High pressure solid–liquid equilibrium of fatty acid ethyl esters binary systems

•The melting temperature of ethyl esters were measured up to 80MPa.•The liquidus line of binary systems of ethyl laurate, ethyl myristate and ethyl palmitate were studied up to 80MPa.•Liquidus line was modeled using a high pressure predictive approach. The solid–liquid phase diagrams of three binary...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Veröffentlicht in:Fluid phase equilibria 2014-11, Vol.382, p.158-163
Hauptverfasser: Carareto, Natália D.D., Costa, Mariana C., Meirelles, Antonio J.A., Pauly, J.
Format: Artikel
Sprache:eng
Schlagworte:
Online-Zugang:Volltext
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
container_end_page 163
container_issue
container_start_page 158
container_title Fluid phase equilibria
container_volume 382
creator Carareto, Natália D.D.
Costa, Mariana C.
Meirelles, Antonio J.A.
Pauly, J.
description •The melting temperature of ethyl esters were measured up to 80MPa.•The liquidus line of binary systems of ethyl laurate, ethyl myristate and ethyl palmitate were studied up to 80MPa.•Liquidus line was modeled using a high pressure predictive approach. The solid–liquid phase diagrams of three binary mixtures of fatty acids ethyl esters (FAEEs), formed by ethyl laurate, ethyl myristate and ethyl palmitate, were measured using high pressure microscopy in the range of 0.1–80MPa. In a first step, the melting temperatures of pure FAEEs have been determined showing a linear dependence from the pressure. The binary phase diagrams are only slightly affected by the pressure, even in very large pressure ranges such as those studied in this work. The modeling of the phase diagrams was attempted using a predictive approach previously developed by one of the authors in the case for n-alkane mixtures. The model was able to provide an accurate description of the high pressure solid–liquid equilibrium of FAEE mixtures. Average absolute deviations between experimental and predicted liquidus curve varied from 0.7 to 2.8K in the entire interval of pressures.
doi_str_mv 10.1016/j.fluid.2014.09.007
format Article
fullrecord <record><control><sourceid>proquest_hal_p</sourceid><recordid>TN_cdi_hal_primary_oai_HAL_hal_01279614v1</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0378381214005123</els_id><sourcerecordid>1685769562</sourcerecordid><originalsourceid>FETCH-LOGICAL-c440t-a90f5c17dacbb3e4abb5d4be12e7d225637a33de95d9a93bafcfd1163dd431253</originalsourceid><addsrcrecordid>eNqFkcGOFCEURYnRxHb0C9yw1EWVPCigWLiYTBzbpBMTo2tCwSubDt3VA1WT9G7-wT_0S6SnzSx1A-Fx7s3Nu4S8BdYCA_Vh145piaHlDLqWmZYx_YysoNemYZx3z8mKCd03ogf-krwqZccYA6n4inxbx59besxYypKRlinF8PvhV4p31Y9iPVMcclz2dBrp6Ob5RJ0__8zbU6JYZsyFDvHg8omWU33uy2vyYnSp4Ju_9xX5cfvp-8262Xz9_OXmetP4rmNz4wwbpQcdnB8GgZ0bBhm6AYGjDpxLJbQTIqCRwTgjBjf6MQAoEUIngEtxRd5ffLcu2WOO-5rBTi7a9fXGnmcMuDYKunuo7LsLe8zT3VJj230sHlNyB5yWYkEraRTvFf8_qnqplZGPqLigPk-lZByfYgCz52Lszj4WY8_FWGZsLaaqPl5UWJdzHzHb4iMePIaY0c82TPGf-j9NeJlK</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>1685769562</pqid></control><display><type>article</type><title>High pressure solid–liquid equilibrium of fatty acid ethyl esters binary systems</title><source>Elsevier ScienceDirect Journals</source><creator>Carareto, Natália D.D. ; Costa, Mariana C. ; Meirelles, Antonio J.A. ; Pauly, J.</creator><creatorcontrib>Carareto, Natália D.D. ; Costa, Mariana C. ; Meirelles, Antonio J.A. ; Pauly, J.</creatorcontrib><description>•The melting temperature of ethyl esters were measured up to 80MPa.•The liquidus line of binary systems of ethyl laurate, ethyl myristate and ethyl palmitate were studied up to 80MPa.•Liquidus line was modeled using a high pressure predictive approach. The solid–liquid phase diagrams of three binary mixtures of fatty acids ethyl esters (FAEEs), formed by ethyl laurate, ethyl myristate and ethyl palmitate, were measured using high pressure microscopy in the range of 0.1–80MPa. In a first step, the melting temperatures of pure FAEEs have been determined showing a linear dependence from the pressure. The binary phase diagrams are only slightly affected by the pressure, even in very large pressure ranges such as those studied in this work. The modeling of the phase diagrams was attempted using a predictive approach previously developed by one of the authors in the case for n-alkane mixtures. The model was able to provide an accurate description of the high pressure solid–liquid equilibrium of FAEE mixtures. Average absolute deviations between experimental and predicted liquidus curve varied from 0.7 to 2.8K in the entire interval of pressures.