Molecular Simulation Study of Vapor-Liquid Equilibrium of Morse Fluids

Author(s):  
Sang Kyu Kwak ◽  
Jayant K Singh ◽  
Jhumpa Adhikari

The Morse potential energy function (PEF) is considered regarding the characterization of interaction forces of particles with tuning parameters. Phase coexistence of Morse fluids is predicted for different steepness and range of the PEF parameters using the grand-canonical transition matrix Monte Carlo (GC-TMMC) method, with quantification of the parameter S, which is the product of a constant with a unit of reciprocal length and the equilibrium distance between two molecules. We found that a lower limit of S exists bounded by infinite critical temperature. The critical properties of the vapor-liquid equilibrium curves are estimated using a rectilinear diameter method and a scaling law approach. A Clausius-Clayperon type relation of S and critical temperature is derived in this work. Vapor-liquid surface tension of Morse fluids by finite size scaling and GC-TMMC is also reported. Surface tensions are found to be higher at lower S.

RSC Advances ◽  
2019 ◽  
Vol 9 (61) ◽  
pp. 35803-35812 ◽  
Author(s):  
José L. Rivera ◽  
Jack F. Douglas

The variance in the surface tension of systems under vapor/liquid equilibrium is strongly affected by the size of the interfacial area. Wider layers increase the variance, but these increments disappear as the interfacial area grows.


DYNA ◽  
2015 ◽  
Vol 82 (191) ◽  
pp. 103-108
Author(s):  
Oscar Ramirez ◽  
Carolina Betancur Gómez ◽  
Bibian Hoyos ◽  
Carlos Naranjo

The solubility of CO2 in Colombian heavy oil was calculated using the Peng-Robinson cubic equation of state and the Lee-Kesler correlations. The crude was represented as a mixture of pseudo-components and for each one of them, the thermodynamic and critical properties were estimated. The results obtained in representing the oil with four, five and six pseudo-components show that all these representations produce similar results and therefore the use of four pseudo-components is sufficient and has a lower computational cost. Excellent results were obtained by comparing the experimental and calculated data. For this system, it is enough to have a complete characterization of the SARA analysis and to use four pseudo-components to adequately model the vapor-liquid equilibrium of CO2 -heavy oil.


1984 ◽  
Vol 15 (21) ◽  
Author(s):  
R. G. RUBIO ◽  
J. ARACIL ◽  
M. DIAZ PENA ◽  
J. A. R. RENUNCIO

Author(s):  
César A. García ◽  
Jessica J. Velandia ◽  
Mario A. Céspedes ◽  
Gerardo Rodríguez ◽  
Iván D. Gil

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