Molecular Simulation of Three-body Interactions for Vapor-liquid and Solid-liquid Phase Equilibria
نویسندگان
چکیده
The phase behavior of both pure systems and binary mixtures has been widely studied by molecular simulation [1], using techniques such as the Gibbs ensemble [2], Gibbs-Duhem [3] or histogram reweighing [4] algorithms. The common aim of many of these investigations is to accurately predict the phase diagram using effective intermolecular potentials, most notable the Lennard-Jones potential. In contrast, other studies [5-11] have used molecular simulation techniques, in conjunction with genuine twoand three-body intermolecular potentials [12-14], to determine the influence of various intermolecular interactions on phase behavior. These studies have concluded that three-body interactions have a significant influence on phase behavior. Threebody interactions decrease the density of the liquid phase of pure fluids [5,6,7,9] and they contribute significantly [6] to the vapor-liquid critical point. In binary mixtures [10,11], three-body interactions are required to obtain good agreement between theory and experiment for the pressurecomposition behavior. There is also some evidence [15] that three-body interactions have a pivotal role in the transition between the different global phase behavior types of binary mixtures. Previous investigations of three-body interactions on phase equilibria have been confined largely to pure fluids. Theoretical studies have been reported [16-22] which indicate three-body interactions are important in solid phases. However, the direct molecular simulation of solid-liquid equilibria [23-25] for both pure fluids and mixtures has mainly focused on predicting phase coexistence using an effective intermolecular potential. The solid-liquid phase transition is difficult to determine accurately using traditional molecular simulation techniques. The high densities mean that it is not practical to use the Gibbs ensemble [2] because of the difficulty of exchanging particles between the phases. Although this limitation is avoided by the Gibbs-Duhem [3] technique, it is not self-starting which means it requires prior knowledge of one pair of coexistence data. Therefore, its ability to predict the phase boundary largely depends on the accuracy of the starting point data. In this work, we employed a novel approach [26] for locating the solid-liquid phase boundary which combines elements of both equilibrium and non-equilibrium molecular dynamics techniques. The approach yields reliable calculations and it avoids the problems encountered in both Gibbs ensemble and Gibbs-Duhem methods.
منابع مشابه
Prediction of Vapor-Liquid Equilibria Using CEOS /GE Models
The present study investigates the use of different GE mixing rules in cubic equations of state for prediction of phase behavior of multicomponent hydrocarbon systems. To predict VLE data in multicomponent symmetric and asymmetric mixtures such as systems that contain light gases (nitrogen, carbon dioxide, etc.) and heavy hydrocarbons, the SRK equation of state has been combined with excess Gib...
متن کاملThree-body interactions and solid-liquid phase equilibria: application of a molecular dynamics algorithm.
The effect of three-body interactions on the solid-liquid phase boundaries of argon, krypton, and xenon is investigated via a novel technique that combines both nonequilibrium and equilibrium molecular dynamics. The simulations involve the evaluation of two- and three-body forces using accurate two-body and three-body intermolecular potentials. The effect of three-body interactions is to substa...
متن کاملInfluence of two-body and three-body interatomic forces on gas, liquid, and solid phases.
Accurate molecular dynamics simulations are reported which quantify the contributions of two- and three-body interactions in the gas, liquid, and solid phases of argon at both subcritical and supercritical conditions. The calculations use an accurate two-body potential in addition to contributions from three-body dispersion interactions from third-order triple-dipole interactions. The number de...
متن کاملModeling of liquid–liquid equilibria of aqueous alcohol + salt systems using amodified NRTL
The modified NRTL (m-NRTL) model is used to represent the excess Gibbs free energy of aqueous (alcohol + electrolyte) solutions. In this work, the m-NRTL model previously developed for representation of vapor-liquid equilibria for (polymer + salt + water) systems has been extended to represent liquid-liquid equilibria of (alcohol + salt + water) systems. The proposed extension is a modified of ...
متن کاملUse of equilibrium and nonequilibrium molecular dynamics to determine solid-liquid phase coexistence at equilibrium
It is often difficult to determine the solid-liquid transition by conventional simulation techniques because of the computational challenges posed by two dense phases. Hansen and Verlet [Han69] reported the first molecular simulation results for solid-liquid phase coexistence. They used a thermodynamic integration algorithm that involves the accurate evaluation of free energies. The widely used...
متن کاملذخیره در منابع من
با ذخیره ی این منبع در منابع من، دسترسی به آن را برای استفاده های بعدی آسان تر کنید
عنوان ژورنال:
دوره شماره
صفحات -
تاریخ انتشار 2006