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

Dilute Vapor Absorption: A New Accurate Technique for Measurement of the Limiting Activity Coefficient of Water in Hydrophobic Solvents of Lower Volatility

Haidl, J.[Jan], Dohnal, V.[Vladimir]
J. Chem. Eng. Data 2017, 62, 9, 2713-2720
ABSTRACT
An accurate experimental method for the determination of the limiting activity coefficient of water in hydrophobic solvents was described theoretically; the pertinent apparatus was built and its performance was duly verified. The method is based on continuously saturating the solvent by a gas stream of a constant and known humidity up to the attainment of the steady state and subsequent determination of the water content in the solvent by Karl Fischer titration. Using this new method, accurate values of the limiting activity coefficient of water were determined in eight selected solvents. The measurements were carried out at several temperatures and from these data the infinite dilution dissolution enthalpy and entropy of water in the solvents were evaluated. They both exhibit highly positive values reflecting the breakage of the hydrogen bonding network of water upon its dissolution in the solvents. Prediction of the water limiting activity coefficients was further attempted using the Modified UNIFAC method and found to fail dramatically, the calculated values being lower than the experimental ones by a factor ranging from 2 to 10. General lack of reliable limiting water activity coefficient data and their unreliable prediction indicate the significance of both the new method and the acquired data.
Compounds
# Formula Name
1 C2HCl3 trichloroethene
2 C7H8 toluene
3 C7H8O anisole
4 C8H10O ethoxybenzene
5 C7H7BrO 1-bromo-4-methoxybenzene
6 C7H5F3 (trifluoromethyl)benzene
7 C6H5Cl chlorobenzene
8 C6H5Br bromobenzene
9 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
  • 1
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 9; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 6
  • POMD
  • 2
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 9; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 6
  • POMD
  • 3
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 9; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 7
  • POMD
  • 4
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 9; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 6
  • POMD
  • 5
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 9; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 6
  • POMD
  • 6
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 9; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 6
  • POMD
  • 7
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 9; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 6
  • POMD
  • 8
  • 9
  • Activity coefficient - 9 ; Liquid
  • Temperature, K; Liquid
  • Mole fraction - 9; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Chemical equilibration / Heterogeneous equilibration
  • 6