ABSTRACT

In this work, 1-ethyl 3-methylimidazolium methylsulfonate [EMIM][MeSO3], 1-ethyl 3-methylimidazolium ethylsulfate [EMIM][EthSO4] and 1-ethyl-3-methylimidazolium acetate [EMIM][Ac] were investigated as green solvents for the denitrification of diesel oil at T = 298.15 K and atmospheric pressure. The liquid-liquid equilibrium (LLE) data for the ternary mixture of [EMIM][MeSO3] (1) + pyridine (2) + n-pentane/isooctane (3), [EMIM][EthSO4] (1) + pyridine (2) + n-pentane/isooctane (3) and [EMIM][Ac] (1) + pyridine (2) + n-pentane/isooctane (3) systems were experimentally determined at ambient conditions. In all the systems, the tie lines had a negative slope at higher concentrations of pyridine, implying higher quantity of ionic liquid is required for the separation of pyridine from hydrocarbon. It was found that at lower concentrations of pyridine in feed, [EMIM][Ac] and [EMIM][MeSO3] are the potential solvents for the extraction of pyridine from n-pentane and isooctane respectively. The experimental results were well correlated with predicted values via NRTL and UNIQUAC models. The average RMSD obtained in NRTL and UNIQUAC models for all the six systems were 1.15% and 1.9% respectively.

Compounds

#	Formula	Name
1	C7H14N2O3S	1-ethyl-3-methylimidazolium methanesulfonate
2	C8H16N2O4S	1-ethyl-3-methylimidazolium ethyl sulfate
3	C8H14N2O2	1-ethyl-3-methylimidazolium acetate
4	C5H12	pentane
5	C8H18	2-methylheptane
6	C5H5N	pyridine

Datasets

The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type	Compound-#	Property	Variable	Constraint	Phase	Method	#Points
POMD	4 6 1	Mole fraction - 4 ; Liquid mixture 1 Mole fraction - 4 ; Liquid mixture 2 Mole fraction - 6 ; Liquid mixture 2	Mole fraction - 6; Liquid mixture 1	Temperature, K; Liquid mixture 2 Pressure, kPa; Liquid mixture 2	Liquid mixture 1 Liquid mixture 2	NMR spectrometry NMR spectrometry NMR spectrometry	8
POMD	6 5 1	Mole fraction - 5 ; Liquid mixture 1 Mole fraction - 5 ; Liquid mixture 2 Mole fraction - 6 ; Liquid mixture 2	Mole fraction - 6; Liquid mixture 1	Temperature, K; Liquid mixture 2 Pressure, kPa; Liquid mixture 2	Liquid mixture 1 Liquid mixture 2	NMR spectrometry NMR spectrometry NMR spectrometry	8
POMD	4 6 2	Mole fraction - 4 ; Liquid mixture 2 Mole fraction - 4 ; Liquid mixture 1 Mole fraction - 6 ; Liquid mixture 1	Mole fraction - 6; Liquid mixture 2	Temperature, K; Liquid mixture 2 Pressure, kPa; Liquid mixture 2	Liquid mixture 2 Liquid mixture 1	NMR spectrometry NMR spectrometry NMR spectrometry	8
POMD	6 5 2	Mole fraction - 5 ; Liquid mixture 1 Mole fraction - 5 ; Liquid mixture 2 Mole fraction - 6 ; Liquid mixture 2	Mole fraction - 6; Liquid mixture 1	Temperature, K; Liquid mixture 2 Pressure, kPa; Liquid mixture 2	Liquid mixture 1 Liquid mixture 2	NMR spectrometry NMR spectrometry NMR spectrometry	8
POMD	4 6 3	Mole fraction - 4 ; Liquid mixture 1 Mole fraction - 4 ; Liquid mixture 2 Mole fraction - 6 ; Liquid mixture 2	Mole fraction - 6; Liquid mixture 1	Temperature, K; Liquid mixture 2 Pressure, kPa; Liquid mixture 2	Liquid mixture 1 Liquid mixture 2	NMR spectrometry NMR spectrometry NMR spectrometry	8
POMD	6 5 3	Mole fraction - 5 ; Liquid mixture 1 Mole fraction - 5 ; Liquid mixture 2 Mole fraction - 6 ; Liquid mixture 2	Mole fraction - 6; Liquid mixture 1	Temperature, K; Liquid mixture 2 Pressure, kPa; Liquid mixture 2	Liquid mixture 1 Liquid mixture 2	OTHER OTHER OTHER	8

Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Liquid liquid equilibria of imidazolium based ionic liquid + pyridine + hydrocarbon at 298.15 K: Experiments and correlations

Ravilla, U. K.[Uday Kiran], Banerjee, T.[Tamal]

ABSTRACT