Most of the world’s helium
supply is obtained by the cryogenic distillation of natural gas. Modeling
the distillation conditions requires equations of state capable of
predicting vapor–liquid equilibria over wide ranges of conditions.
Equations of state, including cubic equations and multiparameter Helmholtz
models, depend on the critical properties of pure substances for
predicting various properties of multicomponent fluid mixtures. Predictions
for helium are problematic as its critical point (5.195 K, 0.2275
MPa) is influenced strongly by quantum effects; large, empirical interaction
parameters tend to be used in equations of state to compensate for
these effects. Prausnitz and co-workers proposed an alternative approach
using effective critical constants for quantum gases but demonstrated
it for only three helium-containing binary mixtures. Here, we demonstrate
that the use of an effective critical point at (11.73 K, 0.568 MPa)
for helium substantially improves the prediction of VLE by the Peng–Robinson
equation of state for 15 binary and 2 ternary mixtures, including
the major components of natural gas. This effective critical point
for helium was selected from a critical analysis of pTxy data for the (methane + helium) binary. The effective critical constants
for helium are compatible with an acentric factor near zero, as expected
for a small spherical molecule and similar to the acentric factors
of heavy noble gases. The possibility of applying this approach to
address recognized limitations of the GERG-2008 equation of state
is discussed.