Excess enthalpies (H-E) for 2-butoxyethanol/water and determination of liquid-liquid equilibrium phase boundaries from fits to H-E of Redlich-Kister, Pade, and critical-scaling equations
DC Field | Value | Language |
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dc.contributor.author | Lim, KH | - |
dc.contributor.author | Smith, DH | - |
dc.date.accessioned | 2021-06-18T14:42:02Z | - |
dc.date.available | 2021-06-18T14:42:02Z | - |
dc.date.issued | 2001-04 | - |
dc.identifier.issn | 0021-9592 | - |
dc.identifier.uri | https://scholarworks.bwise.kr/cau/handle/2019.sw.cau/47267 | - |
dc.description.abstract | Excess enthalpies (H-E) for the binary n-butanol/water measured by isothermal flow calorimetry at 30 and 55 degreesC, and nonionic amphiphile 2-butoxyethanol/water at 10 different temperatures (from 48.5 to 70 degreesC) reported in the literature were analyzed for the determination of phase boundaries. H-E exhibited S-shape behavior in the former system and U-shape behavior in the latter system. When the H-E data in the single-phase were fitted by semi-empirical polynomials and critical-scaling equations, plots of specific H-E vs. weight fraction provided more accurate fitting with fewer parameters than conventionally drawn molar H-E vs, mole fraction plots. This was due to the enhanced symmetry of specific H-E vs. weight fraction plots. Liquid-liquid equilibrium phase boundaries between the single- and two-phase regions were determined from H-E. The phase boundary points were obtained as the intersections of the curve and the straight line, which describe the composition dependence of H-E for the single- and two-phase regions, respectively. When Redlich-Kister(RK) and Fade polynomials were employed, the phase boundary points could be determined For the n-butanol/water but not For the 2-butoxyethanol/water. These results imply that correct phase boundaries may not be obtained with the semi-empirical polynomials when H-E behavior is of the U-type, However, when the critical-scaling equations for H-E of binary mixtures were used, the phase boundaries were obtained accurately, irrespective of the type of H-E data. | - |
dc.format.extent | 10 | - |
dc.language | 영어 | - |
dc.language.iso | ENG | - |
dc.publisher | SOC CHEMICAL ENG JAPAN | - |
dc.title | Excess enthalpies (H-E) for 2-butoxyethanol/water and determination of liquid-liquid equilibrium phase boundaries from fits to H-E of Redlich-Kister, Pade, and critical-scaling equations | - |
dc.type | Article | - |
dc.identifier.doi | 10.1252/jcej.34.513 | - |
dc.identifier.bibliographicCitation | JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, v.34, no.4, pp 513 - 522 | - |
dc.description.isOpenAccess | N | - |
dc.identifier.wosid | 000168389900009 | - |
dc.identifier.scopusid | 2-s2.0-0035297546 | - |
dc.citation.endPage | 522 | - |
dc.citation.number | 4 | - |
dc.citation.startPage | 513 | - |
dc.citation.title | JOURNAL OF CHEMICAL ENGINEERING OF JAPAN | - |
dc.citation.volume | 34 | - |
dc.type.docType | Article | - |
dc.publisher.location | 일본 | - |
dc.subject.keywordAuthor | excess enthalpy | - |
dc.subject.keywordAuthor | partial molar enthalpy | - |
dc.subject.keywordAuthor | Redlich-Kister polynomial | - |
dc.subject.keywordAuthor | LLE phase composition | - |
dc.subject.keywordAuthor | activity coefficient | - |
dc.subject.keywordPlus | THERMODYNAMIC PROPERTIES | - |
dc.subject.keywordPlus | MOLAR ENTHALPIES | - |
dc.subject.keywordPlus | WATER | - |
dc.subject.keywordPlus | MIXTURES | - |
dc.subject.keywordPlus | SYSTEMS | - |
dc.relation.journalResearchArea | Engineering | - |
dc.relation.journalWebOfScienceCategory | Engineering, Chemical | - |
dc.description.journalRegisteredClass | scie | - |
dc.description.journalRegisteredClass | scopus | - |
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