Isothermal Vapor-Liquid Equilibria for the Binary System of Carbon Dioxide (CO2)+1,1,1,2,3,3,3-Heptafluoropropane (R-227ea)
DC Field | Value | Language |
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dc.contributor.author | Kim, Seol A. | - |
dc.contributor.author | Lim, Jong Sung | - |
dc.contributor.author | Kang, Jeong Won | - |
dc.date.accessioned | 2021-09-07T23:22:52Z | - |
dc.date.available | 2021-09-07T23:22:52Z | - |
dc.date.created | 2021-06-14 | - |
dc.date.issued | 2010-11 | - |
dc.identifier.issn | 0021-9568 | - |
dc.identifier.uri | https://scholar.korea.ac.kr/handle/2021.sw.korea/115470 | - |
dc.description.abstract | Isothermal vapor liquid equilibrium (VLE) data for the binary mixture of carbon dioxide (CO2) + 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) were measured at six evenly spaced temperatures of (278.15, 288.15, 298.15, 308.15, 318.15, and 328.15) K. The data in the two-phase region were measured by using a circulation-type equilibrium apparatus in which both vapor and liquid phases are continuously recirculated. The experimental data were correlated with the Peng-Robinson equation of state (PR-EoS) using the Wong-Sandler (W-S) mixing rules combined with the nonrandom two-liquid (NRTL) excess Gibbs free energy model. The calculated values with the PR-EoS using the W-S mixing rules show good agreement with the experimental data. | - |
dc.language | English | - |
dc.language.iso | en | - |
dc.publisher | AMER CHEMICAL SOC | - |
dc.subject | PLUS PROPANE | - |
dc.subject | MIXING RULE | - |
dc.subject | TEMPERATURES | - |
dc.subject | PRESSURES | - |
dc.subject | STATE | - |
dc.subject | HFC-227EA | - |
dc.subject | MIXTURES | - |
dc.subject | EQUATION | - |
dc.subject | MPA | - |
dc.title | Isothermal Vapor-Liquid Equilibria for the Binary System of Carbon Dioxide (CO2)+1,1,1,2,3,3,3-Heptafluoropropane (R-227ea) | - |
dc.type | Article | - |
dc.contributor.affiliatedAuthor | Kang, Jeong Won | - |
dc.identifier.doi | 10.1021/je100583z | - |
dc.identifier.scopusid | 2-s2.0-78449266303 | - |
dc.identifier.wosid | 000284017600068 | - |
dc.identifier.bibliographicCitation | JOURNAL OF CHEMICAL AND ENGINEERING DATA, v.55, no.11, pp.4999 - 5003 | - |
dc.relation.isPartOf | JOURNAL OF CHEMICAL AND ENGINEERING DATA | - |
dc.citation.title | JOURNAL OF CHEMICAL AND ENGINEERING DATA | - |
dc.citation.volume | 55 | - |
dc.citation.number | 11 | - |
dc.citation.startPage | 4999 | - |
dc.citation.endPage | 5003 | - |
dc.type.rims | ART | - |
dc.type.docType | Article | - |
dc.description.journalClass | 1 | - |
dc.description.journalRegisteredClass | scie | - |
dc.description.journalRegisteredClass | scopus | - |
dc.relation.journalResearchArea | Thermodynamics | - |
dc.relation.journalResearchArea | Chemistry | - |
dc.relation.journalResearchArea | Engineering | - |
dc.relation.journalWebOfScienceCategory | Thermodynamics | - |
dc.relation.journalWebOfScienceCategory | Chemistry, Multidisciplinary | - |
dc.relation.journalWebOfScienceCategory | Engineering, Chemical | - |
dc.subject.keywordPlus | PLUS PROPANE | - |
dc.subject.keywordPlus | MIXING RULE | - |
dc.subject.keywordPlus | TEMPERATURES | - |
dc.subject.keywordPlus | PRESSURES | - |
dc.subject.keywordPlus | STATE | - |
dc.subject.keywordPlus | HFC-227EA | - |
dc.subject.keywordPlus | MIXTURES | - |
dc.subject.keywordPlus | EQUATION | - |
dc.subject.keywordPlus | MPA | - |
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