For polymers, the energy and co-volume parameters of cubic equations o
f state can be reliably estimated using only two low-pressure volumetr
ic data points. This procedure is applied to the van der Waals equatio
n of state, and bubble-point pressure calculations are performed for a
number of polymer solutions. The van der Waals one-fluid mixing rules
are used. The Berthelot combining rule is used for estimating the cro
ss energy parameter, while the usual arithmetic mean combining rule is
used for evaluating the cross co-volume parameter. Deviations from Be
rthelot's combining rule are taken into account via a simple method re
quiring only the molecular weight of the solvent. It is shown that whe
n the proposed method is applied, the van der Waals equation of state
can predict the equilibrium pressures of polymer solutions. The accura
cy of the predictions is very good, comparable to those of other more
complex equations of state, but it is in general inferior to those of
the free-volume activity coefficient models. The simplicity, accuracy
and general applicability of the proposed method makes it an attractiv
e alternative to previously proposed complex models for prediction of
equilibrium pressures of nearly athermal and non-polar polymer solutio
ns.