Monte Carlo Simulations of Fluid Phase Equilibria and Interfacial Properties for Water/Alkane Mixtures: An Assessment of Nonpolarizable Water Models and of Departures from the Lorentz-Berthelot Combining Rules

Bai Xue, David B. Harwood, Jingyi L. Chen, J. Ilja Siepmann

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Abstract

Monte Carlo simulations in the Gibbs ensemble were carried out to determine the mutual solubilities for water/n-alkane mixtures over a wide range of temperatures, pressures, and alkane chain lengths. Combinations of the popular, nonpolarizable SPC/E, TIP4P, and TIP4P/2005 water models with the TraPPE united atom model for alkanes are explored to represent these mixtures. Significant deviations from the experimental data are observed for vapor-liquid and liquid-liquid equilibria where the errors in the predicted mole fraction often exceed a factor of 2. Utilizing a scoring metric based on the logarithmic deviation in mole fraction from experimental data, we find that the TIP4P water model outperforms the SPC/E and TIP4P/2005 models in predicting the fluid phase equilibria for water/alkane mixtures. Three models with adjusted Lennard-Jones parameters for water-alkane cross-interactions reflecting departures from the Lorentz-Berthelot combining rules are also investigated. Although a large increase in the well depth can yield a negative Gibbs free energy of transfer for water from the vapor to alkane-rich liquid phases, the overall performance appears to worsen compared to the models using the standard combining rules. Using the standard Lorentz-Berthelot combining rules, the models yield interfacial tensions that deviate by about 10% from the experimental data, but a large increase in the water-alkane cross-interactions leads to a significant underprediction of the interfacial tension.

Original languageEnglish (US)
Pages (from-to)4256-4268
Number of pages13
JournalJournal of Chemical and Engineering Data
Volume63
Issue number11
DOIs
StatePublished - Nov 8 2018

Bibliographical note

Funding Information:
Financial support from the Abu Dhabi Petroleum Institute Research Center (Project Code LTR14009) and from the National Science Foundation (CHE-1152998) is gratefully acknowledged. Notes The authors declare no competing financial interest.

Publisher Copyright:
© 2018 American Chemical Society.

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