Skip navigation elements to page contents
Ionic Liquids Database - (ILThermo)
Contact us
Contact us
Help
Help
Main Menu: Select to go to this tabPure: Select to go to this tabBinary: Select to go to this tabTernary: Currently selected tab
By Ions|By Compounds|By Property|By Literature
Property Data of Ternary Systems Containing Ionic Liquids
Search by Property

Presentation Logic

This page has a hierarchical structure: a new selection made in any displayed table results in an update of all content below the table. Upon selection of a specific physical property from the following table, the browser displays the list of ternary systems for which the selected property is available. Selection of a specific ternary system shows the list of available datasets. Finally, selection of a specific dataset presents a detailed data summary at the bottom of the page.

 

Available Properties for Ternary Systems Containing Ionic Liquids:
Previous functionality disabledPrevious1-33 of 33NextNext functionality disabled
SelectProperty CategoryDescription
Activity, Fugacity, and Osmotic PropertiesActivity Coefficient of Component 1 at Infinite Dilution, Dimensionless
Composition at Phase EquilibriumDistribution Ratio of Component 1 in Component 3/Component 2, Dimensionless
Composition at Phase EquilibriumDistribution Ratio of Component 3 in Component 1/Component 2, Dimensionless
Composition at Phase EquilibriumDistribution Ratio of Component 2 in Liquid/Gas, Dimensionless
Composition at Phase EquilibriumLiquid-Liquid Equilibrium Composition: MolaRity of Component 1, mol/dm**3
Composition at Phase EquilibriumLiquid-Liquid Equilibrium Composition: Weight Fraction of Component 1, Dimensionless
Composition at Phase EquilibriumLiquid-Liquid Equilibrium Composition: Weight Fraction of Component 2, Dimensionless
Composition at Phase EquilibriumLiquid-Liquid Equilibrium Composition: Weight Fraction of Component 3, Dimensionless
Composition at Phase EquilibriumLiquid-Liquid Equilibrium Composition: Mole Fraction of Component 1, Dimensionless
Composition at Phase EquilibriumLiquid-Liquid Equilibrium Composition: Mole Fraction of Component 2, Dimensionless
Composition at Phase EquilibriumLiquid-Liquid Equilibrium Composition: Mole Fraction of Component 3, Dimensionless
Composition at Phase EquilibriumTie-Line Data: Mass Fraction of Component 3
Composition at Phase EquilibriumTie-Line Data: Mole Fraction of Component 2
Composition at Phase EquilibriumTie-Line Data: Mole Fraction of Component 3
Composition at Phase EquilibriumVapor-Liquid Equilibrium Composition: Mass Per Volume of Solution: Component 1, kg/m**3
Composition at Phase EquilibriumVapor-Liquid-Liquid Equilibrium Composition: Mole Fraction of Component 1, Dimensionless
Composition at Phase EquilibriumVapor-Liquid-Liquid Equilibrium Composition: Mole Fraction of Component 3, Dimensionless
Composition at Phase EquilibriumVapor-Liquid Equilibrium Composition: Mole Fraction of Component 1, Dimensionless
Composition at Phase EquilibriumVapor-Liquid Equilibrium Composition: Mole Fraction of Component 2, Dimensionless
Composition at Phase EquilibriumVapor-Liquid Equilibrium Composition: Mole Fraction of Component 3, Dimensionless
Critical PropertiesCritical Pressure, kPa
Electrical ConductivityElectrical Conductivity, S/m
Excess Partial, and Apparent Energetic PropertiesEnthalpy of Solution of Component 3 in mixture of Component 1 and Component 2, kJ/mol
Phase Transition PropertiesLiquid-Liquid Equilibrium Temperature, K
Phase Transition PropertiesSolid-Liquid Equilibrium Temperature, K
Refraction, Surface Tension, and Speed of SoundRefractive index (Na D-line), Dimensionless
Refraction, Surface Tension, and Speed of SoundSpeed of Sound, m/s
Transport PropertiesTracer Diffusion Coefficient of Component 2, m**2/s/10**9
Transport PropertiesViscosity, Pa s
Vapor Pressure, Boiling Temperature, and Azeotropic T & PPhase Boundary Pressure, kPa
Vapor Pressure, Boiling Temperature, and Azeotropic T & PBoiling Temperature at Pressure P, K
Volumetric PropertiesSpecific Density, kg/m**3
Volumetric PropertiesMolar Volume, m**3/mol
Previous functionality disabledPrevious1-33 of 33NextNext functionality disabled

 

 

Ternary Systems for: Activity Coefficient of Component 1 at Infinite Dilution, Dimensionless
Previous functionality disabledPrevious1-7 of 7NextNext functionality disabled
SelectCompound_1Compound_2Compound_3ReferencesData Points
2-pentanone1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide14
1-pentene1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide14
hexane1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide14
octane1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide14
heptane1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide14
butanone1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide14
water1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide14

 

 

References and Data Sets
Previous functionality disabledPrevious1-1 of 1NextNext functionality disabled
SelectReference TitleSample No._1Sample No._2Sample No._3Data SetYear Pub.Authors
Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)11112005Kato, R.; Gmehling, J.

 

Data Summary
Property: Activity Coefficient of 2-pentanone at Infinite Dilution, Dimensionless
Compound 1:
Name - 2-pentanone
Formula - C5H10O
Component 2:
Name - 1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide
Formula - C8H11F6N3O4S2
Component 3:
Name - 1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide
Formula - C10H15F6N3O4S2
Sample No 1 of Compound 1
Source: Commercial source
Initial Purity: Not stated
Purification: Fractional distillation
Final Purity: 99 (Not specified) %
Purity Analysis: Estimation by compiler
Sample No 1 of Compound 2
Source: Commercial source
Initial Purity: Not stated
Purification: Dried by heating in a vacuum
Final Purity: Not stated
Purity Analysis: Not stated
Sample No 1 of Compound 3
Source: Commercial source
Initial Purity: Not stated
Purification: Dried by heating in a vacuum
Final Purity: Not stated
Purity Analysis: Not stated
Measurement Method: Chromatography

 

Selected Data Set No. 1 (Property/Uncertainty - Activity Coefficient of 2-pentanone at Infinite Dilution, Dimensionless)
Under System Condition(s): (1) Binary solvent: mole fraction of 1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide: .5; (2) Gas Phase Present
Note(s):
  • Solvent is defined as mixture of 1-ethyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide and 1-butyl-3-methylimidazolium bis[(trifluoromethyl)sulfonyl]imide
Previous functionality disabledPrevious1-4 of 4NextNext functionality disabled
Temperature, K
Activity Coefficient of 2-pentanone at Infinite Dilution, Dimensionless
Liquid 		Uncertainty Assigned by ILThermo
About Assigned Uncertainty
303.15 0.706 0.029
313.15 0.738 0.029
323.15 0.759 0.029
333.15 0.781 0.028

 

Selected Reference
Year Pub.AuthorsSource
2005Kato, R.; Gmehling, J. J. Chem. Thermodyn. 37 , 603-619
Title:


Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
Keywords:


ionic liquids; activity coefficients at infinite dilution; vapor-liquid equilibria
Abstract:


Not available due to copyright restrictions.
Main Menu  |  Pure  |  Binary  |  Ternary  |  Contact us  |  Help
© 2006 copyright by the US Secretary of Commerce on behalf of the United States of America.
All rights reserved.