The new phase behavior prediction method of petroleum fluids, which was rec
ently developed by Manafi et al. for simple petroleum fluids, has been modi
fied and extended for application to complex petroleum fluids. A combinatio
n of the Peng-Robinson equation of state for phase behavior prediction and
the Riazi and Mansoori equation of state for density prediction has been ap
plied. The proposed method is applicable for various equations of state as
long as they give accurate prediction of phase behavior and densities of hy
drocarbons and their mixtures. The composition of petroleum fluids is descr
ibed by discrete and plus fraction parts. For the plus-fraction of petroleu
m fluids, appropriate distribution functions for molecular mass, true boili
ng point and specific gravity are used. The distribution functions required
an average value of molecular mass, and specific gravity of the plus-fract
ion as input data. Phase behavior calculations are performed for prediction
of saturation pressure as well as flash liberation, differential liberatio
n and flash-separation, in a wide range of pressures and temperatures for s
ix different complex petroleum fluids and compared with experimental data.
It is demonstrated that the proposed method can predict the phase behavior
of complex petroleum fluids mixtures quite accurately. (C) 2001 Elsevier Sc
ience B.V. All rights reserved.