In this work, a series of bubble-point measurements were carried out on the binary system butane + decane. The experiments were carried out using the Cailletet apparatus, and bubble-point pressures were measured in a temperature range of (323.21 to 482.28) K. The corresponding pressures were predicted using the Peng-Robinson equation of state, and the relative errors were estimated. It is shown that this hydrocarbon mixture can be predicted reasonably well by this equation of state.
Compounds
#
Formula
Name
1
C4H10
butane
2
C10H22
decane
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.