2007
DOI: 10.1016/j.jct.2007.02.008
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Mixing properties of binary mixtures presenting azeotropes at several temperatures

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Cited by 31 publications
(21 citation statements)
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“…The viscosity of bmimPF 6 was measured by the use of a Brookfield Viscometer Model DV-II+ (Stoughton, MA, USA) with cone spindle. The results were g (cP) = 228, 164, and 124 at 25, 30, and 35°C, respectively, which are in a range reported in literature, 207-250 cP (25°C), 153-184 cP (30°C), and 116-141 cP (35°C) [33][34][35][36]. As for the refractive index, we used n = 1.41 which is an average of reported values ranging from 1.407 to 1.410 [35,37,38].…”
Section: Methodssupporting
confidence: 76%
“…The viscosity of bmimPF 6 was measured by the use of a Brookfield Viscometer Model DV-II+ (Stoughton, MA, USA) with cone spindle. The results were g (cP) = 228, 164, and 124 at 25, 30, and 35°C, respectively, which are in a range reported in literature, 207-250 cP (25°C), 153-184 cP (30°C), and 116-141 cP (35°C) [33][34][35][36]. As for the refractive index, we used n = 1.41 which is an average of reported values ranging from 1.407 to 1.410 [35,37,38].…”
Section: Methodssupporting
confidence: 76%
“…Excess and derived properties have been calculated from the experimental data. A function of the mole fraction and temperature polynomial equation [20] was used to fit these quantities. The standard deviations between experimental and calculated values are shown.…”
Section: Introductionmentioning
confidence: 99%
“…The RMSD values are lower than 0.020 for the ternary systems hydrocarbon (1) + ethanol (2) + PIL (3). A comparison between the experimental data and those obtained from the NRTL equation is illustrated in Fig.…”
Section: Correlation Using Nrtl Modelmentioning
confidence: 94%
“…In many areas of industry, the increasing interest related to development of green processes and products makes ionic liquids (ILs) candidates to replace conventional organic solvents in many chemical processes [1]. The possibility of recovering compounds used in industrial processes is not easy, because in many cases the mixtures can form azeotropes [2]. The separation of these azeotropic mixtures into the neat components is needed so that they can be reused, minimizing the costs of industrial processes.…”
Section: Introductionmentioning
confidence: 99%