Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Low transition temperature mixtures (LTTMs) as novel entrainers in extractive distillation

Rodriguez, N. R.[Nerea R.], Gonzalez, A. S.[Agustin SB], Tijssen, P. M. A.[Patricia M. A.], Kroon, M. C.[Maaike C.]
Fluid Phase Equilib. 2015, 385, 72-78
ABSTRACT
Low transition temperature mixtures (LTTMs) are evaluated as potential entrainers for extractive distillation for the first time. The selected LTTMs were lactic acid choline chloride 2:1 (LC 2:1), malic acid choline chloride 1:1 (MC 1:1), glycolic acid choline chloride 3:1 (GC 3:1) and glycolic acid choline chloride 1:1 (GC 1:1). Vapour liquid equilibrium (VLE) data for the pseudo-binary mixtures of water LTTM and ethanol LTTM were measured and fitted with the NRLT model to calculate the interaction parameters. These parameters were used to predict the pseudo-ternary VLE data using the same model. The prediction was compared with new experimental data for the water ethanol LTTM system and the prediction was found to be adequate. It was found that the ethanol water azeotrope can be broken by MC 1:1, GC 1:1 and GC 3:1 and it can be moved to the pure ethanol side with LC 2:1.
Compounds
# Formula Name
1 C2H6O ethanol
2 C2H4O3 2-hydroxyethanoic acid
3 C4H6O5 hydroxybutanedioic acid
4 C5H14ClNO choline chloride
5 C3H6O3 (S)-2-hydroxypropanoic acid
6 H2O water
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
  • 4
  • 5
  • 6
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 6; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 24
  • POMD
  • 1
  • 4
  • 5
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 23
  • POMD
  • 4
  • 3
  • 6
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 6; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 26
  • POMD
  • 1
  • 4
  • 3
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 23
  • POMD
  • 4
  • 2
  • 6
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 6; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 46
  • POMD
  • 1
  • 4
  • 2
  • Boiling temperature at pressure P, K ; Liquid
  • Mole fraction - 1; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Ebulliometric method (Recirculating still)
  • 49
  • POMD
  • 4
  • 2
  • Mass density, kg/m3 ; Liquid
  • Mole fraction - 4; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Vibrating tube method
  • 2
  • POMD
  • 4
  • 2
  • Viscosity, Pa*s ; Liquid
  • Mole fraction - 4; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Concentric cylinders viscometry
  • 2