Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
7006882 | Chemical Engineering Research and Design | 2016 | 41 Pages |
Abstract
In this work, we have studied the potential use of the 1-allyl-3-methylimidazolium dicyanamide ([amim][DCA]) and the 1-benzyl-3-methylimidazolium dicyanamide ([bzmim][DCA]) ionic liquids (ILs) in the liquid-liquid extraction of aromatic hydrocarbons. To design an industrial process of extraction of aromatic hydrocarbons from alkanes, it is essential to measure the liquid-liquid and vapor-liquid equilibria between solutes and solvent, and to perform also a thermophysical characterization of the solvent. Because of this, we have studied the liquid-liquid extraction of toluene from n-heptane at 313.2Â K and the vapor-liquid separation of n-heptane from toluene in the presence of [amim][DCA] and [bzmim][DCA] at 323.2Â K, 343.2Â K, and 363.2Â K. Densities and viscosities as a function of temperature and the thermal stability of both ILs were also determined. The [amim][DCA] showed suitable extractive and physical properties to replace sulfolane and an adequate maximum operation temperature (MOT) to be employed at industrial scale. The ([bzmim][DCA]) showed good extractive properties but high viscosities. To complete the study, the Conductor-like Screening Model for Real Solvents (COSMO-RS) methodology was employed to predict the liquid-liquid and vapor-liquid equilibria between the hydrocarbons and ILs and the physical properties of ILs. A comparative evaluation between experimental results and COSMO-RS calculated values was performed.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Filtration and Separation
Authors
Marcos Larriba, Pablo Navarro, Maria Gonzalez-Miquel, Salama Omar, José Palomar, Julián GarcÃa, Francisco RodrÃguez,