A Method To Estimate the Patel−Teja Equation of State Constants
A method to determine the Patel−Teja equation of state (EoS) constants F and ζc is presented. The method uses Wagner and Rackett equations to generate vapor pressure and liquid volume data. Constants were estimated for 498 pure substances. For 19 substances the new constants were used to predict som...
Gespeichert in:
Veröffentlicht in: | Journal of chemical and engineering data 2010-11, Vol.55 (11), p.5094-5100 |
---|---|
Hauptverfasser: | , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 5100 |
---|---|
container_issue | 11 |
container_start_page | 5094 |
container_title | Journal of chemical and engineering data |
container_volume | 55 |
creator | Forero, Luis A Velásquez, Jorge A |
description | A method to determine the Patel−Teja equation of state (EoS) constants F and ζc is presented. The method uses Wagner and Rackett equations to generate vapor pressure and liquid volume data. Constants were estimated for 498 pure substances. For 19 substances the new constants were used to predict some thermodynamical properties like vapor pressure, liquid molar volume, vapor molar volume, and enthalpy of vaporization. An extension to mixtures was done by using the Panagiotopoulous−Reid mixing rule. New constants are comparable to the original ones reported in the Patel−Teja work, and they preserve the good features of the equation of state. |
doi_str_mv | 10.1021/je100656d |
format | Article |
fullrecord | <record><control><sourceid>acs_cross</sourceid><recordid>TN_cdi_crossref_primary_10_1021_je100656d</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>b059471063</sourcerecordid><originalsourceid>FETCH-LOGICAL-a289t-9eaa8ed091095ebd515f6ec913014d4453874b4b2455b6c31dca85f7b244ee2d3</originalsourceid><addsrcrecordid>eNptj79OwzAQhy0EEqUw8AZeGBgC539pPFZVKUhFIFHm6GJf1EYlLrE78AbMPCJPQqqisjDd6e67n-5j7FLAjQApbhsSALnJ_REbCCMhM0LpYzaAfplZkxen7CzGBgD0SIoBG4_5I6Vl8HwR-DSm1Rsm4mlJ_Llv1t-fXwtqkE_ft5hWoeWh5i9ph0xCGxO2KZ6zkxrXkS5-65C93k0Xk_ts_jR7mIznGcrCpswSYkEerABrqPJGmDonZ4UCob3WRhUjXelKamOq3CnhHRamHvUDTSS9GrLrfa7rQowd1eWm67_tPkoB5c69PLj37NWe3WB0uK47bN0qHg6k0qoAC38culg2Ydu1vcE_eT95RmRy</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>A Method To Estimate the Patel−Teja Equation of State Constants</title><source>American Chemical Society Journals</source><creator>Forero, Luis A ; Velásquez, Jorge A</creator><creatorcontrib>Forero, Luis A ; Velásquez, Jorge A</creatorcontrib><description>A method to determine the Patel−Teja equation of state (EoS) constants F and ζc is presented. The method uses Wagner and Rackett equations to generate vapor pressure and liquid volume data. Constants were estimated for 498 pure substances. For 19 substances the new constants were used to predict some thermodynamical properties like vapor pressure, liquid molar volume, vapor molar volume, and enthalpy of vaporization. An extension to mixtures was done by using the Panagiotopoulous−Reid mixing rule. New constants are comparable to the original ones reported in the Patel−Teja work, and they preserve the good features of the equation of state.</description><identifier>ISSN: 0021-9568</identifier><identifier>EISSN: 1520-5134</identifier><identifier>DOI: 10.1021/je100656d</identifier><identifier>CODEN: JCEAAX</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Chemistry ; Exact sciences and technology ; General and physical chemistry ; Phase equilibria</subject><ispartof>Journal of chemical and engineering data, 2010-11, Vol.55 (11), p.5094-5100</ispartof><rights>Copyright © 2010 American Chemical Society</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a289t-9eaa8ed091095ebd515f6ec913014d4453874b4b2455b6c31dca85f7b244ee2d3</citedby><cites>FETCH-LOGICAL-a289t-9eaa8ed091095ebd515f6ec913014d4453874b4b2455b6c31dca85f7b244ee2d3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/je100656d$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/je100656d$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>314,780,784,2765,27076,27924,27925,56738,56788</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=23438090$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Forero, Luis A</creatorcontrib><creatorcontrib>Velásquez, Jorge A</creatorcontrib><title>A Method To Estimate the Patel−Teja Equation of State Constants</title><title>Journal of chemical and engineering data</title><addtitle>J. Chem. Eng. Data</addtitle><description>A method to determine the Patel−Teja equation of state (EoS) constants F and ζc is presented. The method uses Wagner and Rackett equations to generate vapor pressure and liquid volume data. Constants were estimated for 498 pure substances. For 19 substances the new constants were used to predict some thermodynamical properties like vapor pressure, liquid molar volume, vapor molar volume, and enthalpy of vaporization. An extension to mixtures was done by using the Panagiotopoulous−Reid mixing rule. New constants are comparable to the original ones reported in the Patel−Teja work, and they preserve the good features of the equation of state.