The solid–liquid–gas
equation of state (SLV-EOS)
is based on the initial cubic equation of state, the van der Waals
equation. Since the van der Waals equation is not accurate enough
to predict gas–liquid properties, SLV-EOS cannot better predict
the gas–liquid properties of hydrocarbons in actual gas reservoirs.
Therefore, a modified solid–liquid–gas unified equation
of state was constructed inthis paper, which was developed using the
material’s actual critical compressibility factor
Z
c
. The minimum liquid-phase volume at the triple point
is also introduced to limit the value of
c
in the
equation, which effectively avoids the solution of Maxwell’s
equal-area rule in the solid–liquid transformation process.
The model extends the classical Peng–Robinson equation of state
for fluid-only (liquid and vapor) states. The predicted
p
-
T
and
p
-ρ phase transition
diagrams are reported in this paper for methane, ethane, propane,
carbon dioxide, hydrogen sulfide, and sulfur, and they are in good
agreement with the experimental data. This methodology is suitable
for any substance for which the density of the solid phase is higher
than that of the liquid phase. Additionally, the modified SLV equation
can be used to estimate the solubility of solid sulfur in the absence
of relevant experimental data.