Densities and vapor-liquid compositions for twelve complex mixtures (c
rude oil and natural gas) are calculated using a lattice fluid model e
quation of state. Fractions of the heavy ends are approximated as pseu
docomponents defined in terms of their 'equivalent normal alkane'. The
lattice fluid model equation of state of Sanchez-Lacombe is used, thr
ee parameters are required for each pure component and one binary inte
raction parameter (zeta(ij)) is required for each unlike pair. Binary
interaction parameters are developed for 56 binary mixtures whose comp
onents are typical of those found in petroleum systems. It is seen tha
t, even though pseudocomponent are defined in very simple manner, the
predicted results for multicomponent systems are comparable to or bett
er than many popular alternative methods. (C) 1997 Elsevier Science B.
V.