Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane

Trejo, A.[Arturo], Yanez, P.[Patricia], Eustaquio-Rincon, R.[Rafael]
J. Chem. Eng. Data 2006, 51, 3, 1070-1075
ABSTRACT
Experimental liquid-liquid miscibility temperatures as a function of mole fraction are reported for binary systems formed by methanol as common component with hexane, 2-methylpentane, 3-methylpentane, 2,2-dimethylbutane, 2,3-dimethylbutane, and cyclohexane. All the studied coexistence curves present an upper critical solution temperature (UCST). The UCST of the binary systems presents a clear dependence with the molecular shape of the hydrocarbons (e.g., the solubility of the alkanes in methanol increases as branching increases in the structural isomers); hence, 2,2-dimethylbutane shows the lowest UCST with methanol. Cyclohexane presents the highest UCST with methanol (i.e., it shows the lowest mutual miscibility for the six studied systems). Values of the UCST have been calculated with the Weimer-Prausnitz modification for polar components of Hildebrand s Regular Solutions Theory. The predicted UCSTs compare well with those obtained experimentally.
Compounds
# Formula Name
1 CH4O methanol
2 C6H14 hexane
3 C6H14 2-methylpentane
4 C6H14 2,2-dimethylbutane
5 C6H14 2,3-dimethylbutane
6 C6H12 cyclohexane
7 C6H14 3-methylpentane
Datasets
The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type Compound-# Property Variable Constraint Phase Method #Points
  • POMD
  • 1
  • 2
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:12
  • 14
  • POMD
  • 1
  • 3
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:12
  • 11
  • POMD
  • 1
  • 4
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:12
  • 12
  • POMD
  • 1
  • 5
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:12
  • 12
  • POMD
  • 1
  • 6
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:8
  • 11
  • POMD
  • 1
  • 7
  • Liquid-liquid equilibrium temperature, K ; Liquid mixture 1
  • Mole fraction - 1; Liquid mixture 1
  • Pressure, kPa; Liquid mixture 1
  • Liquid mixture 1
  • Liquid mixture 2
  • VISOBS:UFactor:12
  • 11