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

Solubilities and Thermodynamic Properties of NH3 in Glycerin and its Derivatives

Duan, Xiuzhi, Cui, Yanhong, Zhang, Chao, Gao, Bao, Deng, Dongshun
J. Chem. Eng. Data 2019, 64, 3, 1131-1139
ABSTRACT
The solubilities of ammonia (NH3) in glycerin (G) as well as its derivatives were measured at 303.15 K, 313.15 K, 323.15 K and 333.15 K under pressures up to 570.0 kPa using isochoric saturation method. Three glycerin derivatives include glycerol formal (GF), DL-1,2-isopropyli-deneglycerol (GAK), and 3-methoxy-1,2-propanediol (MP). Henry's constants and thermodynamic properties such as dissolution Gibbs free energy, enthalpy, and entropy changes of NH3 solvation were derived by fitting the experimental data. The results showed that the gravimetric solubilities of NH3 in these solvents changes along with the sequence of G greater than GF greater than MP greater than GAK. The solubility of NH3 in the solvents increased with the increasing pressure or the decreasing temperature. All the dissolving enthalpies were negative at each condition. The dissolution of NH3 was a spontaneous process. By comparative comparison of dissolving ability, properties, price and environmental impact between present solvents and other absorbents in the literatures, glycerin was believed as a potential NH3 captures in the industry.
Compounds
# Formula Name
1 H3N ammonia
2 C3H8O3 glycerol
3 C4H8O3 1,3-dioxolane-4-methanol
4 C4H8O3 1,3-dioxan-5-ol
5 C6H12O3 2,2-dimethyl-1,3-dioxolane-4-methanol
6 C4H10O3 3-methoxy-1,2-propanediol
7 C5H14ClNO choline chloride
8 CH4N2O urea
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
  • 2
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 1
  • POMD
  • 5
  • Viscosity, Pa*s ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 1
  • POMD
  • 4
  • 3
  • Viscosity, Pa*s ; Liquid
  • Mole fraction - 4; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Capillary tube (Ostwald; Ubbelohde) method
  • 1
  • POMD
  • 1
  • 2
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 38
  • POMD
  • 1
  • 5
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 36
  • POMD
  • 1
  • 6
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 38
  • POMD
  • 1
  • 4
  • 3
  • Mole fraction - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Mole fraction - 4; Liquid
  • Liquid
  • Gas
  • Phase equilibration
  • 36
  • POMD
  • 1
  • 7
  • 8
  • Molality, mol/kg - 1 ; Liquid
  • Temperature, K; Liquid
  • Pressure, kPa; Liquid
  • Solvent: Amount ratio of component to other component of binary solvent - 7; Liquid
  • Liquid
  • Gas
  • phase equilibration
  • 15