A Study of Equation-Solving and Gibbs Free Energy Minimization Methods for Phase Equilibrium Calculations

Phase equilibrium calculations are often involved in the design, simulation, and optimization of chemical processes. Reported methods for these calculations are based on either equation-solving or Gibbs free energy minimization approaches. The main objective of this work is to compare selected metho...

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Published inChemical engineering research & design Vol. 80; no. 7; pp. 745 - 759
Main Authors Teh, Y.S., Rangaiah, G.P.
Format Journal Article
LanguageEnglish
Published Rugby Elsevier B.V 01.10.2002
Institution of Chemical Engineers
Subjects
Online AccessGet full text
ISSN0263-8762
1876-4800
1744-3563
1744-3598
0957-5820
DOI10.1205/026387602320776821

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Abstract Phase equilibrium calculations are often involved in the design, simulation, and optimization of chemical processes. Reported methods for these calculations are based on either equation-solving or Gibbs free energy minimization approaches. The main objective of this work is to compare selected methods for these two approaches, in terms of reliability to find the correct solution, computational time, and number of K-value evaluations. For this, four equation-solving and three free minimization methods have been selected and applied to commonly encountered vapour–liquid equilibrium (VLE), liquid–liquid equilibrium (LLE), and vapour–liquid–liquid equilibrium (VLLE) examples involving multiple components and popular thermodynamic models. Detailed results show that the equation-solving method based on the Rachford–Rice formulation accompanied by mean value theorem and Wegstein's projection is reliable and efficient for two-phase equilibrium calculations not having local minima. When there are multiple minima and for three-phase equilibrium, the stochastic method, genetic algorithm (GA) followed by modified simplex method of Nelder and Mead (NM) is more reliable and desirable. Generic programs for numerical methods are ineffective for phase equilibrium calculations. These findings are of interest and value to researchers and engineers working on phase equilibrium calculations and/or developing thermodynamic models for phase behaviour.
AbstractList Phase equilibrium calculations are often involved in the design, simulation and optimisation of chemical processes. Reported methods for these calculations are based on either equation-solving or Gibbs free energy minimisation approaches. The main objective of this work is to compare selected methods for the 2 approaches, in terms of reliability, computational time, and number of k-value evaluations. For this comparison, 4 equation-solving and 3 minimisation methods have been applied to commonly found vapour-liquid equilibrium (VLE), liquid-liquid equilibrium (LLE) and vapour-liquid-liquid equilibrium (VLLE) examples. Results are presented and discussed. (Original abstract - amended)
Phase equilibrium calculations are often involved in the design, simulation, and optimization of chemical processes. Reported methods for these calculations are based on either equation-solving or Gibbs free energy minimization approaches. The main objective of this work is to compare selected methods for these two approaches, in terms of reliability to find the correct solution, computational time, and number of K-value evaluations. For this, four equation-solving and three free minimization methods have been selected and applied to commonly encountered vapour–liquid equilibrium (VLE), liquid–liquid equilibrium (LLE), and vapour–liquid–liquid equilibrium (VLLE) examples involving multiple components and popular thermodynamic models. Detailed results show that the equation-solving method based on the Rachford–Rice formulation accompanied by mean value theorem and Wegstein's projection is reliable and efficient for two-phase equilibrium calculations not having local minima. When there are multiple minima and for three-phase equilibrium, the stochastic method, genetic algorithm (GA) followed by modified simplex method of Nelder and Mead (NM) is more reliable and desirable. Generic programs for numerical methods are ineffective for phase equilibrium calculations. These findings are of interest and value to researchers and engineers working on phase equilibrium calculations and/or developing thermodynamic models for phase behaviour.
Author Rangaiah, G.P.
Teh, Y.S.
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Issue 7
Keywords vapour–liquid equilibrium
liquid–liquid equilibrium
equation-solving approach
Gibbs free energy minimization
vapour–liquid-liquid equilibrium
Gibbs free energy
Thermodynamic model
Liquid liquid vapor equilibrium
Liquid vapor equilibrium
Multiphase equilibrium
Minimization
Equation resolution
Phase equilibrium
Liquid liquid equilibrium
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SSID ssj0001748
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Snippet Phase equilibrium calculations are often involved in the design, simulation, and optimization of chemical processes. Reported methods for these calculations...
Phase equilibrium calculations are often involved in the design, simulation and optimisation of chemical processes. Reported methods for these calculations are...
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SubjectTerms Chemical thermodynamics
Chemistry
equation-solving approach
Exact sciences and technology
General and physical chemistry
General. Theory
Gibbs free energy minimization
liquid–liquid equilibrium
Phase equilibria
vapour–liquid equilibrium
vapour–liquid-liquid equilibrium
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Title A Study of Equation-Solving and Gibbs Free Energy Minimization Methods for Phase Equilibrium Calculations
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http://scholarbank.nus.edu.sg/handle/10635/66425
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