids methyl esters. The association effect in methanol and glycerol are represented with the same hydrogen bonding hydroxyl groups (OH) with two associating sites, one group in methanol and three in glycerol. For the residual contribution, both molecules are considered as molecular groups (CH3OH and C3H8O3). The residual interaction parameters between CH3OH and C3H8O3 were obtained by fitting isothermal liquid-liquid equilibrium data on the ternary system dodecanoic acid methyl ester-methanol–glycerol [2]. The glycerol/paraffin (C3H8O3/CH2) and glycerol/ester (C3H8O3/CCOO) interaction parameters were estimated by fitting experimental data on liquid-liquid equilibrium and infinite dilution activity coefficients of the binary systems dodecanoic acid methyl ester-glycerol and hexanoic acid methyl ester-glycerol between 320-438 K [2]. A-UNIFAC with the final set of parameters is able to predict with good agreement experimental data on binary and ternary liquid-liquid equilibria of glycerol + methanol + fatty esters as well as infinite dilution activity coefficient for this system. References [1] O. Ferreira, E.A. Macedo, S.B. Bottini, Fluid Phase Equilib. 227 (2005) 165-176. [2] F.M. Korgitzsch, Study of Phase Equilibria as a Fundament for the Refinement of Vegetable and Animal Fats and Oils. Ph.D. Dissertation, TU Berlin, 1993.application/pdfapplication/pdfptA-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerolGarrido, Nuno M.PersonalFerreira, OlgaDSpacehttp://dspace.org/items/59e0c608-0c21-4191-af5e-529d21970399DSpacehttp://dspace.org/items/59e0c608-0c21-4191-af5e-529d21970399FerreiraOlgaCiência IDhttps://www.ciencia-id.pt9F1D-C75A-4A54ORCIDhttp://orcid.org0000-0001-8414-3479Researcher IDhttps://www.researcherid.comM-4567-2013Scopus Author IDhttps://www.scopus.com57203083219Lugo, RafaelHemptinne, Jean-Charles deMacedo, Eugénia A.Bottini, Susana B.HostingInstitutionOrganizationalBiblioteca Digital da UPBe-mailmailto:dspace@unipb.ptdspace@unipb.ptISBNIsPartOf978-989-20-1694-82010-02-25T15:10:57Z20092009-01-01T00:00:00ZHandlehttp://hdl.handle.net/10198/2170http://purl.org/coar/access_right/c_abf2open access9144 bytes128230 bytesother research producthttp://purl.org/coar/resource_type/c_5794conference paperhttp://purl.org/coar/access_right/c_abf2application/pdffulltexthttps://bibliotecadigital.unipb.pt/bitstreams/9c8be37a-6471-41b7-af10-7ae87f7c6b5d/downloadhttp://purl.org/coar/access_right/c_abf2application/pdffulltexthttps://bibliotecadigital.unipb.pt/bitstreams/4fa2067b-e034-4d32-8f2c-a77e554b6511/downloadVIII Iberoamerican Conference on Phase Equilibria and Fluid Properties for Process Design - Equifase 2009: Book of abstractsPortimão
spellingShingle A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
Garrido, Nuno M.
status SINGLETON
title A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
title_full A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
title_fullStr A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
title_full_unstemmed A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
title_short A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
title_sort A-UNIFAC modelling of binary and multicomponent phase equilibria of fatty esters+water+methanol+glycerol
url http://hdl.handle.net/10198/2170
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