In
a phase envelope, an adequate description of the critical point
is of high importance. It identifies the conditions where the bubble
and dew curves meet, and where the nature of the single phase region
outside the phase envelope changes. The knowledge of the mixture critical
point is relevant to preventing production and transport problems,
as well as to optimizing near-critical and supercritical processes.
A modified cubic plus association (CPA) model was recently shown to
accurately describe the vapor–liquid equilibrium (VLE) critical
temperatures and pressures of pure compounds. The model is usually
fitted to pure component data between 0.45T
r and 0.85T
r, while forcing the correct
description of both T
c and P
c. Here, the performance of the model is evaluated for
mixtures. Interaction parameters are regressed from VLE/liquid–liquid
equilibrium (LLE) data at lower temperatures. Accurate results, for
binary and ternary mixtures, were obtained. These results concern
mainly mixtures containing, water, alkanes, alkanols, and amines.
The results obtained are compared to those from perturbed-chain statistical
associating fluid theory (PC-SAFT), simplified CPA (s-CPA), and Soave–Redlich–Kwong.
Results for liquid–liquid critical temperatures are also analyzed
for mixtures of methanol/ethanol with alkanes. The average absolute
deviations with this approach, when considering VLE fitted binary
interaction parameters, are 0.58 for T
c and 5.18 for P
c, for the VL critical
point (CP) data in analysis. For LL CP, the model can describe the
results for compounds, with similar critical properties, as is the
case of methanol and hexane.