A systematic study on the phase behavior
of saturated ethyl esters
with supercritical CO2 is presented. High pressure phase
behavior measurements for the systems CO2/ethyl decanoate,
CO2/ethyl dodecanoate, CO2/ethyl tetradecanoate,
and CO2/ethyl hexadecanoate were conducted in a static
synthetic view cell in the temperature range 308–358 K. Phase
transition pressures were measured in the range 5.86–23.01
MPa for ethyl ester mass fractions in the range 0.0174–0.657
and complement existing literature data. Throughout the temperature
and compositional range measured, which encompassed the liquid phase,
mixture critical region, and vapor phase, an increase in temperature
leads to an increase in phase transition pressure with no temperature
inversions or three phase regions observed. Additionally, an increase
in hydrocarbon backbone length leads to an ever-increasing phase-transition
pressure, suggesting fractionation of ethyl esters according to molecular
mass with supercritical CO2 is possible. Finally, the measured
and previously published CO2/ethyl ester data were successfully
correlated with a modified Chrastil models and the MT model. While
these models cannot easily be used predictively and depend on the
data sets used for correlation, these are simple and easy methods
that can be used to interpolate data.