2015
DOI: 10.1080/07366299.2015.1132060
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Separation of Hydrocarbons by Means of Liquid-Liquid Extraction with Deep Eutectic Solvents

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Cited by 27 publications
(21 citation statements)
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“…For describing liquid-liquid phase equilibria in quasi-three-component systems containing DES, NRTL model 16,17 and COSMO-RS model 16 have been used so far; thereby NRTL gave significantly better results.…”
Section: Thermodynamic Modelling In Quasi-three-component Systemsmentioning
confidence: 99%
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“…For describing liquid-liquid phase equilibria in quasi-three-component systems containing DES, NRTL model 16,17 and COSMO-RS model 16 have been used so far; thereby NRTL gave significantly better results.…”
Section: Thermodynamic Modelling In Quasi-three-component Systemsmentioning
confidence: 99%
“…the mass fraction of aliphatic hydrocarbons in the extract stage was set at w i E = 1 × 10 −6 . The mass fraction of the raffinate phase, Ψ R , was calculated according to: (17) where i denotes the component, and the superscripts F, E, R denote the total mixture, the extract phase and the refractive phase, respectively. For each hydrocarbon, a distinct value of Ψ R was obtained; the appropriate value for the whole system was calculated as the average of the three specific individual values.…”
Section: Extraction Experiments In Quasi-seven-component Systemsmentioning
confidence: 99%
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“…Real hydrocarbon fuels originating both from nonrenewable and renewable sources are complex mixtures and it is therefore often simpler and easier to observe trends by studying model fuels. Thus desulfurization (Li et al, 2013;Li et al, 2016;Gano et al, 2015), denitrification (Ali et al, 2016;Hizaddin et al, 2016) and dearomatization processes (Sander et al, 2016) were investigated using DESs and model fuels. An even simpler approach is possible by the experimental study of ternary liquid-liquid equilibria (LLE) in the systems based on DES as a quasi-component.…”
Section: Introductionmentioning
confidence: 99%