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David M. Heyes

Publications and source records attributed to David M. Heyes.

3 recordsLinked to original sources

Chemical potential of a test hard sphere of variable size in hard-sphere fluid mixtures

A detailed comparison between the Boublík-Mansoori-Carnahan-Starling-Leland (BMCSL)equation of state of hard-sphere mixtures is made with Molecular Dynamics (MD) simulations of the same compositions. The Labík and Smith simulation technique [S. Labík and W. R. Smith, Mol. Simul. \textbf{12}, 23-31 (1994)] was used to implement the Widom particle insertion method to calculate the excess chemical potential, $βμ_0^\text{ex}$, of a test particle of variable diameter, $σ_0$, immersed in a hard-sphere fluid mixture with different compositions and values of the packing fraction, $η$. Use is made of the fact that the only polynomial representation of $βμ_0^\text{ex}$ which is consistent with the limits $σ_0\to 0$ and $σ_0\to\infty$ has to be of the cubic form, i.e., $c_0(η)+\overline{c}_1(η)σ_0/M_{1}+\overline{c}_2(η)(σ_0/M_{1})^2+\overline{c}_3(η)(σ_0/M_{1})^3$, where $M_{1}$ is the first moment of the distribution. The first two coefficients, $c_0(η)$ and $\overline{c}_1(η)$, are known analytically, while $\overline{c}_2(η)$ and $\overline{c}_3(η)$ were obtained by fitting the MD data to this expression. This in turn provides a method to determine the excess free energy per particle, $βa^\text{ex}$, in terms of $\overline{c}_2$, $\overline{c}_3$, and the compressibility factor, $Z$. Very good agreement between the BMCSL formulas and the MD data is found for $βμ^\text{ex}_0$, $Z$, and $βa^\text{ex}$ for binary mixtures and continuous particle size distributions with the top-hat analytic form. However, the BMCSL theory typically slightly underestimates the simulation values, especially for $Z$, differences which the Boublík-Carnahan-Starling-Kolafa formulas and an interpolation between two Percus-Yevick routes capture well in different ranges of the system parameter space.

cond-mat.soft

Chemical potential of a test hard sphere of variable size in a hard-sphere fluid

The Labík and Smith Monte Carlo simulation technique to implement the Widom particle insertion method is applied using Molecular Dynamics (MD) instead to calculate numerically the insertion probability, $P_0(η,σ_0)$, of tracer hard-sphere (HS) particles of different diameters, $σ_0$, in a host HS fluid of diameter $σ$ and packing fraction, $η$, up to $0.5$. It is shown analytically that the only polynomial representation of $-\ln P_0(η,σ_0)$ consistent with the limits $σ_0\to 0$ and $σ_0\to\infty$ has necessarily a cubic form, $c_0(η)+c_1(η)σ_0/σ+c_2(η)(σ_0/σ)^2+c_3(η)(σ_0/σ)^3$. Our MD data for $-\ln P_0(η,σ_0)$ are fitted to such a cubic polynomial and the functions $c_0(η)$ and $c_1(η)$ are found to be statistically indistinguishable from their exact solution forms. Similarly, $c_2(η)$ and $c_3(η)$ agree very well with the Boublík-Mansoori-Carnahan-Starling-Leland and Boublík-Carnahan-Starling-Kolafa formulas. The cubic polynomial is extrapolated (high density) or interpolated (low density) to obtain the chemical potential of the host fluid, or $σ_{0}\toσ$, as $βμ^{\text{ex}}=c_0+c_1+c_2+c_3$. Excellent agreement between the Carnahan-Starling and Carnahan-Starling-Kolafa theories with our MD data is evident.

cond-mat.soft

Line of critical states for Lennard-Jones fluids

A method of obtaining the critical temperature from within a supercritical mesophase bounded by percolation transition loci is described. We report thermodynamic pressures from MD simulations for more than 2000 state points along 7 near-critical isotherms of a Lennard-Jones fluid. Direct evaluation of Gibbs chemical potential along the critical isotherm reaffirms the existence of a supercritical mesophaseand a line of critical states and non-existence of van der Waals critical point.

cond-mat.stat-mech