Abstract
PVT data are presented for 38 reservoir fluids counting fluids dominated by paraffins, heavy aromatic fluids with a significant content of C81+ and high-temperature-high-pressure (HT/HP) reservoir fluids. By properly taking into account the compositional differences, these fluid types can all be represented using a classical cubic equation of state (SRK or PR) with volume correction. The plus fraction is split into carbon number fractions and EOS model parameters assigned to each fraction. To keep the number of components at a manageable level the carbon number fractions are lumped into pseudocomponents, each containing several carbon number fractions. Hydrocarbons as heavy as C200 are considered when splitting up the plus fraction. Neglecting the content of components heavier than C80 will give a false picture of the phase behavior of heavy aromatic fluids. Correlations are presented for Tc, Pc and ω as a function of molecular weight and density. Problems are experienced representing the thermal expansion of stable oils using cubic equations of state in the classical form. It is shown that this deficiency can be cured by introduction of a temperature dependent volume correction term.