A new model for the n-alkane homologous series has been developed, param-eterized to the vapor-liquid coexistence properties for a range of chain lengths. The model utilizes the Buckingham exponential-6 potential to describe the non-bonded interaction energy. Histogram reweighting grand canonical Monte Carlo methods were used to determine the model parameters. The new model repro-duces the experimental saturated liquid and vapor densities and vapor pressure for ethane through octane to within average errors of 0.5%, 2.1 % and 2.2 % re-spectively. Critical temperatures and densities were also found to be in good agreement with experiment. Critical pressures are slightly overestimated for longer chain lengths. Comparisons were made to the Tra...
ACLInternational audienceIn this work, using molecular dynamics simulations, we have investigated ho...
Mixtures of molecular fluids are encountered often in chemical industry, and the vapor-liquid coexis...
A model for the temperature dependence of the isobaric heat capacity of associated pure liquids C-p,...
A new set of united-atom Lennard-Jones interaction parameters for n-alkanes is proposed from fitting...
Grand-canonical transition-matrix Monte Carlo is combined with configurational-bias and expanded ens...
A transferable united-atom (UA) force field based on Mie potentials is presented for branched alkane...
A transferable united-atom (UA) force field based on Mie potentials is presented for branched alkane...
A transferable united-atom (UA) force field based on Mie potentials is presented for branched alkane...
The NpT - Gibbs ensemble Monte Carlo computer simulation method was applied to predict the vapour-li...
The interest in phase equilibrium and thermophysical properties of mixtures containing long chain hy...
Based on Flory’s ideas about functional groups, a statistical model for liquids has been developed. ...
Development of intermolecular potentials between molecules of methane, ethane, hydrogen sulfide, and...
lations for the thermodynamic and structural properties of liquid n- alkanes, from n- butane to n- h...
The Transferable Potentials for Phase Equilibria-United Atom (TraPPE-UA) force field for hydrocarbon...
An extension of the transferable potentials for phase equilibria united-atom (TraPPE-UA) force field...
ACLInternational audienceIn this work, using molecular dynamics simulations, we have investigated ho...
Mixtures of molecular fluids are encountered often in chemical industry, and the vapor-liquid coexis...
A model for the temperature dependence of the isobaric heat capacity of associated pure liquids C-p,...
A new set of united-atom Lennard-Jones interaction parameters for n-alkanes is proposed from fitting...
Grand-canonical transition-matrix Monte Carlo is combined with configurational-bias and expanded ens...
A transferable united-atom (UA) force field based on Mie potentials is presented for branched alkane...
A transferable united-atom (UA) force field based on Mie potentials is presented for branched alkane...
A transferable united-atom (UA) force field based on Mie potentials is presented for branched alkane...
The NpT - Gibbs ensemble Monte Carlo computer simulation method was applied to predict the vapour-li...
The interest in phase equilibrium and thermophysical properties of mixtures containing long chain hy...
Based on Flory’s ideas about functional groups, a statistical model for liquids has been developed. ...
Development of intermolecular potentials between molecules of methane, ethane, hydrogen sulfide, and...
lations for the thermodynamic and structural properties of liquid n- alkanes, from n- butane to n- h...
The Transferable Potentials for Phase Equilibria-United Atom (TraPPE-UA) force field for hydrocarbon...
An extension of the transferable potentials for phase equilibria united-atom (TraPPE-UA) force field...
ACLInternational audienceIn this work, using molecular dynamics simulations, we have investigated ho...
Mixtures of molecular fluids are encountered often in chemical industry, and the vapor-liquid coexis...
A model for the temperature dependence of the isobaric heat capacity of associated pure liquids C-p,...