This paper presents an evaluation of the performance of cubic equation
s of state in the prediction of the phase behavior of hyperbaric mixtu
res. It points out a number of problems that should be resolved in a c
ooperative way. Items related to EoS parameter definitions such as int
eraction coefficients, critical properties of hydrocarbon compounds an
d volume translation are investigated. VLE experimental data, isotherm
al flash compositional and volumetric data up to 4000 bar as well as P
VT data up to 2000 bar for binary mixtures and synthetic multicomponen
t systems have been considered in this study. Correlation and predicti
on results are presented with the translated and modified Peng-Robinso
n (t-mPR) EoS. It is shown that serious problems are encountered at hi
gh pressure, when extrapolated interaction coefficients are used. Pred
iction of saturation pressures of gas condensates is more satisfactory
when binary interaction parameters are obtained from high pressure de
w point correlations. Compositional and volumetric predictions are rem
arkable under the assumption that definition of the EoS parameters is
based on high pressure VLE binary data. Contradictory results are obta
ined with different methods for estimating the critical properties of
high molecular weight hydrocarbons. Generalized expressions for the vo
lume translation appear to be very efficient even at very high tempera
tures and pressures (up to 2000 bar).