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Free-volume theory coupled with modified group-contribution PC-SAFT for predicting viscosities of 1-alkenes
A modified group-contribution PC-SAFT EoS combined with the Free-volume theory (FVT), recently proposed (DOI: https://doi.org/10.1016/j.fluid.2019.112280 ) to simultaneously model the fluid phase equilibria and viscosity of fluids, is extended in this work to estimate the viscosity of 1-alkenes. Gen...
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Published in: | The Korean journal of chemical engineering 2020, 37(3), 240, pp.402-410 |
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container_issue | 3 |
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container_title | The Korean journal of chemical engineering |
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creator | NguyenHuynh, Dong Luu, My T. Mai, Chau T. Q. Tran, Siem T. K. |
description | A modified group-contribution PC-SAFT EoS combined with the Free-volume theory (FVT), recently proposed (DOI:
https://doi.org/10.1016/j.fluid.2019.112280
) to simultaneously model the fluid phase equilibria and viscosity of fluids, is extended in this work to estimate the viscosity of 1-alkenes. Generalized correlation coefficients are proposed for the FVT triplet parameter set, which makes it possible to extrapolate the viscosity prediction of similar compounds that are not included in the fitting pool. The model is validated using a large experimental data of 1-alkenes over wide range of temperature and pressure (up to 2,500 bars). For 1-pentene to 1-triacontene, the overall average absolute deviation of the experimental liquid and vapor viscosity from those calculated by the model is of 5.37% and 1.41%, respectively, which are appropriate for most industrial applications. |
doi_str_mv | 10.1007/s11814-019-0473-x |
format | article |
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https://doi.org/10.1016/j.fluid.2019.112280
) to simultaneously model the fluid phase equilibria and viscosity of fluids, is extended in this work to estimate the viscosity of 1-alkenes. Generalized correlation coefficients are proposed for the FVT triplet parameter set, which makes it possible to extrapolate the viscosity prediction of similar compounds that are not included in the fitting pool. The model is validated using a large experimental data of 1-alkenes over wide range of temperature and pressure (up to 2,500 bars). For 1-pentene to 1-triacontene, the overall average absolute deviation of the experimental liquid and vapor viscosity from those calculated by the model is of 5.37% and 1.41%, respectively, which are appropriate for most industrial applications.</description><identifier>ISSN: 0256-1115</identifier><identifier>EISSN: 1975-7220</identifier><identifier>DOI: 10.1007/s11814-019-0473-x</identifier><language>eng</language><publisher>New York: Springer US</publisher><subject>Alkenes ; Biotechnology ; Catalysis ; Chemistry ; Chemistry and Materials Science ; Computational fluid dynamics ; Correlation coefficients ; Industrial applications ; Industrial Chemistry/Chemical Engineering ; Materials Science ; Phase equilibria ; Transport Phenomena ; Viscosity ; 화학공학</subject><ispartof>Korean Journal of Chemical Engineering, 2020, 37(3), 240, pp.402-410</ispartof><rights>The Korean Institute of Chemical Engineers 2020</rights><rights>2020© The Korean Institute of Chemical Engineers 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c387t-3187893208493a99430f3e43f003fcd19985341d27c730f4b88eb4bd24cdc0523</citedby><cites>FETCH-LOGICAL-c387t-3187893208493a99430f3e43f003fcd19985341d27c730f4b88eb4bd24cdc0523</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,780,784,27923,27924</link.rule.ids><backlink>$$Uhttps://www.kci.go.kr/kciportal/ci/sereArticleSearch/ciSereArtiView.kci?sereArticleSearchBean.artiId=ART002558322$$DAccess content in National Research Foundation of Korea (NRF)$$Hfree_for_read</backlink></links><search><creatorcontrib>NguyenHuynh, Dong</creatorcontrib><creatorcontrib>Luu, My T.</creatorcontrib><creatorcontrib>Mai, Chau T. Q.</creatorcontrib><creatorcontrib>Tran, Siem T. K.</creatorcontrib><title>Free-volume theory coupled with modified group-contribution PC-SAFT for predicting viscosities of 1-alkenes</title><title>The Korean journal of chemical engineering</title><addtitle>Korean J. Chem. Eng</addtitle><description>A modified group-contribution PC-SAFT EoS combined with the Free-volume theory (FVT), recently proposed (DOI:
https://doi.org/10.1016/j.fluid.2019.112280
