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

Solubilities of Sulfuryl Fluoride in 2-Butoxyethyl Acetate, 3-Methoxybutyl Acetate, 2-Methoxyethyl Acetate, 1-Methoxy-2-propyl Acetate, and 2-(2-Ethoxyethoxy)ethyl Acetate

Liang, Xiaojiang, Fei, Yanren, Xie, Qinglong, Lu, Meizhen, Pan, Zhiyan, Nie, Yong, Ji, Jianbing
J. Chem. Eng. Data 2018, 63, 6, 2271-2279
ABSTRACT
Large amount of sulfuryl fluoride (SO2F2) is released into atmosphere after fumigation, intensifying the greenhouse effect. Therefore, it is important to remove SO2F2 generated in fumigation. In this study, the solubilities of SO2F2 in 2-butoxyethyl acetate (BOEA), 3-methoxybutyl acetate (MOBA), 2-methoxyethyl acetate (MOEA), 1-methoxy-2-propyl acetate (MOPA), and 2-(2-ethoxyethoxy)ethyl acetate (DEOEA) were determined at T= (293.15 to 323.15) K and pressures up to about 600 kPa using isochoric saturation method. Results showed that SO2F2 solubility increased with increasing pressure and decreased with increasing temperature in the five acetate derivatives, and the dissolution of SO2F2 in these solvents belonged to a physical process. Furthermore, the Henry's law constants and thermodynamic properties including standard Gibbs free energy, enthalpy, and entropy changes of SO2F2 dissolution were further obtained. Compared with water, these five selected acetate derivatives showed potential application for SO2F2 removal. Moreover, the solubility of SO2F2 in these solvents followed the order of MOBA greater than MOPA greater than BOEA greater than DEOEA greater than MOEA.
Compounds
# Formula Name
1 CO2 carbon dioxide
2 F2O2S sulfuryl difluoride
3 C4H6O3 4-methyl-1,3-dioxolan-2-one
4 C8H16O3 2-butoxyethyl acetate
5 C7H14O3 3-methoxybutyl acetate
6 C5H10O3 2-methoxyethyl ethanoate
7 C6H12O3 1-methoxy-2-propyl acetate
8 C8H16O4 2-(2-ethoxyethoxy)ethyl acetate
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
  • 3
  • Mole fraction - 1 ; Liquid
  • Pressure, kPa; Liquid
  • Temperature, K; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 14
  • POMD
  • 2
  • 4
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 44
  • POMD
  • 2
  • 5
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 44
  • POMD
  • 2
  • 6
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 44
  • POMD
  • 2
  • 7
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 44
  • POMD
  • 2
  • 8
  • Mole fraction - 2 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 44