Toluene

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M Bochmann - One of the best experts on this subject based on the ideXlab platform.

Jerry L Atwood - One of the best experts on this subject based on the ideXlab platform.

  • liquid liquid equilibria for Toluene heptane 1 ethyl 3 methylimidazolium triiodide and Toluene heptane 1 butyl 3 methylimidazolium triiodide
    Journal of Chemical & Engineering Data, 2000
    Co-Authors: Murugan S Selvan, Marvin D Mckinley, And Raymond H Dubois, Jerry L Atwood
    Abstract:

    This study focuses on the use of an ionic liquid for extracting an aromatic hydrocarbon from a mixture of an aromatic and an aliphatic hydrocarbon. Liquid−liquid equilibrium data were collected for the Toluene + heptane + 1-ethyl-3-methylimidazolium triiodide system at 45 °C and for the Toluene + heptane + 1-butyl-3-methylimidazolium triiodide system at 35 °C. The nonrandom two-liquid (NRTL) physical thermodynamic model was used to correlate the experimental data. The NRTL model was found to represent the data very well. The selectivity and capacity of the ionic liquids for extracting Toluene from Toluene + heptane solutions were evaluated. The separation factors were found to be above 50 for low Toluene compositions and nearly unity for high Toluene compositions.

Murugan S Selvan - One of the best experts on this subject based on the ideXlab platform.

  • liquid liquid equilibria for Toluene heptane 1 ethyl 3 methylimidazolium triiodide and Toluene heptane 1 butyl 3 methylimidazolium triiodide
    Journal of Chemical & Engineering Data, 2000
    Co-Authors: Murugan S Selvan, Marvin D Mckinley, And Raymond H Dubois, Jerry L Atwood
    Abstract:

    This study focuses on the use of an ionic liquid for extracting an aromatic hydrocarbon from a mixture of an aromatic and an aliphatic hydrocarbon. Liquid−liquid equilibrium data were collected for the Toluene + heptane + 1-ethyl-3-methylimidazolium triiodide system at 45 °C and for the Toluene + heptane + 1-butyl-3-methylimidazolium triiodide system at 35 °C. The nonrandom two-liquid (NRTL) physical thermodynamic model was used to correlate the experimental data. The NRTL model was found to represent the data very well. The selectivity and capacity of the ionic liquids for extracting Toluene from Toluene + heptane solutions were evaluated. The separation factors were found to be above 50 for low Toluene compositions and nearly unity for high Toluene compositions.

Eun Ji Park - One of the best experts on this subject based on the ideXlab platform.

  • Adsorption and desorption of Toluene on nanoporous TiO_2/SiO_2 prepared by atomic layer deposition (ALD): influence of TiO_2 thin film thickness and humidity
    Adsorption, 2013
    Co-Authors: Eun Ji Park
    Abstract:

    Adsorption and desorption of Toluene on bare and TiO_2-coated silica with a mean pore size of 15 nm under dry and humid conditions were studied using Toluene breakthrough curves and temperature programmed desorption (TPD) of Toluene and CO_2. Two TiO_2/silica samples (either partially or fully covered with TiO_2) were prepared with 50 and 200 cycles of TiO_2 atomic layer deposition (ALD), respectively. The capacity of silica to adsorb Toluene improved significantly with TiO_2-thin film coating under dry conditions. However, Toluene desorption from the surface due to displacement by water was more pronounced for TiO_2-coated samples than bare samples under humid conditions. In TPD experiments, silica with a thinner TiO_2 film (50-ALD cycled) had the highest reactivity for Toluene oxidation to CO_2 both in the absence and presence of water. Toluene adsorption and oxidation reactivity of silica can be controlled by modifying the silica surface with small amount of TiO_2 using ALD.

And Raymond H Dubois - One of the best experts on this subject based on the ideXlab platform.

  • liquid liquid equilibria for Toluene heptane 1 ethyl 3 methylimidazolium triiodide and Toluene heptane 1 butyl 3 methylimidazolium triiodide
    Journal of Chemical & Engineering Data, 2000
    Co-Authors: Murugan S Selvan, Marvin D Mckinley, And Raymond H Dubois, Jerry L Atwood
    Abstract:

    This study focuses on the use of an ionic liquid for extracting an aromatic hydrocarbon from a mixture of an aromatic and an aliphatic hydrocarbon. Liquid−liquid equilibrium data were collected for the Toluene + heptane + 1-ethyl-3-methylimidazolium triiodide system at 45 °C and for the Toluene + heptane + 1-butyl-3-methylimidazolium triiodide system at 35 °C. The nonrandom two-liquid (NRTL) physical thermodynamic model was used to correlate the experimental data. The NRTL model was found to represent the data very well. The selectivity and capacity of the ionic liquids for extracting Toluene from Toluene + heptane solutions were evaluated. The separation factors were found to be above 50 for low Toluene compositions and nearly unity for high Toluene compositions.