화학공학소재연구정보센터
Journal of Chemical and Engineering Data, Vol.40, No.4, 726-731, 1995
Vapor Plus Liquid Equilibria for the Ternary-System Methane Plus Ethane Plus Carbon-Dioxide at 230 K and Its Constituent Binaries at Temperatures from 207 to 270 K
Vapor-liquid equilibrium data for the binary system methane + carbon dioxide were measured at 230, 250, and 270 K. The ethane + carbon dioxide system was studied at 207, 210, 213, 230, 250, and 270 K, and the methane + ethane system was. studied at 210, 230, 250, and 270 K. Ternary vapor-liquid equilibria for the methane + ethane + carbon dioxide system were measured at 230 K over the pressure range from 1.15 to 6.59 MPa. The Peng-Robinson equation of state was used to model the systems, and binary interaction coefficients are reported.