</description><identifier>ISSN: 0378-3812</identifier><identifier>EISSN: 1879-0224</identifier><identifier>DOI: 10.1016/j.fluid.2014.09.007</identifier><language>eng</language><publisher>Elsevier B.V</publisher><subject>Binary systems ; Computational fluid dynamics ; Deviation ; Engineering Sciences ; Ethyl esters ; Fatty acid ethyl esters ; Fatty acids ; High pressure data ; Mathematical models ; Melting ; Phase diagrams ; Solid–liquid equilibrium</subject><ispartof>Fluid phase equilibria, 2014-11, Vol.382, p.158-163</ispartof><rights>2014 Elsevier B.V.</rights><rights>Distributed under a Creative Commons Attribution 4.0 International License</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c440t-a90f5c17dacbb3e4abb5d4be12e7d225637a33de95d9a93bafcfd1163dd431253</citedby><cites>FETCH-LOGICAL-c440t-a90f5c17dacbb3e4abb5d4be12e7d225637a33de95d9a93bafcfd1163dd431253</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0378381214005123$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>230,314,776,780,881,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttps://hal.science/hal-01279614$$DView record in HAL$$Hfree_for_read</backlink></links><search><creatorcontrib>Carareto, Natália D.D.</creatorcontrib><creatorcontrib>Costa, Mariana C.</creatorcontrib><creatorcontrib>Meirelles, Antonio J.A.</creatorcontrib><creatorcontrib>Pauly, J.</creatorcontrib><title>High pressure solid–liquid equilibrium of fatty acid ethyl esters binary systems</title><title>Fluid phase equilibria</title><description>•The melting temperature of ethyl esters were measured up to 80MPa.•The liquidus line of binary systems of ethyl laurate, ethyl myristate and ethyl palmitate were studied up to 80MPa.•Liquidus line was modeled using a high pressure predictive approach. The solid–liquid phase diagrams of three binary mixtures of fatty acids ethyl esters (FAEEs), formed by ethyl laurate, ethyl myristate and ethyl palmitate, were measured using high pressure microscopy in the range of 0.1–80MPa. In a first step, the melting temperatures of pure FAEEs have been determined showing a linear dependence from the pressure. The binary phase diagrams are only slightly affected by the pressure, even in very large pressure ranges such as those studied in this work. The modeling of the phase diagrams was attempted using a predictive approach previously developed by one of the authors in the case for n-alkane mixtures. The model was able to provide an accurate description of the high pressure solid–liquid equilibrium of FAEE mixtures. Average absolute deviations between experimental and predicted liquidus curve varied from 0.7 to 2.8K in the entire interval of pressures.</description><subject>Binary systems</subject><subject>Computational fluid dynamics</subject><subject>Deviation</subject><subject>Engineering Sciences</subject><subject>Ethyl esters</subject><subject>Fatty acid ethyl esters</subject><subject>Fatty acids</subject><subject>High pressure data</subject><subject>Mathematical models</subject><subject>Melting</subject><subject>Phase diagrams</subject><subject>Solid–liquid equilibrium</subject><issn>0378-3812</issn><issn>1879-0224</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2014</creationdate><recordtype>article</recordtype><recordid>eNqFkcGOFCEURYnRxHb0C9yw1EWVPCigWLiYTBzbpBMTo2tCwSubDt3VA1WT9G7-wT_0S6SnzSx1A-Fx7s3Nu4S8BdYCA_Vh145piaHlDLqWmZYx_YysoNemYZx3z8mKCd03ogf-krwqZccYA6n4inxbx59besxYypKRlinF8PvhV4p31Y9iPVMcclz2dBrp6Ob5RJ0__8zbU6JYZsyFDvHg8omWU33uy2vyYnSp4Ju_9xX5cfvp-8262Xz9_OXmetP4rmNz4wwbpQcdnB8GgZ0bBhm6AYGjDpxLJbQTIqCRwTgjBjf6MQAoEUIngEtxRd5ffLcu2WOO-5rBTi7a9fXGnmcMuDYKunuo7LsLe8zT3VJj230sHlNyB5yWYkEraRTvFf8_qnqplZGPqLigPk-lZByfYgCz52Lszj4WY8_FWGZsLaaqPl5UWJdzHzHb4iMePIaY0c82TPGf-j9NeJlK</recordid><startdate>20141101</startdate><enddate>20141101</enddate><creator>Carareto, Natália D.D.</creator><creator>Costa, Mariana C.</creator><creator>Meirelles, Antonio J.A.</creator><creator>Pauly, J.</creator><general>Elsevier B.V</general><general>Elsevier</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7U5</scope><scope>8FD</scope><scope>L7M</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H96</scope><scope>L.G</scope><scope>1XC</scope></search><sort><creationdate>20141101</creationdate><title>High pressure solid–liquid equilibrium of fatty acid ethyl esters binary systems</title><author>Carareto, Natália D.D. ; Costa, Mariana C. ; Meirelles, Antonio J.A. ; Pauly, J.