Data for: Dearomatization of pyrolysis gasoline by extractive distillation with 1-ethyl-3-methylimidazolium tricyanomethanide

Supplementary material of the manuscript "Dearomatization of pyrolysis gasoline by extractive distillation with 1-ethyl-3-methylimidazolium tricyanomethanide"
Tables
Table S1 Experimental VLLE or VLE dataa for pyrolysis gasoline model dearomatization using [emim][TCM] with S/F = 5
Table S2 Experimental VLLE or VLE dataa for pyrolysis gasoline model dearomatization using [emim][TCM] with S/F = 10
Table S3 FUGK simulations of the EDC to separate BTX from pyrolysis gasoline by extractive distillation
Table S4 Experimental VLE dataa for the BTX/[emim][TCM] separation in the residue stream
Table S5. Residue and distillate temperature and composition by FUGK and COSMO-based/Aspen Plus methodologies at 101.3 kPa
Table S6. Aromatic purities (Puarom) and recoveries (Rarom) by Navarro et al. algorithm and COSMO-based/Aspen Plus methodologies at 452 K and 5 kPa
Table S7. Benzene, toluene and p-xylene solubilities in [emim][TCM] at 363.2 K
Table S8. Battery limits for extractive distillation and liquid-liquid extraction processes for S/F = 5 and 15 equilibrium stages for comparison purposes
Table S9. Costs for the utilities used from Aspen Economics
Figures
Figure S1. Extractive distillation process scheme evaluated in the operating cost calculation.
Figure S2. Liquid-liquid extraction process scheme evaluated in the operating cost calculation.