Vapor-Liquid Equilibrium Measurement for the Binary System of Carbon Dioxide (CO2) + 1,1,1-Trifluoroethane (R-143a) at High Pressures

Monday, November 9, 2009
Ryman Hall B1/B2 (Gaylord Opryland Hotel)

Seol A. Kim, Department of Chemical and Biomolecular Engineering, Sogang University, Seoul, South Korea
Ah Ram Kim, Department of Chemical and Biomolecular Engineering, Sogang University, Seoul, South Korea
Ki-Pung Yoo, Department of Chemical and Biomolecular Engineering, Sogang University, Seoul, South Korea
Jong Sung Lim, Department of Chemical and Biomolecular Engineering, Sogang University, Seoul, South Korea

PTxy measurements for the binary system of carbon dioxide (CO2) + 1,1,1-trifluoroethane (HFC-143a) were measured at seven equally spaced temperatures of (273.15, 283.15, 293.15, 303.15, 313.15, 323.15 and 333.15) K, by using a circulation-type equilibrium apparatus in which both vapor and liquid phases were recirculated. The experimental data were correlated with the Peng-Robinson equation of state (PR-EoS) using the Wong-Sandler mixing rule combines with the NRTL excess Gibbs free energy model and the Carnahan–Starling–De Santis equation of state (CSD EoS). Almost all the calculated values with these models show good agreement with the experimental data.
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