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c440t-a90f5c17dacbb3e4abb5d4be12e7d225637a33de95d9a93bafcfd1163dd431253</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2014</creationdate><topic>Binary systems</topic><topic>Computational fluid dynamics</topic><topic>Deviation</topic><topic>Engineering Sciences</topic><topic>Ethyl esters</topic><topic>Fatty acid ethyl esters</topic><topic>Fatty acids</topic><topic>High pressure data</topic><topic>Mathematical models</topic><topic>Melting</topic><topic>Phase diagrams</topic><topic>Solid–liquid equilibrium</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Carareto, Natália D.D.</creatorcontrib><creatorcontrib>Costa, Mariana C.</creatorcontrib><creatorcontrib>Meirelles, Antonio J.A.</creatorcontrib><creatorcontrib>Pauly, J.</creatorcontrib><collection>CrossRef</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>Technology Research Database</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Water Resources Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ASFA: Aquatic Sciences and Fisheries Abstracts</collection><collection>Aquatic Science &amp; Fisheries Abstracts (ASFA) 2: Ocean Technology, Policy &amp; Non-Living Resources</collection><collection>Aquatic Science &amp; Fisheries Abstracts (ASFA) Professional</collection><collection>Hyper Article en Ligne (HAL)</collection><jtitle>Fluid phase equilibria</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Carareto, Natália D.D.</au><au>Costa, Mariana C.</au><au>Meirelles, Antonio J.A.</au><au>Pauly, J.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>High pressure solid–liquid equilibrium of fatty acid ethyl esters binary systems</atitle><jtitle>Fluid phase equilibria</jtitle><date>2014-11-01</date><risdate>2014</risdate><volume>382</volume><spage>158</spage><epage>163</epage><pages>158-163</pages><issn>0378-3812</issn><eissn>1879-0224</eissn><abstract>•The melting temperature of ethyl esters were measured up to 80MPa.•The liquidus line of binary systems of ethyl laurate, ethyl myristate and ethyl palmitate were studied up to 80MPa.•Liquidus line was modeled using a high pressure predictive approach. The solid–liquid phase diagrams of three binary mixtures of fatty acids ethyl esters (FAEEs), formed by ethyl laurate, ethyl myristate and ethyl palmitate, were measured using high pressure microscopy in the range of 0.1–80MPa. In a first step, the melting temperatures of pure FAEEs have been determined showing a linear dependence from the pressure. The binary phase diagrams are only slightly affected by the pressure, even in very large pressure ranges such as those studied in this work. The modeling of the phase diagrams was attempted using a predictive approach previously developed by one of the authors in the case for n-alkane mixtures. The model was able to provide an accurate description of the high pressure solid–liquid equilibrium of FAEE mixtures. Average absolute deviations between experimental and predicted liquidus curve varied from 0.7 to 2.8K in the entire interval of pressures.</abstract><pub>Elsevier B.V</pub><doi>10.1016/j.fluid.2014.09.007</doi><tpages>6</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0378-3812
ispartof Fluid phase equilibria, 2014-11, Vol.382, p.158-163
issn 0378-3812
1879-0224
language eng
recordid cdi_hal_primary_oai_HAL_hal_01279614v1
source Elsevier ScienceDirect Journals
subjects Binary systems
Computational fluid dynamics
Deviation
Engineering Sciences
Ethyl esters
Fatty acid ethyl esters
Fatty acids
High pressure data
Mathematical models
Melting
Phase diagrams
Solid–liquid equilibrium
title High pressure solid–liquid equilibrium of fatty acid ethyl esters binary systems
url https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-01T13%3A21%3A20IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_hal_p&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=High%20pressure%20solid%E2%80%93liquid%20equilibrium%20of%20fatty%20acid%20ethyl%20esters%20binary%20systems&rft.jtitle=Fluid%20phase%20equilibria&rft.au=Carareto,%20Nat%C3%A1lia%20D.D.&rft.date=2014-11-01&rft.volume=382&rft.spage=158&rft.epage=163&rft.pages=158-163&rft.issn=0378-3812&rft.eissn=1879-0224&rft_id=info:doi/10.1016/j.fluid.2014.09.007&rft_dat=%3Cproquest_hal_p%3E1685769562%3C/proquest_hal_p%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=1685769562&rft_id=info:pmid/&rft_els_id=S0378381214005123&rfr_iscdi=true