To improve the SRK equation of state for the calculation of vapor-liquid eq
uilibria of petroleum fluids, the parameters of the Mathias-Copeman alpha-f
unction were refitted to a large number of experimental vapor-pressure data
(15,311 data points) stored in the Dortmund Data Bank with a particular vi
ew to improving the accuracy of the vapor-pressure correlation in the low p
ressure range. Using the new parameters, vapor-liquid equilibria were calcu
lated using two different mixing rules: the group contribution mixing rule
for the mixture parameters a of the SRK EOS; the conventional mixing rules
for the mixture parameters a and b of the SRK EOS together with a character
ization method developed on the basis of existing empirical correlations fo
r the properties of plus fractions of undefined mixtures. The results show
that the accuracy for crude oil and natural gas mixtures can be improved by
refitting the SRK EOS parameters.