This paper presents an improved version of a purely predictive thermodynamic model proposed
previously by Coniglio et al. (Fluid
Phase Equilib.
1993, 87, 53−88). The main feature of this
model is to be based on a Peng−Robinson type equation of state with parameters determined
through homogeneous group contribution methods. The new model estimates vapor pressures,
saturated liquid densities, heats of vaporization, saturated liquid heat capacities, and speed of
sound in saturated liquids of a large number of hydrocarbons within the experimental accuracy,
from the triple point to 2 bar. The required inputs for each compound are the molecular structure
and the experimental normal boiling point or at least one vapor pressure measurement. The
applicability of the new model was verified through prediction of vapor pressures of non-hydrocarbon organic compounds (acids, esters, alcohols, ...). The obtained results confirm the
reliability of the new model when extrapolating to non-hydrocarbon organic compounds.