Modeling of CO2 vapor-liquid equilibrium in Colombian heavy oil using SARA analysis

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 obt...

Full description

Autores:
Ramirez, Oscar
Betancur Gómez, Carolina
Hoyos, Bibian
Naranjo, Carlos
Tipo de recurso:
Article of journal
Fecha de publicación:
2015
Institución:
Universidad Nacional de Colombia
Repositorio:
Universidad Nacional de Colombia
Idioma:
spa
OAI Identifier:
oai:repositorio.unal.edu.co:unal/60698
Acceso en línea:
https://repositorio.unal.edu.co/handle/unal/60698
http://bdigital.unal.edu.co/59030/
Palabra clave:
62 Ingeniería y operaciones afines / Engineering
Equation of state
pseudo-component
SARA analysis
crude
solvent
phase equilibrium.
Rights
openAccess
License
Atribución-NoComercial 4.0 Internacional
Description
Summary: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.