2012
DOI: 10.1016/j.fluid.2011.11.008
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Extraction of propylbenzene from its mixtures with heptadecane using 4-methyl-N-butylpyridinium tetrafluoroborate

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Cited by 27 publications
(19 citation statements)
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“…The variation of S with the mass concentration of isopropanol in the raffinate phase is plotted in Figure . It should be noted that the S values decrease with the increase in isopropanol concentration in the raffinate phase, which is attributed to the two-phase region shrinking as the isopropanol content increased, implying that the extraction ability of the investigated extractants diminished. , Additionally, the ternary system with 1,4-BDO as the extractant had a higher S value than the other three systems, revealing that 1,4-BDO is most suitable for the separation of isopropanol from cyclohexane.…”
Section: Resultsmentioning
confidence: 94%
See 1 more Smart Citation
“…The variation of S with the mass concentration of isopropanol in the raffinate phase is plotted in Figure . It should be noted that the S values decrease with the increase in isopropanol concentration in the raffinate phase, which is attributed to the two-phase region shrinking as the isopropanol content increased, implying that the extraction ability of the investigated extractants diminished. , Additionally, the ternary system with 1,4-BDO as the extractant had a higher S value than the other three systems, revealing that 1,4-BDO is most suitable for the separation of isopropanol from cyclohexane.…”
Section: Resultsmentioning
confidence: 94%
“…It should be noted that the S values decrease with the increase in isopropanol concentration in the raffinate phase, which is attributed to the two-phase region shrinking as the isopropanol content increased, implying that the extraction ability of the investigated extractants diminished. 26,27 Additionally, the ternary system with 1,4-BDO as Standard uncertainties u are u(T) = 0.1 K, u(w 1 ) = 0.0017, u(w 2 ) = 0.0010, and u(w 3 ) = 0.0016. Standard uncertainties u are u(T) = 0.1 K, u(w 1 ) = 0.0024, u(w 2 ) = 0.0005, and u(w 3 ) = 0.0024. the extractant had a higher S value than the other three systems, revealing that 1,4-BDO is most suitable for the separation of isopropanol from cyclohexane.…”
mentioning
confidence: 99%
“…Currently, there are few data published for {[bmim][PF 6 ] + aromatic + n-alkane (C 5 -C 9 )} and hardly any for systems containing carbon number greater than 9 for the aliphatic and/or aromatic compounds [10,11]. This paper is a continuation of our study on liquid-liquid phase equlibria for de-aromatization of Kuwait middle distilled fraction [12][13][14]. Our interest in IL is to provide experimental new LLE data, and to examine the effect of n-alkane chain length, temperature and solvent to feed ratio upon solubility, the per cent removal of aromatic, the distribution ratio (K), and the selectivity (S) for two systems, viz.…”
Section: Introductionmentioning
confidence: 92%
“…Ionic liquids and paraffins have very low mutual solubility, and most ionic liquids are insoluble in paraffin-rich phases with paraffins > C 10 , producing a ready raffinate product without wasting any solvent. The solubility of paraffin in the ionic-rich phase is also very low, reducing the cost of solvent regeneration by simple flash distillation or stripping . Ionic liquids are nonvolatile, which makes them environmentally attractive alternatives to conventional solvents that contaminate the atmosphere. They also can be produced in a variety of anion–cation combinations, which allows optimization of the separation process. …”
Section: Introductionmentioning
confidence: 99%