2007
DOI: 10.1016/j.fluid.2007.06.025
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Separation of aromatic hydrocarbons from alkanes using ammonium ionic liquid C2NTf2 at T=298.15K

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Cited by 192 publications
(165 citation statements)
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“…Rogers et al [96] reported the extraction of substituted benzene derivatives from water using the hydrophobic [Bmim]A C H T U N G T R E N N U N G [PF 6 ]. Continuous studies focus on the removal of sulfides [97,98] and nitrides [99,100] from diesel and gasoline, the separation of aromatics from aliphatics, [101] the removal of pollutants (e.g., phenols, dyes, organic acids) from water, and so on. However, the discussions on mechanism are very rare, and a general viewpoint is that ILs can recognize the products by hydrogen-bonding interactions.…”
Section: Roles Of Hydrogen Bonds In the Applications Of Ionic Liquidsmentioning
confidence: 99%
“…Rogers et al [96] reported the extraction of substituted benzene derivatives from water using the hydrophobic [Bmim]A C H T U N G T R E N N U N G [PF 6 ]. Continuous studies focus on the removal of sulfides [97,98] and nitrides [99,100] from diesel and gasoline, the separation of aromatics from aliphatics, [101] the removal of pollutants (e.g., phenols, dyes, organic acids) from water, and so on. However, the discussions on mechanism are very rare, and a general viewpoint is that ILs can recognize the products by hydrogen-bonding interactions.…”
Section: Roles Of Hydrogen Bonds In the Applications Of Ionic Liquidsmentioning
confidence: 99%
“…The application of these ILs in extraction processes has been extensively investigated and reviewed [1][2][3][4]. Moreover, ILs are increasingly being focused on as possible replacement solvents for volatile organic compounds in the development of sustainable green chemistry.…”
Section: Introductionmentioning
confidence: 99%
“…Unfortunately, it was impossible to detect visually the cloud point of the solvent rich phase for the investigated systems. The left-hand limits of the equilibrium curves in this system and many others [9,[11][12][13][14][15][16][17][18] are very close to zero mole fraction of the IL, that is x 1 = 10 −4 to 10 −5 . These data were calculated previously for some ILs by COSMO-RS [11] within x 1 = 10 −4 to 10 −5 in hexane, benzene and alkylbenzenes as x 1 = 10 −5 [34].…”
Section: Resultsmentioning
confidence: 59%
“…In particular, effective and profitable design of industrial liquid-liquid extraction or either extractive or azeotropic distillation of close-boiling mixtures (e.g. those containing both aromatic and aliphatic hydrocarbons [9]) requires a lot of input data concerning with thermodynamic properties (activity coefficients, excess volumes and enthalpies of mixing) as well as transport properties (densities, viscosities, diffusivities, speeds of sound of pure components and their mixtures). Those data are determined by means of experiments, or can be calculated (predicted), e.g.…”
Section: Introductionmentioning
confidence: 99%