Abstract

The paper is the first of a series of two articles on molecular models for alkanes with air components and combustion products. This article reports simulations of the vapor-liquid equilibrium phase diagram for mixtures of linear hydrocarbons with nitrogen, carbon dioxide and water. We consider four alkanes: methane, propane, octane and dodecane as characteristic components of natural gas, liquefied natural gas, gasoline and kerosene. Combustion products are presented with common computationally inexpensive molecular models: three-center models for N2 and CO2, TIP4P-2005 model for water, and united-atom forcefield for alkanes. The parameters for nitrogen, CO2 and water oxygen interactions with CH2 and CH3 groups are calculated with Lorentz-Berthelot mixing rules with an adjustable coefficient for the energy parameter ε, a single temperature-independent coefficient for each non-alkane component. We obtained very reasonable agreement with the experimental data for most alkane-nitrogen and alkane-carbon dioxide binary mixtures and discuss in detail the capability of the models with unified adjustable parameters. For dodecane-water system, reasonable agreement between calculated solubility of water in dodecane and experimental data was obtained; the model however is unable to represent the near-critical and high pressure phase boundaries.

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.