DC Field | Value | Language |
---|---|---|
dc.contributor.author | Kim, JS | - |
dc.contributor.author | Lee, Huen | - |
dc.date.accessioned | 2013-03-15T00:22:05Z | - |
dc.date.available | 2013-03-15T00:22:05Z | - |
dc.date.created | 2012-02-06 | - |
dc.date.issued | 1994-12-01 | - |
dc.identifier.citation | The 7th Symposium on Chemical Engineering Taejeon/Chungnam-Kyushu, v., no., pp.0 - 0 | - |
dc.identifier.uri | http://hdl.handle.net/10203/114959 | - |
dc.description.abstract | High-pressure vapor-liquid equilibria for the binary system carbon dioxide-2-methyl-2-propanol were measured at 299.0, 323.2, and 343.2 K. For the ternary system carbon dioxide-2-methyl-2-propanol-water equilibrium compositions were measured at 323.2 K and pressures of 60, 80, 100, and 120 bar. An isothermal three-phase region at 323.2 K and phase equilibria at 60 and 80 bar are also presented. The experimental data were correlated with the Soave-Redlich-Kwong equation of state with the modified Huron-Vidal second-order mixing rule. The model was able to provide good predictions of the phase behavior of all systems considered in this study. | - |
dc.language | ENG | - |
dc.title | High-pressure Phase Equilibria for Carbon Dioxide-2-Methyl-2-Propanol and Carbon Dioxide-2-Methyl-2-Propanol-Water: Measurement and Prediction | - |
dc.type | Conference | - |
dc.type.rims | CONF | - |
dc.citation.beginningpage | 0 | - |
dc.citation.endingpage | 0 | - |
dc.citation.publicationname | The 7th Symposium on Chemical Engineering Taejeon/Chungnam-Kyushu | - |
dc.identifier.conferencecountry | Japan | - |
dc.identifier.conferencecountry | Japan | - |
dc.contributor.localauthor | Lee, Huen | - |
dc.contributor.nonIdAuthor | Kim, JS | - |
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