) to simultaneously model the fluid phase equilibria and viscosity of fluids, is extended in this work to estimate the viscosity of 1-alkenes. Generalized correlation coefficients are proposed for the FVT triplet parameter set, which makes it possible to extrapolate the viscosity prediction of similar compounds that are not included in the fitting pool. The model is validated using a large experimental data of 1-alkenes over wide range of temperature and pressure (up to 2,500 bars). For 1-pentene to 1-triacontene, the overall average absolute deviation of the experimental liquid and vapor viscosity from those calculated by the model is of 5.37% and 1.41%, respectively, which are appropriate for most industrial applications.</description><subject>Alkenes</subject><subject>Biotechnology</subject><subject>Catalysis</subject><subject>Chemistry</subject><subject>Chemistry and Materials Science</subject><subject>Computational fluid dynamics</subject><subject>Correlation coefficients</subject><subject>Industrial applications</subject><subject>Industrial Chemistry/Chemical Engineering</subject><subject>Materials Science</subject><subject>Phase equilibria</subject><subject>Transport Phenomena</subject><subject>Viscosity</subject><subject>화학공학</subject><issn>0256-1115</issn><issn>1975-7220</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp1kE1rGzEQhkVJoU7aH9CbIKcclM7ow5KOxtRJINDSumex1kqOYnvlSLtp8u-77gZ66mmYmecdhoeQzwjXCKC_VESDkgFaBlIL9vKOzNBqxTTncEZmwNWcIaL6QM5rfQRQas5hRnarEgJ7zvvhEGj_EHJ5pT4Px31o6e_UP9BDblNMY7ct45j53PUlbYY-5Y5-X7Kfi9WaxlzosYQ2-T51W_qcqs819SlUmiNF1ux3oQv1I3kfm30Nn97qBfm1-rpe3rL7bzd3y8U988Longk02ljBwUgrGmulgCiCFBFARN-itUYJiS3XXo8ruTEmbOSm5dK3HhQXF-RqutuV6HY-udykv3Wb3a64xY_1nZsbxed4Yi8n9ljy0xBq7x7zULrxPceFHi1ZBScKJ8qXXGsJ0R1LOjTl1SG4k383-Xejf3fy717GDJ8ydWS7bSj_Lv8_9AeQBoe-</recordid><startdate>20200301</startdate><enddate>20200301</enddate><creator>NguyenHuynh, Dong</creator><creator>Luu, My T.</creator><creator>Mai, Chau T. Q.</creator><creator>Tran, Siem T. K.</creator><general>Springer US</general><general>Springer Nature B.V</general><general>한국화학공학회</general><scope>AAYXX</scope><scope>CITATION</scope><scope>ACYCR</scope></search><sort><creationdate>20200301</creationdate><title>Free-volume theory coupled with modified group-contribution PC-SAFT for predicting viscosities of 1-alkenes</title><author>NguyenHuynh, Dong ; Luu, My T. ; Mai, Chau T. Q. ; Tran, Siem T. K.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c387t-3187893208493a99430f3e43f003fcd19985341d27c730f4b88eb4bd24cdc0523</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Alkenes</topic><topic>Biotechnology</topic><topic>Catalysis</topic><topic>Chemistry</topic><topic>Chemistry and Materials Science</topic><topic>Computational fluid dynamics</topic><topic>Correlation coefficients</topic><topic>Industrial applications</topic><topic>Industrial Chemistry/Chemical Engineering</topic><topic>Materials Science</topic><topic>Phase equilibria</topic><topic>Transport Phenomena</topic><topic>Viscosity</topic><topic>화학공학</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>NguyenHuynh, Dong</creatorcontrib><creatorcontrib>Luu, My T.</creatorcontrib><creatorcontrib>Mai, Chau T. Q.</creatorcontrib><creatorcontrib>Tran, Siem T. K.</creatorcontrib><collection>CrossRef</collection><collection>Korean Citation Index</collection><jtitle>The Korean journal of chemical engineering</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>NguyenHuynh, Dong</au><au>Luu, My T.</au><au>Mai, Chau T. Q.</au><au>Tran, Siem T. K.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Free-volume theory coupled with modified group-contribution PC-SAFT for predicting viscosities of 1-alkenes</atitle><jtitle>The Korean journal of chemical engineering</jtitle><stitle>Korean J. Chem. Eng</stitle><date>2020-03-01</date><risdate>2020</risdate><volume>37</volume><issue>3</issue><spage>402</spage><epage>410</epage><pages>402-410</pages><issn>0256-1115</issn><eissn>1975-7220</eissn><abstract>A modified group-contribution PC-SAFT EoS combined with the Free-volume theory (FVT), recently proposed (DOI:
https://doi.org/10.1016/j.fluid.2019.112280
) to simultaneously model the fluid phase equilibria and viscosity of fluids, is extended in this work to estimate the viscosity of 1-alkenes. Generalized correlation coefficients are proposed for the FVT triplet parameter set, which makes it possible to extrapolate the viscosity prediction of similar compounds that are not included in the fitting pool. The model is validated using a large experimental data of 1-alkenes over wide range of temperature and pressure (up to 2,500 bars). For 1-pentene to 1-triacontene, the overall average absolute deviation of the experimental liquid and vapor viscosity from those calculated by the model is of 5.37% and 1.41%, respectively, which are appropriate for most industrial applications.</abstract><cop>New York</cop><pub>Springer US</pub><doi>10.1007/s11814-019-0473-x</doi><tpages>9</tpages></addata></record> |
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subjects | Alkenes Biotechnology Catalysis Chemistry Chemistry and Materials Science Computational fluid dynamics Correlation coefficients Industrial applications Industrial Chemistry/Chemical Engineering Materials Science Phase equilibria Transport Phenomena Viscosity 화학공학 |
title | Free-volume theory coupled with modified group-contribution PC-SAFT for predicting viscosities of 1-alkenes |
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