Thermodynamic calculations using a simulated annealing optimization algorithm

In Chemical Engineering, several thermodynamic calculations can be formulated as optimization problems with or without restrictions. As indicated by Henderson et al. [1] the formulation of thermodynamic calculations for optimization problems offers some advantages: a) the use of a robust optimization method, b) the possibility of using a direct optimization method which requires only calculations of the objective function and c) the use of an iterative procedure whose convergence is almost independent on the initial guesses. Some examples of these calculations are phase stability analysis, phase equilibrium problems, parameter estimation in thermodynamic models, calculation of critical points, among others. These problems are non-linear, multivariable and the objective function used as optimization criterion is non-convex with several local optimums. By consequence, its solving with local optimization methods is not reliable because they generally converge to local optimums. During the last years, the development and application of global optimization strategies have increased in many areas of Chemical Engineering. Global optimization methods can be classified as deterministic and stochastic [2]. The first class offers a guarantee to find the global optimum of the objective function [21, 32, 24]. However, these strategies often require high computational time (generally more time than stochastic methods) and in some cases the problem reformulation is needed. In the other hand, stochastic optimization methods are robust numerical tools that present a reasonable computational effort in the optimization of multivariable functions; they are applicable to ill-structure or unknown structure problems and can be used with all thermodynamic models [3]. Thermodynamic Calculations Using a Simulated Annealing Optimization Algorithm

[1]  R. P. Marques,et al.  Modeling and analysis of the isothermal flash problem and its calculation with the simulated annealing algorithm , 2001 .

[2]  M. Stadtherr,et al.  Reliable Nonlinear Parameter Estimation in VLE Modeling , 2000 .

[3]  G. Froment,et al.  A hybrid genetic algorithm for the estimation of parameters in detailed kinetic models , 1998 .

[4]  N. Aslam,et al.  Sensitivity of azeotropic states to activity coefficient model parameters and system variables , 2006 .

[5]  Masao Fukushima,et al.  Hybrid simulated annealing and direct search method for nonlinear unconstrained global optimization , 2002, Optim. Methods Softw..

[6]  H. Gregor,et al.  MOLAL ACTIVITY COEFFICIENTS OF METHANE— AND ETHANESULFONIC ACIDS AND THEIR SALTS , 1963 .

[7]  N. Metropolis,et al.  Equation of State Calculations by Fast Computing Machines , 1953, Resonance.

[8]  Mark A. Stadtherr,et al.  Modeling of Activity Coefficients of Aqueous Solutions of Quaternary Ammonium Salts with the Electrolyte-NRTL Equation , 2004 .

[9]  Robert W. Maier,et al.  Reliable computation of homogeneous azeotropes , 1998 .

[10]  S. T. Harding,et al.  Locating all homogeneous azeotropes in multicomponent mixtures , 1997 .

[11]  A. Bonilla-Petriciolet,et al.  Performance of Stochastic Global Optimization Methods in the Calculation of Phase Stability Analyses for Nonreactive and Reactive Mixtures , 2006 .

[12]  Alexander H. G. Rinnooy Kan,et al.  A stochastic method for global optimization , 1982, Math. Program..

[13]  Marcelo Castier,et al.  Automatic implementation of thermodynamic models for reliable parameter estimation using computer algebra , 2002 .

[14]  H. Renon Models for excess properties of electrolyte solutions: molecular bases and classification, needs and trends for new developments , 1996 .

[15]  F. Pessoa,et al.  Parameter estimation of thermodynamic models for high-pressure systems employing a stochastic method of global optimization , 2000 .

[16]  Yushan Zhu,et al.  A reliable prediction of the global phase stability for liquid-liquid equilibrium through the simulated annealing algorithm: Application to NRTL and UNIQUAC equations , 1999 .

[17]  S. Lindenbaum,et al.  Structural Effects on the Osmotic and Activity Coefficients of the Quaternary Ammonium Halides in Aqueous Solutions at 25°1 , 1966 .

