High-pressure Phase Equilibria for Carbon Dioxide-2-Methyl-2-Propanol and Carbon Dioxide-2-Methyl-2-Propanol-Water: Measurement and Prediction

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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.
Issue Date
1994-12-01
Language
ENG
Citation

The 7th Symposium on Chemical Engineering Taejeon/Chungnam-Kyushu, pp.0 - 0

URI
http://hdl.handle.net/10203/114959
Appears in Collection
CBE-Conference Papers(학술회의논문)
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