Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Activity coefficients and partial molar excess enthalpies at infinite dilution for four esters in water

Dohnal, V.[Vladimir], Vrbka, P.[Pavel], Rehak, K.[Karel], Bohme, A.[Alexander], Paschke, A.[Albrecht]
Fluid Phase Equilib. 2010, 295, 2, 194-200
ABSTRACT
Infinite dilution activity coefficients of four esters, namely dimethyl carbonate, diethyl carbonate, vinyl acetate, and methyl methacrylate in water were measured at several temperatures in the range from 273 K to 333 K. The inert gas stripping technique, and for methyl methacrylate also the headspace analysis with solid-phase microextraction sampling, was employed for the purpose. Infinite dilution partial molar excess enthalpies of these aqueous solutes were further measured at several temperatures in the range from 288 K to 318 K using isothermal flow mixing microcalorimetry which allowed reliable derivation of respective heat capacities. For each ester, the data measured in this work together with those reported previously in the literature were correlated with a suitable model equation providing adequate simultaneous description of the equilibrium measurements and the calorimetric information. As a result, a recommended thermodynamically consistent temperature dependence of infinite dilution activity coefficients of superior accuracy was established. Analogous recommendations were derived also for the temperature dependence of the Henry's law constants (KH). In addition, literature data on mutual solubilities of esters and water were employed to calculate the infinite dilution activity coefficient values which in turn were compared with the recommended infinite dilution activity coefficient dependence on temperature.
Compounds
# Formula Name
1 C3H6O3 dimethyl carbonate
2 H2O water
3 C5H10O3 diethyl carbonate
4 C4H6O2 vinyl acetate
5 C5H8O2 methyl methacrylate
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
  • Activity coefficient - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Inert gas stripping
  • 8
  • POMD
  • 1
  • 2
  • Molar enthalpy of solution, kJ/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 1; Liquid
  • Liquid
  • Flow calorimetry
  • 4
  • POMD
  • 3
  • 2
  • Activity coefficient - 3 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Inert gas stripping
  • 8
  • POMD
  • 3
  • 2
  • Molar enthalpy of solution, kJ/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 3; Liquid
  • Liquid
  • Flow calorimetry
  • 4
  • POMD
  • 4
  • 2
  • Activity coefficient - 4 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Inert gas stripping
  • 8
  • POMD
  • 4
  • 2
  • Molar enthalpy of solution, kJ/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 4; Liquid
  • Liquid
  • Flow calorimetry
  • 7
  • POMD
  • 5
  • 2
  • Activity coefficient - 5 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • Headspace solid-phase microextraction
  • 3
  • POMD
  • 5
  • 2
  • Activity coefficient - 5 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • Inert gas stripping
  • 8
  • POMD
  • 5
  • 2
  • Molar enthalpy of solution, kJ/mol ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Mole fraction - 5; Liquid
  • Liquid
  • Flow calorimetry
  • 5