</description><subject>Chemistry</subject><subject>Exact sciences and technology</subject><subject>General and physical chemistry</subject><subject>Phase equilibria</subject><issn>0021-9568</issn><issn>1520-5134</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNptj79OwzAQhy0EEqUw8AZeGBgC539pPFZVKUhFIFHm6GJf1EYlLrE78AbMPCJPQqqisjDd6e67n-5j7FLAjQApbhsSALnJ_REbCCMhM0LpYzaAfplZkxen7CzGBgD0SIoBG4_5I6Vl8HwR-DSm1Rsm4mlJ_Llv1t-fXwtqkE_ft5hWoeWh5i9ph0xCGxO2KZ6zkxrXkS5-65C93k0Xk_ts_jR7mIznGcrCpswSYkEerABrqPJGmDonZ4UCob3WRhUjXelKamOq3CnhHRamHvUDTSS9GrLrfa7rQowd1eWm67_tPkoB5c69PLj37NWe3WB0uK47bN0qHg6k0qoAC38culg2Ydu1vcE_eT95RmRy</recordid><startdate>20101111</startdate><enddate>20101111</enddate><creator>Forero, Luis A</creator><creator>Velásquez, Jorge A</creator><general>American Chemical Society</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>20101111</creationdate><title>A Method To Estimate the Patel−Teja Equation of State Constants</title><author>Forero, Luis A ; Velásquez, Jorge A</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a289t-9eaa8ed091095ebd515f6ec913014d4453874b4b2455b6c31dca85f7b244ee2d3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Chemistry</topic><topic>Exact sciences and technology</topic><topic>General and physical chemistry</topic><topic>Phase equilibria</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Forero, Luis A</creatorcontrib><creatorcontrib>Velásquez, Jorge A</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><jtitle>Journal of chemical and engineering data</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Forero, Luis A</au><au>Velásquez, Jorge A</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>A Method To Estimate the Patel−Teja Equation of State Constants</atitle><jtitle>Journal of chemical and engineering data</jtitle><addtitle>J. Chem. Eng. Data</addtitle><date>2010-11-11</date><risdate>2010</risdate><volume>55</volume><issue>11</issue><spage>5094</spage><epage>5100</epage><pages>5094-5100</pages><issn>0021-9568</issn><eissn>1520-5134</eissn><coden>JCEAAX</coden><abstract>A method to determine the Patel−Teja equation of state (EoS) constants F and ζc is presented. The method uses Wagner and Rackett equations to generate vapor pressure and liquid volume data. Constants were estimated for 498 pure substances. For 19 substances the new constants were used to predict some thermodynamical properties like vapor pressure, liquid molar volume, vapor molar volume, and enthalpy of vaporization. An extension to mixtures was done by using the Panagiotopoulous−Reid mixing rule. New constants are comparable to the original ones reported in the Patel−Teja work, and they preserve the good features of the equation of state.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/je100656d</doi><tpages>7</tpages></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0021-9568 |
ispartof | Journal of chemical and engineering data, 2010-11, Vol.55 (11), p.5094-5100 |
issn | 0021-9568 1520-5134 |
language | eng |
recordid | cdi_crossref_primary_10_1021_je100656d |
source | American Chemical Society Journals |
subjects | Chemistry Exact sciences and technology General and physical chemistry Phase equilibria |
title | A Method To Estimate the Patel−Teja Equation of State Constants |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-20T10%3A00%3A14IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-acs_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=A%20Method%20To%20Estimate%20the%20Patel%E2%88%92Teja%20Equation%20of%20State%20Constants&rft.jtitle=Journal%20of%20chemical%20and%20engineering%20data&rft.au=Forero,%20Luis%20A&rft.date=2010-11-11&rft.volume=55&rft.issue=11&rft.spage=5094&rft.epage=5100&rft.pages=5094-5100&rft.issn=0021-9568&rft.eissn=1520-5134&rft.coden=JCEAAX&rft_id=info:doi/10.1021/je100656d&rft_dat=%3Cacs_cross%3Eb059471063%3C/acs_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true |