Prediction of gas solubility and vapor-liquid equilibria by group contribution

This publication has 13 references indexed in Scilit:

• A modified UNIFAC group-contribution model for prediction of phase equilibria and heats of mixing
  Industrial & Engineering Chemistry Research, 1987
• A note on the derivation of mixing rules from excess Gibbs energy models
  Fluid Phase Equilibria, 1986
• A new group-contribution equation of state for vapor-liquid equilibria
  Industrial & Engineering Chemistry Fundamentals, 1986
• Generating appropriate density values from a cubic state equation to avoid false unit K values. Application to distillation problems
  Industrial & Engineering Chemistry Process Design and Development, 1984
• Gas solubility calculations. II. Application of a new group-contribution equation of state
  Fluid Phase Equilibria, 1984
• Gas solubility calculations. I. Unifac
  Fluid Phase Equilibria, 1983
• Extension of the Peng-Robinson equation of state to complex mixtures: Evaluation of the various forms of the local composition concept
  Fluid Phase Equilibria, 1983
• Numerical aspects of the implementation of cubic equations of state in flash calculation routines
  Computers & Chemical Engineering, 1982
• New mixing rules in simple equations of state for representing vapour-liquid equilibria of strongly non-ideal mixtures
  Fluid Phase Equilibria, 1979
• Local compositions in thermodynamic excess functions for liquid mixtures
  AIChE Journal, 1968