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

Authors
WEI MSW BROWN TS KIDNAY AJ SLOAN ED
Citation
Msw. Wei et al., 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, Journal of chemical and engineering data, 40(4), 1995, pp. 726-731
Citations number
12
Categorie Soggetti
Engineering, Chemical",Chemistry
Journal title
Journal of chemical and engineering data → ACNP
ISSN journal
00219568
Volume
40
Issue
4
Year of publication
1995
Pages
726 - 731
Database
ISI
SICI code
0021-9568(1995)40:4<726:VPLEFT>2.0.ZU;2-E
Abstract
Vapor-liquid equilibrium data for the binary system methane + carbon d ioxide were measured at 230, 250, and 270 K. The ethane + carbon dioxi de system was studied at 207, 210, 213, 230, 250, and 270 K, and the m ethane + ethane system was. studied at 210, 230, 250, and 270 K. Terna ry vapor-liquid equilibria for the methane + ethane + carbon dioxide s ystem 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 system s, and binary interaction coefficients are reported.