[18]  J. K. Axmann,et al.  Evolutionary algorithms for the optimization of Modified UNIFAC parameters , 1998 .

[19]  L. E. Baker,et al.  Gibbs energy analysis of phase equilibria , 1982 .

[20]  M. Stadtherr,et al.  Deterministic global optimization for error-in-variables parameter estimation , 2002 .

[21]  Patrick Siarry,et al.  Tabu Search applied to global optimization , 2000, Eur. J. Oper. Res..

[22]  Gade Pandu Rangaiah,et al.  Tabu search for global optimization of continuous functions with application to phase equilibrium calculations , 2003, Comput. Chem. Eng..

[23]  Dr. Zbigniew Michalewicz,et al.  How to Solve It: Modern Heuristics , 2004 .

[24]  C. D. Gelatt,et al.  Optimization by Simulated Annealing , 1983, Science.

[25]  M. Montaz Ali,et al.  A direct search variant of the simulated annealing algorithm for optimization involving continuous variables , 2002, Comput. Oper. Res..

[26]  S. Bandyopadhyay,et al.  Modelling Vapour − Liquid Equilibrium of CO2 in Aqueous N‐Methyldiethanolamine through the Simulated Annealing Algorithm , 2008 .

[27]  K. Kobe The properties of gases and liquids , 1959 .

[28]  M. Michelsen The isothermal flash problem. Part I. Stability , 1982 .

[29]  Nélio Henderson,et al.  Prediction of critical points: A new methodology using global optimization , 2004 .

[30]  G. P. Rangaiah,et al.  A Study of Equation-Solving and Gibbs Free Energy Minimization Methods for Phase Equilibrium Calculations , 2002 .

[31]  Sandro Ridella,et al.  Minimizing multimodal functions of continuous variables with the “simulated annealing” algorithmCorrigenda for this article is available here , 1987, TOMS.

[32]  S. Lindenbaum,et al.  Osmotic and Activity Coefficients for the Symmetrical Tetraalkyl Ammonium Halides in Aqueous Solution at 25°1 , 1964 .

[33]  J. Gmehling,et al.  Vapor-liquid equilibrium data collection. Aqueous-organic systems , 1977 .

[34]  J. Smith,et al.  Introduction to chemical engineering thermodynamics , 1949 .

[35]  M. Stadtherr,et al.  Enhanced Interval Analysis for Phase Stability: Cubic Equation of State Models , 1998 .

[36]  Angelo Lucia,et al.  Simulation of refrigerant phase equilibria , 1997 .

[37]  G. P. Rangaiah Evaluation of genetic algorithms and simulated annealing for phase equilibrium and stability problems , 2001 .

[38]  Manish K. Singh,et al.  Genetic algorithm to estimate interaction parameters of multicomponent systems for liquid-liquid equilibria , 2005, Comput. Chem. Eng..

[39]  Nélio Henderson,et al.  Novel approach for the calculation of critical points in binary mixtures using global optimization , 2004 .

[40]  William R. Esposito,et al.  Global Optimization in Parameter Estimation of Nonlinear Algebraic Models via the Error-in-Variables Approach , 1998 .

[41]  S. T. Harding,et al.  Phase stability with cubic equations of state: Global optimization approach , 2000 .

[42]  J. Gaube J. Gmehling, U. Onken: Vapor‐Liquid Equilibrium Data Collection, Aqueous‐Organic Systems, in der Reihe: Chemistry Data Series, Vol. I, Part. 1. DECHEMA, Frankfurt 1977. 698 Seiten, Preis: DM 120,‐ , 1978 .

[43]  Gade Pandu Rangaiah,et al.  Implementation and evaluation of random tunneling algorithm for chemical engineering applications , 2006, Comput. Chem. Eng..

[44]  Herbert I. Britt,et al.  Local composition model for excess Gibbs energy of electrolyte systems. Part I: Single solvent, single completely dissociated electrolyte systems , 1982 .