Abstract In this paper, we advocate the use of the Tunnelling global optimization method for phase stability analysis and for multiphase equilibria calculations. The method had been successfully used for solving a variety of phase-equilibrium problems. The Tunnelling method has two steps. First, a minimum (which may not be the putative global minimum) of the objective function is found by a local bounded minimization algorithm. In a second step, the method checks for global optimality. If the minimum found in the first step is only a local minimum, a feasible initial estimate for a new minimization is generated in another valley of the objective function. Cubic equations of state are used, but any thermodynamic model for the Gibbs free energy can be used (the method being model-independent). The proposed method has proven to be an efficient and reliable tool for multiphase equilibrium calculation. Introduction The methods for multiphase equilibria calculation based on the equality of chemical potentials cannot guarantee the convergence to the correct solution since the problem is non-convex (i.e., several local minima exist), and such methods can find only one minimum for a given initial guess. Moreover, the global optimization methods currently available are generally very time consuming. A global optimization method(1, 2), called Tunnelling, able to escape from local minima and saddle points, is used in this work for the direct minimization of the Gibbs free energy and of the tangent plane distance function (TPD). The Tunnelling method has two phases. In phase one, a local bounded optimization method is used to minimize the objective function. In phase two (tunnelization), either global optimality is ascertained or a feasible initial estimate for a new minimization is generated. The Tunnelling method has shown its ability in efficiently solving difficult non-convex, highly non-linear problems. Different kinds of phase equilibrium problems were solved using Tunnelling(3–6). The problems addressed here are vapour-liquid and liquid-liquid two-phase equilibria, three-phase vapour-liquid-liquid equilibria, and three-phase vapour-liquid-solid equilibria for a variety of representative systems. We use in this work a general form of cubic equation of state (EOS), incorporating the Soave-Redlich-Kwong (SRK) and Peng- Robinson (PR) EOS. Multiphase Equilibrium Equations Phase Splitting According to the second law of thermodynamics, at the equilibrium state, a system of nc components of composition z = (z1, z2,...,znc)T has the lowest possible Gibbs free energy from all possible states. The dimensionless Gibbs free energy is expressed as:
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