DC Field | Value | Language |
---|---|---|
dc.contributor.author | Lee, HS | ko |
dc.contributor.author | Mun, SY | ko |
dc.contributor.author | Lee, Huen | ko |
dc.date.accessioned | 2009-05-18T01:21:07Z | - |
dc.date.available | 2009-05-18T01:21:07Z | - |
dc.date.created | 2012-02-06 | - |
dc.date.created | 2012-02-06 | - |
dc.date.issued | 1999-03 | - |
dc.identifier.citation | FLUID PHASE EQUILIBRIA, v.157, no.1, pp.81 - 91 | - |
dc.identifier.issn | 0378-3812 | - |
dc.identifier.uri | http://hdl.handle.net/10203/8979 | - |
dc.description.abstract | High-pressure vapor-liquid equilibria for the binary carbon dioxide-2-methyl-1-butanol and carbon dioxide-2-methyl-2-butanol systems were measured at 313.2 K. The phase equilibrium apparatus used in this work is of the circulation type in which the coexisting phases are recirculated, on-line sampled, and analyzed. The critical pressure and corresponding mole fraction of carbon dioxide for the binary carbon dioxide-2-methyl-1-butanol system at 313.2 K were found to be 8.36 MPa and 0.980, respectively. The critical point of the binary carbon dioxide-2-methyl-2-butanol was also found 8.15 MPa and 0.970 mole fraction of carbon dioxide. In addition, the phase equilibria of the ternary carbon dioxide-2-methyl-1-butanol-water and carbon dioxide-2-methyl-2-butanol-water systems were measured at 313.2 K and several pressures. These ternary systems showed the liquid-liquid-vapor phase behavior over the range of pressure up to their critical point. The binary equilibrium data were all reasonably well correlated with the Redlich-Kwong (RK), Soave-Redlich-Kwong (SRK), Peng-Robinson (PR), and Patel-Teja (PT) equations of state with eight different mixing rules the van der Waals, Panagiotopoulos-Reid (P&R), and six Huron-Vidal type mixing rules with UNIQUAC parameters. (C) 1999 Elsevier Science B.V. All rights reserved. | - |
dc.language | English | - |
dc.language.iso | en_US | en |
dc.publisher | ELSEVIER SCIENCE BV | - |
dc.subject | VAPOR-LIQUID-EQUILIBRIA | - |
dc.subject | MIXING RULE | - |
dc.subject | GAS SOLUBILITIES | - |
dc.subject | CUBIC EQUATIONS | - |
dc.subject | PSRK METHOD | - |
dc.subject | STATE | - |
dc.subject | MIXTURES | - |
dc.subject | PREDICTION | - |
dc.subject | THERMODYNAMICS | - |
dc.subject | COMBINATION | - |
dc.title | High-pressure phase equilibria for the carbon dioxide-2-methyl-1-butanol, carbon dioxide-2-methyl-2-butanol, carbon dioxide-2-methyl-1-butanol-water, and carbon dioxide-2-methyl-2-butanol-water systems | - |
dc.type | Article | - |
dc.identifier.wosid | 000079983900006 | - |
dc.identifier.scopusid | 2-s2.0-0345161696 | - |
dc.type.rims | ART | - |
dc.citation.volume | 157 | - |
dc.citation.issue | 1 | - |
dc.citation.beginningpage | 81 | - |
dc.citation.endingpage | 91 | - |
dc.citation.publicationname | FLUID PHASE EQUILIBRIA | - |
dc.embargo.liftdate | 9999-12-31 | - |
dc.embargo.terms | 9999-12-31 | - |
dc.contributor.localauthor | Lee, Huen | - |
dc.contributor.nonIdAuthor | Lee, HS | - |
dc.contributor.nonIdAuthor | Mun, SY | - |
dc.type.journalArticle | Article | - |
dc.subject.keywordAuthor | carbon dioxide | - |
dc.subject.keywordAuthor | mixing rule | - |
dc.subject.keywordAuthor | equation of state | - |
dc.subject.keywordAuthor | high-pressure VLE data | - |
dc.subject.keywordPlus | VAPOR-LIQUID-EQUILIBRIA | - |
dc.subject.keywordPlus | MIXING RULE | - |
dc.subject.keywordPlus | GAS SOLUBILITIES | - |
dc.subject.keywordPlus | CUBIC EQUATIONS | - |
dc.subject.keywordPlus | PSRK METHOD | - |
dc.subject.keywordPlus | STATE | - |
dc.subject.keywordPlus | MIXTURES | - |
dc.subject.keywordPlus | PREDICTION | - |
dc.subject.keywordPlus | THERMODYNAMICS | - |
dc.subject.keywordPlus | COMBINATION | - |
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