… This article is the fifth in the series. The purposes of the present revision and extension are
… parameters of Table II have improved the reliability of UNIFAC vapor-liquid equilibrium predic…

… The group contribution method UNIFAC has become very … vapor−liquid equilibria. With the
help of new data stored in the Dortmund Data Bank (DDB), many gaps in the existing UNIFAC …

… to reportfurther extensions and revisions of the UNIFAC parameter tables. UNIFAC Parameters
The UNIFAC group contribution method is based on the solution of groups concept. The …

… extensions and revisions of the UNIFAC parameter tables. New Parameters (Extension) In
this work we have extended the UNIFAC group… vapor-liquid equilibrium data published until …

… [8] noted that extension of UNIFAC-ZM model could be … supercritical fluids, while extension
of UNIFAC-FV would be … been extended by addition of a free-volume term of the UNIFAC-…

… The most reliable group … for vapor−liquid equilibria (VLE), activity coefficients at infinite
dilution (γ ∞ ), excess enthalpies (h E ), liquid−liquid equilibria (LLE), solid−liquid equilibria of …

… group contribution model modified UNIFAC (Dortmund) for the prediction of phase equilibria
… pairs using vapor–liquid equilibria (VLE), h E , and γ ∞ data stored in the NIST databank. …

… All previously published vapor-liquid equilibrium data points for binary … an extension to the
UNIFAC group assignment for common refrigerants. It is shown that ten new main groups are …

… revised parameters for several groups and new parameters for 52 pairs of groups for which
… used by our groups in Dortmund and Lyngby for vapor-liquid equilibrium predictions in the …

… While ASOG and the original UNIFAC method were developed mainly for the prediction
of vapor−liquid equilibria (VLE) and azeotropic data, the modified versions of UNIFAC also …