Binary vapor-liquid equilibrium data were measured for the 1,1,1-trifluoroethane (HFC-143a) + n-butane (HC-600) system at temperatures from (313.15 to 363.15) K. This experiment was carried out with a circulatingtype apparatus with online gas chromatography. The experimental data were correlated well by Peng-Robinson- Stryjek-Vera equation of state with the Wong-Sandler mixing rules. The average absolute deviation of pressure and vapor composition between the measured data and the correlation was below 0.98 % and 0.0128, respectively.
Compounds
#
Formula
Name
1
C2H3F3
1,1,1-trifluoroethane
2
C4H10
butane
Datasets
The table above is generated from the ThermoML associated json file (link above).
POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied;
the numbers refer to the table of compounds on the left.