This paper reports experimental phase equilibrium data for the systems {CO2 (1) + solketal (2)} and {CO2 (1) + solketal (2) + oleic acid (3)}. The phase transition pressure measurements for ternary mixtures were carried out by injecting a known amount of carbon dioxide into a mixture with fixed molar ratios of the two other components (0.75 solketal + 0.25 oleic acid). A variable-volume cell with a front window was used for the measurements. The experimental data were measured over the temperature range from (308 to 338) K and at pressures of up to 20 MPa. Bubble point conditions were measured for the binary system {CO2 (1) + solketal (2)}, whereas bubble and dew point conditions were measured for the ternary system {CO2 (1) + solketal (2) + oleic acid (3)}. Phase equilibrium modeling with the Peng Robinson equation of state was successful in describing the behavior of the investigated systems.
Compounds
#
Formula
Name
1
C18H34O2
(Z)-9-octadecenoic acid
2
CO2
carbon dioxide
3
C6H12O3
2,2-dimethyl-1,3-dioxolane-4-methanol
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.